AUTHOR OF THIS BLOG

DR ANTHONY MELVIN CRASTO, WORLDDRUGTRACKER

New FDA Guidance on Completeness Assessements for Type II API Drug Master Files

 regulatory  Comments Off on New FDA Guidance on Completeness Assessements for Type II API Drug Master Files
Mar 172016
 

Since 1st October 2012, special regulations have been applying to the US Type II Drug Master Files. This year in February, the FDA published a new Guidance for Industry. Read here what the DMF holder has to consider when submitting data about the API Drug Master File.

http://www.gmp-compliance.org/enews_05256_New-FDA-Guidance-on-Completeness-Assessements-for-Type-II-API-Drug-Master-Files_15328,15339,S-WKS_n.html

Since the coming into force of the “Generic Drug User Fee Act” (GDUFA) on 1st October 2012, special regulations have been applying to the submission to the FDA of a Drug Master Files for a pharmaceutical API (Type II DMF). The DMF holder must pay a one-time fee when authorising the reference of his/ her DMF in an application for a generic drug (Abbreviated New Drug Application, ANDA). Moreover, the DMF will undergo a completeness assessment through the FDA.

This year in February, the FDA published a Guidance for Industry entitled “Completeness Assessments for Type II API DMFs under GDUFA” which provides DMF holders with comprehensive information regarding the application for a Type II DMF. The document describes the criteria according to which the FDA performs a completeness assessment and which data are expected.

This completeness assessment does not replace the full scientific assessment to be executed at a later time. It serves to find out whether the data contained in the DMF are sufficient for the ANDA. In a completeness assessment, the following elements are examined:

  • Is the DMF active?
  • Has the fee been paid?
  • Has the DMF been previously reviewed?
  • Does the DMF pertain to a single API?
  • Does the DMF contain certain administrative information?
  • Does the DMF contain all the information necessary to enable a scientific review?
  • Is the DMF written in English?

The Guidance contains a checklist (Appendix 1) listing the criteria according to which the FDA performs the assessment. For the DMF holder, this list is helpful to check the completeness of his/ her data before submitting them to the FDA.

One essential element underlined in this Guidance is to pay the DMF fee in due time (at least 6 months prior to the submission of an ANDA). The FDA won’t continue to process the DMF as long as the fee hasn’t been paid. If the applicant of an ANDA references in his dossier a DMF for which a fee is due, the FDA will inform him. If the fee hasn’t been paid within 20 days after notification, the FDA will stop the further processing of the application.

When submitting a DMF, the form “FDA 3794″ (Generic Drug User Fee Cover Sheet) should be attached. It contains the minimum information required by the FDA to determine whether the DMF holder has satisfied his fee obligations.

After the successful completeness assessment of a DMF, a number will be attributed and posted on a publicly available API DMF list. The FDA has compiled all important information regarding DMFs Type I-V on the Drug Master File webpage. Here, you can also find the list of all active DMFs.

 

 

//////API Drug Master File, fda, type2

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Current Practices of Process Validation for Drug Substances and Intermediates

 PROCESS, regulatory  Comments Off on Current Practices of Process Validation for Drug Substances and Intermediates
Jan 132016
 
Abstract Image

Process validation includes laboratory optimization, pilot-plant introduction, and process implementation on manufacturing scale, as well as monitoring batches after implementation and continuously improving the manufacturing processes. There are many opportunities to change and optimize operations. The background information in this contribution describes current guidance and terminology for validation, including the integration of validation over the development lifecycle of drug substances. Various examples illustrate challenges and success stories of implementation as part of the overall approach to process validation.

 

Current Practices of Process Validation for Drug Substances and Intermediates

Anderson’s Process Solutions, 7400 Griffin Lane, Jacksonville, Oregon 97530, United States, Creative Innovation Partners, 1971 Western Avenue, Albany, New York 12203, United States, and Rib-X Pharmaceuticals Inc., 300 George Street, New Haven, Connecticut 06511, United States
Org. Process Res. Dev., 2011, 15 (1), pp 162–172
DOI: 10.1021/op1002825
Publication Date (Web): December 21, 2010
Copyright © 2010 American Chemical Society
* To whom correspondence should be addressed: E-mail: nganderson@dishmail.net., †

Creative Innovation Partners., ‡Rib-X Pharmaceuticals Inc.

http://pubs.acs.org/doi/abs/10.1021/op1002825

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Indian Generics 2016

 PROCESS, regulatory  Comments Off on Indian Generics 2016
Aug 032015
 

 

The generic APIs market is expected to continue to rise faster than the branded/innovative APIs, by 7.7%/year to reach $30.3 billion in 2016. Asia-Pacific is expected to show the fastest growth rates (10.8%/year). The 24 fastest growing markets will include 11 in Asia-Pacific, seven in Eastern Europe and CIS, four in Africa-Middle East and two in Latin America (Figure ).

Figure  – Top growth markets for generic APIs to 2016

By 2016, China will account for 27.7% of the global generic API merchant market, while the US will have fallen to 23.8%; the mature markets as a whole will see their share fall from 41.8% in 2012 to 36.9%. India will be the third largest, with a 7.2% share.

 

 

 

 

 

101st Anniversary of the First Electric Traffic Signal System

 

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GMP IN AN API PILOT PLANT

 regulatory  Comments Off on GMP IN AN API PILOT PLANT
Jul 102015
 

 

GMP……API PILOT PLANT

PRESENTATION

 

Pilot plant and scale-up techniques are both integral and critical to drug discovery and development process for new medicinal products. A major decision focuses on that point where the idea or process is advanced from a research oriented program targeted towards commercialization.

The speed of drug discovery has been accelerating at an exponential rate. The past two decades particular have witnessed amazing inventions and innovations in pharmaceutical research, resulting in the ability to produce new drugs faster than even before.

The new drug applications (NDAs) and abbreviated new drug applications (ANDA) are all-time high. The preparation of several clinical batches in the pilot plant provides its personnel with the opportunity to perfect and validate the process. Also different types of laboratories have been motivated to adopt new processes and technologies in an effort to stay at the forefront scientific innovation.

 MY PRESENTATION

 

 

Pharmaceutical pilot plants that can quickly numerous short-run production lines of multiple batches are essential for ensuring success in the clinical testing and bougainvilleas study phases. Drug formulation research time targets are met by having a well-designed facility with the appropriate equipment mix, to quickly move from the laboratory to the pilot plant scale 1. In pilot plant, a formula is transformed into a viable, robust product by the development of a reliable and practical method of manufacture that effects the orderly transition from laboratory to routine processing in a full scale production facility where as the scale up involves the designing of prototype using the data obtained from the pilot plant model.

Pilot plant studies must includes a close examination of formula to determine its ability to withstand batch-scale and process modifications; it must includes a review of range of relevant processing equipment also availability of raw materials meeting the specification of product and during the scale up efforts in the pilot plant production and process control are evaluated, validated and finalized.

pilot pic 12

In addition, appropriate records and reports issued to support Good Manufacturing Practices and to provide historical development of the production formulation, process, equipment train, and specifications

A manufacturer’s decision to scale up / scale down a process is ultimately rooted in the economics of the production process, i.e., in the cost of material, personnel, and equipment associated with the process and its control.

 When developing technologies, there are a number of steps required between the initial concept and completion of the final production plant. These steps include the development of the commercial process, optimization of the process, scale-up from the bench to a pilot plant, and from the pilot plant to the full scale process. While the ultimate goal is to go directly from process optimization to full scale plant, the pilot plant is generally a necessary step.

Reasons for this critical step include: understanding the potential waste streams, examination of macro-processes, process interactions, process variations, process controls, development of standard operating procedures, etc. The information developed at the pilot plant scale allows for a better understanding of the overall process including side processes. Therefore, this step helps to build the information base so that the technology can be permitted and safely implemented.

Should be versatile pilot plant that is entirely GMP and facilitates the development of API’s in scalable, safe and environmentally friendly ways.

pilot pic 6

The combination of  facilities,  experience and flexibility enable  an integral Contract Manufacturing service ranging from laboratory to industrial scale; it should manufacture under regulation small amounts of high added value active substances or key intermediate products.

pilot pic 4

 

pilot pic 5

Product quality: Operations that depend on people for executing manual recipes are subject to human variability. How precisely are the operators following the recipe? Processes that are sensitive to variations in processing will result in quality variation. Full recipe automation that controls most of the critical processing operations provides very accurate, repeatable material processing. This leads to very highly consistent product quality.

pilot pic 11

 Improved production: Many biotech processes have extremely long cycle times (some up to 6 months), and are very sensitive to processing conditions. It is not uncommon for batches to be lost for unexplained reasons after completing a large portion of the batch cycle time. The longer the batch cycle time and the more sensitive production is to processing conditions, the more batch automation is justified. Imagine losing a batch of very valuable product because the recipe was not precisely followed!

 Process optimization: Increasing the product yield can be done by making small changes in processing conditions to improve the chemical conversions or biological growth conditions. Manual control offers a limited ability to finely implement small changes to processing conditions due to the inherent lack of precision in human control. Conversely, computers are very good at controlling conditions precisely. In addition, advanced control capabilities such as model predictive control can greatly improve process optimization. This results in higher product yield and lower production cost. This consideration is highly relevant to pilot plant facilities where part of the goal is to learn how to make the product.

 Recordkeeping: A multi-unit recipe control system is capable of collecting detailed records as to how a batch was made and relates all data to a single batch ID. Data of this nature can be very valuable for QA reporting, QA deviation investigations, and process analysis.

 Safety: Operators spend less time exposed to chemicals when the process is fully automated as compared to manual control. Less exposure to the process generally results in a safer process.

A good batch historian should be able to collect records for a production run to include the following information:  Product and recipe identification

 User defined report parameters

 Formulation data and relevant changes

 Procedural element state changes (Operations, unit procedures, procedures)

 Phase state changes

 Operator changes

 Operator prompts and responses

 Operator comments

 Equipment acquisitions and releases

 Equipment relationships

 Campaign creation data (recipe, formula values, equipment, etc.)

 Campaign modifications

 Campaign execution activity

 Controller I/O subsystem events from the Continuous Historian

 Process alarms

 Process events

 Device state changes.

 

Raw materials

Buildings and facilities. GMPs under the 21 Code of Federal Regulations (CFR) Part 211.42 state that buildings or areas used in the receiving, storage, and handling of raw materials should be of suitable size, construction and location to allow for the proper cleaning, maintenance, and operation (7). The common theme for this section of CFR Parts 210 and 211 is the prevention of errors and contamination. In principle, the requirements for buildings and facilities used in early phase manufacturing are not significantly different than those for later phases or even commercial production. However, there are some areas that are unique to early clinical trial manufacturing.

Control of materials. The CFR regulations under Part 211.80 provide good direction with respect to lot identification, inventory, receipt, storage, and destruction of materials (7). The clear intent is to ensure patient safety by establishing controls that prevent errors or cross-contamination and ensure traceability of components from receipt through clinical use. In general, the requirements for the control of materials are identical across all phases of development, so it is important to consider these requirements when designing a GMP facility within a laboratory setting.

Combination Glass/Glass-lined reactors

For example, all materials must be assigned a unique lot number and have proper labeling. An inventory system must provide for tracking each lot of each component with a record for each use. Upon receipt, each lot should be visually examined for appropriate labeling and for evidence of tampering or contamination. Materials should be placed into quarantine or in the approved area or reject area with proper labeling to identify the material and prevent mix-ups with other materials in the storage area. Provision should be made for materials with special storage requirements (e.g., refrigeration, high security). The storage labeling should match the actual conditions that the material is being stored and should include expiry/retest dates for approved materials. Although such labeling is inconvenient for new materials where the expiration or retest date may change as more information is known, this enables personnel to be able to determine quickly whether a particular lot of a material is nearing or exceeding the expiration or retest date. General expiry/retest dates for common materials should be based on manufacturer’s recommendation or the literature.

Finally, there are clear regulatory and environmental requirements for the destruction of expired or rejected materials. It is important to observe regional and international requirements regarding the use of animal sourced materials (12). It is recommended to use materials that are not animal sourced and that there be available certification by the raw material manufacturers that they contain no animal sourced materials. If animal sourced raw materials must be used, then certifications by the raw material manufacturers that they either originate from certified and approved (by regulatory bodies) sources for use in human pharmaceuticals, or that the material has been tested to the level required for acceptance by regulatory agencies (following US, EU, or Japanese guidelines, as applicable) is required.

Direct advantages for customers 

  • Shorter implementation time for product by determination of the product suitability as well as the necessary process cycle
  • Optimized adjustment of the processing times in the production lines (trains) by relatively precise estimation of the drying times
  • Definition of effective cleaning processes (CIP/WIP and SIP)
  • Definition of the selection criteria based on the weighting of the customer, e.g.: drying time, quality (form of crystal, activity, etc.), cleanout, ability of CIP, price

 

An overview of further trials and test functions, that can be realized in the new pilot plant facility:

  • Product tests for determination of suitability
  • Scale-up tests as basis for the extrapolation on production batches regarding drying time, filling degree, crystalline transformation and grain spectrum
  • Optimization of the process cycle
  • Optimization of the machine
  • Data acquisition and analysis

SEE THIS SECTION IN ACTION…………..KEEP WATCHING

Case study 1

Designed and equipped for the manufacturing of solid oral dosage form
Hammann

PlantaFabri

Designed and equipped for the manufacturing of solid oral dosage forms, specialized in high-activity substances (cytostatic, cytotoxic, hormonal, hormone inhibitors). It has ancillary areas for the proper management of materials intended for clinical trials of new drugs.

Equipment:

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CASE STUDY 2

OPERATION OF PILOT PLANT FOR CLINICAL LOTS OF BIOPHARMACEUTICALS

http://www.peq.coppe.ufrj.br/biotec/presentations/Papamichael_RioDeJaneiro2009_secure.pdf

 

pilot pic

 

pilot pic 2

 

pilot pic 3

 

 

pilot pic 7

 CASE STUDY 3

Good Manufacturing Practices in Active Pharmaceutical Ingredients Development

 http://apic.cefic.org/pub/5gmpdev9911.pdf

Example below

3. Introduction Principles basic to the formulation of this guideline are: ·

Development should ensure that all products meet the requirements for quality and purity which they purport or are represented to possess and that the safety of any subject in clinical trials will be guaranteed. ·

During Development all information directly leading to statements on quality of critical intermediates and APIs must be retrievable and/or reconstructable. ·

The system for managing quality should encompass the organisational structure, procedures, processes and resources, as well as activities necessary to ensure confidence that the API will meet its intended specifications for quality and purity. All quality related activities should be defined and documented. Any GMP decision during Development must be based on the principles above.

During the development of an API the required level of GMP control increases. Using these guidelines, the appropriate standard may be implemented according to the intended use of the API. Firms should apply proper judgement, to discern which aspects need to be addressed during different development stages (non-clinical, clinical, scale-up from laboratory to pilot plant to manufacturing site).

Suppliers of APIs and/or critical intermediates to pharmaceutical firms should be notified on the intended use of the materials, in order to apply appropriate GMPs. The matrix (section 8) should be used in conjunction with text in section 7, as is only intended as an initial guide.  READ MORE AT….  http://apic.cefic.org/pub/5gmpdev9911.pdf

 

CASE STUDY 4

http://www.steroglass.it/doc_area_download/ita/process/20LT_PILOT_PLANT.pdf

pilot pic 8

 

 

CASE STUDY 5

 

Health Canada

http://www.hc-sc.gc.ca/dhp-mps/compli-conform/gmp-bpf/question/gmp-bpf-eng.php

The Good Manufacturing Practices questions and answers (GMP Q&A) presented below have been updated following the issuance of the “Good Manufacturing Practices Guidelines, 2009 Edition Version 2 (GUI-0001)“.

This Q&A list will be updated on a regular basis.

Premises – C.02.004

Equipment – C.02.005

Personnel – C.02.006

Sanitation – C.02.007 & C.02.008

Raw Material Testing – C.02.009 & C.02.010

Manufacturing Control – C.02.011 & C.02.012

Quality Control Department – C.02.013, C.02.014 & C.02.015

Packaging Material Testing – C.02.016 & C.02.017

Finished Product Testing – C.02.018 & C.02.019

Records – C.02.020, C.02.021, C.02.022, C.02.023 & C.02.024

Samples – C.02.025 & C.02.026

Stability – C.02.027 & C.02.028

Sterile Products – C.02.029

 

 

 

CASE STUDY 6

CASE STUDY 7

 

 http://www.niper.gov.in/tdc_2013.pdf

 

 

 

CASE STUDY 8

Multi-kilo scale-up under GMP conditions

Examples of flow processes being used to produce exceptionally large amounts of material are becoming increasingly common as industrial researchers become more knowledgeable about the benefits of continuous reactions. The above examples from academic groups serve to illustrate that reactions optimized in small reactors processing tens to hundreds of mg hour−1 of material can be scaled up to several grams per hour. Projects in process chemistry are often time-sensitive, however, and production of multiple kg of material may be needed in a short amount of time. An example of how the efficient scaling of a flow reaction can save time and reduce waste is provided by a group of researchers at Eli Lilly in their kg synthesis of a key drug intermediate under GMP conditions . In batch, ketoamide 13 was condensed with NH4OAc and cyclized to form imidazole 14 at 100 °C in butanol on a 1 gram scale. However, side product formation became a significant problem on multiple runs at a 250 g scale. It was proposed that this was due to slow heat up times of the reactor with increasing scale, as lower temperatures seemed to favour increased degradation over productivecyclization. Upon switching to a 4.51 mL flow reactor, another optimization was carried out which identified methanol as a superior solvent that had been neglected in batch screening due to its low boiling point at atmospheric pressure. Scale-up to a 7.14 L reactor proceeded smoothly without the need for reoptimization, and running on this scale with a residence time of 90 minutes for a six-day continuous run provided 29.2 kg of product after recrystallization (approximately 207 g hour−1). The adoption of a flow protocol by a group of industrial researchers in a scale-up with time constraints demonstrates both the effectiveness and maturity of flow chemistry. While the given reaction was used to produce kilograms of material for a deadline, continuous operation without further optimization could produce over 1 metric tonne of product per year in a reactor that fits into a GC oven.

Kilogram-scale synthesis of an imidazole API precursor.
Scheme 20 Kilogram-scale synthesis of an imidazole API precursor.

 

 

 

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Definitions

Plant:  A plant is a place where an industrial or manufacturing process takes place. It may also be expressed as a place where the 5 M’s that are; man, materials, money, method and materials are brought together for the manufacture of products.

Pilot Plant: A part of a manufacturing industry where a laboratory scale formula is transformed into a viable product by development of reliable practical procedures of manufacturing.

Scale-Up: This is the art of designing a prototype based on the information or data obtained from a pilot plant model.

cGMP: current Good Manufacturing Processes refer to an established system of ensuring that products are consistently produced and controlled according to quality standards. It is designed to minimize risk involved in any industrial design. GMP covers all aspects of production from the starting materials, premises and equipment to the training and personal hygiene of staff within industries. Detailed, written procedures are essential for each process that could affect the quality of the finished product. There must be a system to provide documented proof that correct procedures are consistently followed at each step in the manufacturing process every time a product is made.

SCALING UP FROM PILOT PLANTS

When scaling up, it is of utmost importance to consider all aspects of risk and futuristic expansion. The pilot plant is usually a costly apparatus and therefore the decision of building it is always a hard one. The function of a pilot plant is not just to prove that the laboratory experiments work, but;

  1. To test technologies that are about to be implemented on industrial plants before establishment
  2. To evaluate performance specifications before the actual installation of industrial plant.
  3. Evaluation of reliability of mathematical models within real environment.
  4. Economic considerations for production involving process optimization and automated control systems.

GMP GENERAL PRACTISES

Facilities and Equipment Systems

  • Ø Cleaning and maintenance
  • Ø Facility layout and air handling systems for prevention of cross-contamination (e.g. Penicillin, beta-lactams, steroids, hormones, cytotoxic, etc.)
  • Ø Specifically designed areas for the manufacturing operations performed by the firm to prevent contamination or mix-ups.

Facilities

  • Ø General air handling systems
  • Ø Control system for implementing changes in the building
  • Ø Lighting, potable water, washing and toilet facilities, sewage and refuse disposal
  • Ø Sanitation of the building, use of rodenticides, fungicides, insecticides, cleaning and sanitizing agents. 

GMP FOR PLANT DESIGN

The application of GMP to plant design is primary to the establishment of such plants. Regulatory boards have precedence over these operations helping to establish a proper and functional system in plant design.

Design Review

l  Conceptual drawings;

From plant design drawings which are inspected and approved by cGMP regulatory bodies (such as Department of Petroleum Resources in Nigeria), approvals are issued depending on adherence to specifications such as muster points, proper spacing of fuel sources from combustion units and other more elaborate considerations.

l  Proposed plant layouts;

A choice of location for plant and layout play an important role on environmental impact. Hence, environmental impact assessment is a major part of GMP. Industries must be located at least 100M from closest residential quarter (depending of materials processed in plant).

l  Flow diagrams for facility

For optimization and efficiency purposes, flow diagrams for complete refinery process are important for review with intent to ensure they conform to GMP

l  Critical systems and areas

Some areas in a plant may require extra safety precautions in operations. The cGMP makes provision for such special considerations with the creation of customized set of operational guidelines that ensure safety and wellness of staff and environment alike.

cGMP EXAMPLE:  FOOD PROCESSING PLANT

Outlined below are the cGMP considerations in the establishment and handling of a food processing plant.

Safety of Water

1. Process water is safe, if private supply should be tested at least annually.

2. Backflow prevention by an air gap or back flow prevention device. Sinks that are used to prepare food must have an air-gap. 

Food Contact Surface

1. Designed, maintained, and installed so that it is easy to clean and to withstand the use, environment, and cleaning compounds.

2. If cleaning is necessary to protect against microorganisms, food-contact surfaces shall be cleaned in this sequence: wash with detergent, rinse with clear water, and then use an approved sanitizer. The sanitizer used shall be approved for use on food-contact surfaces. UA three-compartment ware washing sink or other equivalent methods shall be used for this purpose.

3. Gloves shall be clean/sanitary. Outer garments suitable.

Prevention of Cross-Contamination

1. Food handlers use good hygienic practices; hands shall be washed before starting work, after absence from work station, or when they become contamination (such as with eating or smoking).

2. Signs shall be posted in processing rooms and other appropriate areas directing employees that handle unprotected food, food-contact surfaces, food packaging materials to wash their hands prior to starting to work, after each absence from the work station, and whenever hands may become contaminated.

3. Plant design so that the potential for contamination of food, food-contact surfaces, or packaging materials is reduced to the extent possible.

4. Physical separation of raw and finished products. 

Hand Washing Sinks and Toilet Facilities

1. Hand washing sinks, properly equipped, shall be conveniently located to exposed food processing areas. Ware washing sinks shall not be used for this purpose.

2. Adequate supply of hot and cold water under pressure.

3. Toilet facilities; adequate and accessible, self-closing doors.

4. Sewage disposal system shall be installed and maintained according to State law.

Protection from Adulteration (Food, Food Contact Surfaces, and Packaging Materials)

1. Food processing equipment designed to preclude contamination with lubricants, fuel, metal fragments, contaminated water, or other sources of contamination.

2. Food processed so that production methods to not contaminate the product.

3. Raw materials, works-in-process, filling, assembly, packaging, and storage and transportation conducted so that food is not contaminated.

4. Protection from drip and condensate overhead.

5. Ventilation adequate and air not blown on food or food-contact surfaces.

6. Lights adequately shielded.

7. Compressed air or gas mechanically introduced adequately filtered. 

Scope of services

  • Engineering support
  • Representation of the construction owner (equipment, construction: supervision of general contractors, GMP concept draft)
  • Basic and detailed design
  • Support during the implementation phase
  • Clean room planning (incl. lab areas)
  • Construction management
  • Qualification
  • Validation support

Toxic Items: Labelling, Use, and Storage

1. Products used approved and used according to product’s label.

2. Sanitizer used on food-contact surfaces must be approved for that use.

3. Shall be securely stored, so unauthorized use is prevented.

Personnel Disease Control

1. Food handler, who has illness or open lesion, or other source of microbiological contamination that presents a reasonable possibility of contamination of food, food-contact surfaces, or packaging materials shall be excluded from such operations.

2. Adequate training in food protection, dangers of poor personal hygiene, and unsanitary practices shall be provided.

3. Management shall provide adequate supervision and competent training to ensure compliance with these provisions.

Pest Control

1. Management shall provide an adequate pest control program so that pests are excluded from the plant.

2. Program shall ensure that only approved pesticides are used and applied per the product’s label. 

Plant Construction and Design

1. Walls, floors, and ceilings constructed so that they can be adequately cleaned and kept in good repair.

2. Adequate lighting provided.

3. Adequate ventilation or controls to minimize odours and vapours.

4. Adequate screening or protection of outer openings.

5. Grounds maintained free of litre, weeds, and pooling water.

6. Roads, yards, and parking lots maintained so that food is not contaminated.

Equipment

1. Equipment, utensils, and seams on equipment – adequately cleanable, properly maintained, designed, and made of safe materials.

2. Refrigerators and freezers equipped with adequate thermometer.

3. Instruments and control devices – accurate and maintained.

4. Compressed air or gas designed/treated so that food is not contaminated.

Equipment. Most equipment used to manufacture early GMP drug product is be managed under a qualification, preventive maintenance, and calibration program for the GMP facility. However, in early development, there may occasionally be a need to use equipment that is not part of such a program. Rather than performing a comprehensive qualification for a piece of equipment not expected to be frequently used, an organization may choose to qualify it for a single step or campaign. Documentation from an installation qualification/operational qualification (IQ/OQ) and or performance verification at the proposed operating condition is sufficient. For example, if solution preparation needs a mixer with a rotation speed of 75 rpm, then documentation in the batch record using a calibrated tachometer to verify that the mixer was operating at 75 rpm will suffice.

The use of dedicated or disposable equipment or product contact parts may be preferable to following standard cleaning procedures to ensure equipment is clean and acceptable for use. However, not all equipment or equipment parts are disposable or may have a substantial cost that makes disposal prohibitive. In that case, the product contact parts could be dedicated to a specific drug substance for use in drug product manufacture. Dedicating product contact parts to a compound may be costly and may be avoided in some cases by carefully considering product changeover and effective cleaning methods when purchasing equipment.

Another item to consider with respect to equipment, is that the more complicated the equipment is to run or maintain, the less desirable it might be for early GMP batches. In most cases, simple equipment is adequate and will uses less material and consume less total time for preparation, operation, and cleaning activities.

Weights and Measures

1. Scales used to measure net weight of contents shall be designed so they can be calibrated.

2. Products in interstate commerce – net weights/measurements also in metric.

 

CONCLUSION

Plant establishment is an activity that has kept rising from the inception of the industrial revolution until date. Giving rise to increase in raw material demand, increased pollution levels, higher energy demand, and overall greater economic output. As history and record keeping has served for an even longer period, it becomes necessary for adaptation to be made to avoid incidents and accidents that have occurred previously and also those that can be anticipated without actual devastating effect.

The development of the GMP is as a result of observed challenges in industry and environment over years of industrialization. It becomes necessary to upset these poor trends that have developed as a result of industrialization by so doing increasing the pros and reducing the cons.

GMP protects consumer, produce, equipment, and conserves the processes as a whole, leading to a more efficient sustainable process defining a new standard for yields and profit and eliminating the tendency of compromise made by industrialists to increase overall profits at the risk of staff and environment.

pilot pic 9

 

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Batch documentation and execution

Batch record documentation preparation. Manufacturing documentation is a basic requirement for all phases of clinical development. 21 CFR Parts 211.186 and 211.188 describe master production and batch production records, respectively (7). The stated purpose of the master production record is to “assure uniformity from batch to batch.” Although the record assurance is important for a commercial validated manufacturing process, it does not necessarily apply to clinical-development batches. Material properties, manufacturing scale, and quality target product profile frequently change from batch to batch. Therefore, batch production records are the appropriate documentation for clinical trial supplies. Batch production records for Phase 1 materials should minimally include:

  • Name, strength, and description of the dosage form
  • A complete list of active and inactive ingredients, including weight or measure per dosage unit and total weight or measure per unit
  • Theoretical batch size (number of units)
  • Manufacturing and control instructions.

These minimum requirements are consistent with the FDA Guidance for Industry: cGMP for Early Phase Investigational Drugs, which requires a record of manufacturing that details the materials, equipment, procedures used and any problems encountered during manufacturing (2). The records should allow for the replication of the process. On this basis, there is flexibility in the manner for which documentation of batch activities can occur, provided that the documentation allows for the post execution review by the quality unit and for the retention of these records.

 

Batch documentation approvals. Review and approval of executed batch records by the Quality unit is required per 21 CFR Part 211.192 (7). This review and approval is required for all stages of clinical manufacturing. Pre-approvals of batch records should be governed by internal procedures as there is no requirement in CFR 21 that the Quality unit pre-approves the batch record (though this is highly recommended in order to minimize the chance of errors). Indeed, Table I shows that pre-approval of batch records by the Quality Unit is practiced by all 10 companies that participated in the IQ Consortium’s drug-product manufacturing survey related to early development. Batch records must be retained for at least 1 year after the expiration of the batch according to CFR Part 211.180, but many companies keep their GMP records archived for longer terms.

Room clearance. 21 CFR Part 211.130 requires inspection of packaging and labeling facilities immediately before use to ensure that all drug products from previous operations have been removed. This inspection should be documented and can be performed by any qualified individual.

Although line clearance for bulk manufacture is not specifically mentioned in the CFR, it is expected that a room clearance be performed. At a minimum, this clearance should be performed prior to the initiation of a new batch (i.e., prior to batch materials entering a processing room).

Hold time. During the early stages of development, final dosage form release testing confirms product quality and support establishment of hold times later in the clinical development. There is no requirement to establish hold times for work in process in early development. Specific formulation and stability experience, which is usually limited at this stage of development, should be leveraged to assess any substantial variations from expected batch processing times. The data gathered from these batches and subsequent development can be used to help establish hold times for future batches. (Exceptions to this approach may include solution or suspension preparations used in solid dosage form manufacturing, where procedures typically govern allowable hold times to ensure the absence of microbial contamination in the final product.)

Change control. Changes to raw materials, processes, and products during early development are inevitable. It is not required that these changes be controlled by a central system but rather may be appropriately documented in technical reports and manufacturing batch records. Any changes in manufacturing process from a previous batch should be captured as part of the batch record documentation and communicated to affected areas. The rationale for these changes should also be documented as this serves as a source for development history reports and for updating regulatory filings. The authors recommend that those changes that could affect a regulatory filing be captured in a formal system.

Process changes. Process parameters should be recorded but do not need to be predetermined because processes may not be fixed or established in early development. Given the limited API availability in early development, a clinical batch is often the first time a product is manufactured at a particular scale or using a particular process train. Therefore, process changes should be expected. Process trains and operating parameters must be documented in the batch record but changes should not trigger an exception report or CAPA. Changes should be documented as an operational note or modification to the batch record in real time. Such changes driven by technical observations should not require prior approval by the Quality unit, but should have the appropriate scientific justification (via formulator/scientist) or the appropriate flexibility built into the batch record to allow for the changes. This documentation should be available for Quality review prior to product disposition.

Calculation of yield. Actual yields should be calculated for major processing steps to further process understanding and enable optimization of processes. Expected yield tolerances are not always applicable to early development manufacture. At this stage of early development, when formulation and process knowledge is extremely limited, there may be no technical basis for setting yield tolerances and, therefore, this yield may not be an indicator of the quality of the final product.

In-process controls and R&D sampling. In-process tests and controls should follow basic requirements of GMPS to document consistency of the batch. For capsule products, these requirements may include capsule weights and physical inspection. For tablet products, compression force or tablet hardness and weights should be monitored together with appearance. R&D sampling, defined as samples taken for purposes of furthering process understanding but not utilized for batch disposition decisions, is a normal part of all phases of clinical manufacturing. In early development manufacturing, a sampling plan is required for in-process control tests, but not for R&D samples. However, for the purpose of material accountability, R&D sampling should be documented as part of batch execution. For these samples, testing results may be managed separately, and are not required to be included in regulatory documentation.

Facilities and equipment

Regardless of the scale of manufacturing, the facility used for manufacturing clinical trial supplies must meet the basic GMP requirements as described in the regulations and guidance documents. Below are three scenarios for early development and the advantages of each as pertaining to early development. The first involves a pilot plant facility designed and equipped for routine GMP operations. The second scenario aims to establish a GMP area within a laboratory environment. The third example focuses on conducting GMP manufacturing or leveraging the practice of pharmacy in close proximity to the clinical site.

GMP facility for drug-product manufacture. The traditional approach in GMP drug-product manufacture is to use a dedicated facility (often called a pilot plant) for early phase clinical trials. Advantages of this approach include that the quality systems for the facility (i.e., maintenance, calibration, cleaning, change management, CAPA, and documentation) are well defined, and that training and other activities required for maintaining GMP compliance are centralized. Other drivers to use a pilot plant in early development may be the need for specialized equipment, or larger batch sizes in special situations.

GMP area within a laboratory setting. In some cases, it may be advantageous to establish a GMP area within a “laboratory setting” (i.e., a drug-development facility not dedicated to the production of clinical supplies) for the manufacture of drug product in early development. The rationale for this approach might be to avoid the significant investment in setting up a dedicated facility and to create simpler, more flexible systems that meet GMP requirements but are tailored for the specific activity envisioned. Examples where this approach might be considered include the need for special containment not available in the pilot-plant; the need to work with radioactive or hazardous materials, use of controlled substances and the production of “one-off manufactured” product used for proof of concept. The business rationale should be documented and approved by the manufacturing and Quality groups. As long as the appropriate GMP controls are maintained, especially as related to operator safety, cleaning, and prevention of cross-contamination, there is no compliance barrier to using “lab-type” facilities for the manufacturing of early phase clinical batches. Before GMP manufacturing is initiated, however, a risk assessment should be conducted and documented. Inclusion of representatives from Quality, analytical, clinical manufacturing, product development, and environmental health and safety would be prudent. When selecting/designing an early development clinical manufacturing facility, consideration should be made for the receipt, storage, dispensing, and movement of materials. The manufacturing processes in the nondedicated area must protect the product, patient, and the manufacturing operators.

Additionally, companies should consider what items are appropriate for the manufacture. For example, the use of a certified laminar flow hood may be a better choice for manufacturing than a fume hood, because the former is designed to prevent contamination of the product, protect the operator, and the laboratory environment. In addition, with the appropriate cleaning, a laminar flow hood can more easily be used for multiple products. Small scale/manual equipment or procedures may be the best approach because the space is likely to be limited. With a small batch size, the use of small scale or manual equipment/procedures will minimize yield loss. Additional measures to be assessed include appropriate gowning and operator personal protection devices, area and operator monitoring for potent or radiolabeled drug exposure, and so forth.

Documentation of the facility preparation, product manufacture, and the return of the facility to the previous state, if needed, is recommended. This documentation should describe the rationale for the manufacture in the nondedicated area, risk assessment, preparation of the area, cleaning procedures, and list of responsible persons. This documentation can reference existing procedures or standard operating procedures (SOPs) along with documents associated with the meetings and preparation for the manufacture of the batch. Batch records and cleaning records should be part of the documentation and should follow the company’s data-retention policy.

Receipt and approval

Specifications. It is a GMP requirement that all raw materials for the manufacture of drug product have appropriate specifications to ensure quality. The compendial requirements should be used for setting specifications provided the material is listed in at least one pharmaceutical compendium (e.g., US, European, and Japanese Pharmacopeias). It is important that the use of materials meeting the requirements of a single compendium is acceptable for use in early phase clinical studies conducted in the US, Europe, and Japan. For example, a material that meets USP criteria and is used in the manufacture of a drug product should be acceptable for use in early clinical studies in the European Union. In the absence of a pharmaceutical compendium monograph, the vendor specification and/or alternative compendial specifications such as USP’s Food Chemical Codex should guide specification setting. In any case, the sponsor is responsible for the establishment of appropriate specifications. Therefore, it is the authors’ position that good practice is to have at least a basic understanding of the manufacture, chemistry, and toxicology of the materials to guide appropriate specification setting.

Material testing and evaluation. The minimum testing required for incoming materials is visual inspection and identification. However, as mentioned above, the appropriate tests should be determined for the material based on the knowledge of the manufacture, chemistry, and toxicology. If the vendor is qualified, then the certificate of analysis may be acceptable in conjunction with the visual inspection and identification testing (see “Vendor Qualification” section below).

Approval for use. Ideally, manufacture of a bulk drug product should begin with approved material specifications and with materials that are fully tested and released. However, there are circumstances where it may not be feasible to start manufacture with approved specifications and fully tested and released materials, including API. Manufacturing prior to final release (sometimes called manufacturing “at risk”) may be acceptable, however, because the quality system ensures that all specifications are approved, test results are within specifications, and all relevant documents are in place before the product is released for administration to humans. The “risk” must lie fully with the manufacturer and not with the patient.

Vendor qualification. Vendors supplying excipients, raw materials, or API must be qualified by the sponsor. Appropriate qualification should depend on the stage of development and an internal risk assessment. For, example if a vendor has a history of supplying the pharmaceutical industry and the material is to be used in early development, a paper assessment (e.g., a questionnaire) should be sufficient. If a supplier does not have a history of supplying the pharmaceutical industry, a risk assessment should be performed and depending on the outcome a site audit may be required prior to accepting material for use.

Ideally, vendors should be qualified prior to using raw materials for manufacture. However, it is acceptable for qualification to proceed in parallel as long as documentation/risk assessments are available prior to product release and as in the previous section all risk lies with the manufacturer and not the patient.

 

A production mixing unit is usually not geometrically similar to the mixer used for process development. Such differences can make scale-up from the laboratory or pilot plant challenging. A solution to these problems is to systematically calculate and evaluate mixing characteristics for each geometry change.

Geometric similarity is often used in mixing scale-up because it greatly simplifies design calculations. Geometric similarity means that a single ratio between small scale and large scale applies to every length dimension (see figure). With geometric similarity, all of the length dimensions in the large-scale equipment are set by the corresponding dimensions in the small-scale equipment. The only remaining variable for scale-up to large-scale mixing is the rotational speed — one or more mixing characteristics, such as tip speed, can be duplicated by the appropriate selection of a large-scale mixer speed.

Mixing Figure 1
The two most popular and effective geometric scale-up methods are equal tip speed and equal power per volume. Equal tip speed results when the small-scale mixer speed is multiplied by the inverse geometric ratio of the impeller diameters to get the large-scale mixer speed:

N2 = N1(D1/D2)

Equal power per volume involves a similar calculation, except the geometry ratio is raised to the two-thirds power:

N2 = N1(D1/D2)(2/3)

This expression for power per volume only applies strictly for turbulent conditions, where the power number is constant, but is approximately correct for transition-flow mixing.

Avoid mix-ups
As we have seen, taking successive steps allows the development of alternative solutions to scale-up. Similar methods can be used to scale-down process problems for investigation in a pilot-plant or laboratory simulation. Here, too, non-geometric similarity often is a problem. Such scale-down calculations should help pinpoint appropriate operating speeds to test in the small-scale mixer.
In any scale-up or scale-down evaluation, some variables can be held constant while others must change. For example, even with geometric similarity, scale-up will result in less surface per volume because surface area increases as the length squared and volume increases as length cubed. Similarly, keeping blend time constant rarely is practical with any significant scale change. Larger tanks take longer to blend than smaller ones. Also, Reynolds number is expected to increase as size increases. In addition, standard operating speeds or available impeller sizes may necessitate a final adjustment to the scale-up calculations.

Rules for scale-up always have exceptions but understanding the effects of scale-up, especially non-geometric scale-up, can provide valuable guidance. Indeed, appreciation of the tradeoffs involved in non-geometric scale-up may be crucial for success with large-scale mixing processes.

 REFERENCES

1  https://docs.google.com/viewer?url=http%3A%2F%2Fwww.sunbio.com%2Fsub%2FSunbio%2520GMP%2520Capabilty.ppt

http://apic.cefic.org/pub/5gmpdev9911.pdf

http://www.pharmtech.com/early-development-gmps-drug-product-manufacturing-small-molecules-industry-perspective-part-iii?rel=canonical

“ICH Q7a. Good Manufacturing Practice for Active Pharmaceutical Ingredients” (Draft 6, October 19th, 1999, section 19).

“ICH Q6a. Specifications: test procedures and acceptance criteria for new drug substances and new drug products: chemical substances”.

“Good Manufacturing Practices for Active Pharmaceutical Ingredients” (EFPIA / CEFIC Guideline, August, 1996).

“Quality Management System for Active Pharmaceutical Ingredients Manufacturers” (APIC/CEFIC May 1998).

“Good Manufacturing Practices Guide for Bulk Pharmaceutical Excipients”, The International Pharmaceutical Excipients Council (October 1995).

“21 Code of Federal Regulations, parts 210 to 211”, U.S. Food & Drug Administration. “Guide to inspection of Bulk Pharmaceutical Chemicals”, U.S. Food & Drug Administration, (Revised Edition: May 1994).

“Guidance for Industry. ANDAs: Impurities in Drug Substances”, U.S. Food and Drug Administration, CDER (June 1998).

“Guideline on the Preparation of Investigational New Drug Products”, U.S. Food & Drug Administration, CDER (March 1991).

“EC Guides to GMP, Annex 13: Manufacture of Investigational Medicinal Products” (Revised Dec. 1996).

“GMP Compliance during Development”, David J. DeTora. Drug Information Journal, 33, 769-776, 1999.

FDA Guidance documents on internet address: http://www.fda.gov/cder/guidance /index.htm

EMEA Guidance documents on internet address: http://www.eudra.org.

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Jul 092015
 

Areas of discussion included how expectations for raw material control are evolving within changing regulatory and business paradigms including quality by design (QbD), counterfeiting, complex supply chains, and sourcing changes. discussed risk assessment and mitigation strategies along with supplier risk management plans.

Regulatory Considerations

the lack of a consistent definition of raw materials in regulations pertaining to the pharmaceutical industry. In its Q7 guideline, the International Conference on Harmonisation of Technical Requirements for the Registration of Pharmaceuticals for Human Use (ICH) defines raw materials as “starting materials, reagents, and solvents intended for use in the production of intermediates or APIs.” However, the term as defined by different speakers could cover a wide range of materials including the following:

• starting or source materials (cell lines, viral or bacterial stocks, media components, chemicals, tissues, serum, water)

• in-process materials (resins, buffers, filters, column housings, tubing, reagents)

• excipients

• packaging components, both primary and secondary (syringes, vials, stoppers, plungers, crimps, boxes, trays, and labels)

• device/delivery components (pen/ injector components, IV bags, filters). Some regulations directly consider the control of raw materials, but they are not comprehensive and are scattered among the US Code of Federal Regulations (CFR), ICH, and other regulations/guidances. Although the regulations are not extensive, the need to control raw materials was clear from all presenters and is implicit in the sources cited below:

• 21 CFR 610.15 regarding constituents

• 21 CFR 211.80 regarding components and containers/closures

• 21 CFR 211.110 regarding control of in-process materials • ICH Q5A/D for cell substrates and viral safety

• ICH Q7 discussing the need to control materials with appropriate specifications

• ICH Q10 stating that a biomanufacturer is responsible for the quality of purchased materials

• the US bill “Country-of-Origin Labeling for Pharmaceutical Ingredients,” proposed in September 2008

• QbD principles requiring an understanding of the criticality of quality attributes for raw materials and their effect on processes and products.

Developing Control

Strategies Control of raw materials is essential to maintaining safety. Thorough knowledge of raw materials can mitigate the potential for contamination derived from such sources as microbes, chemicals, prions, and pyrogens. Raw material control for safety also includes identification — being able to verify that you have received the correct material — because the presence of an incorrectly identified material in a manufacturing process could compromise safety.

Control of raw materials is essential to ensure lot-to-lot consistency because variation in them can directly affect the variation of both product and process. So manufacturers must understand the critical material attributes (CMAs) of their raw materials and which of those affect variability — as well as how to control that variability.

You must show that you are using appropriate analytical methods to characterize raw materials. Raw materials such as polyethylene glycol (PEG) isomers, trace materials in media and water, container and closure materials, and chromatography resins all have the potential to affect lot-to-lot consistency. An effective raw material control program will also ensure consistent supplies.

A single source for a vital raw material can be a significant financial and quality-assurance risk. If a supplier goes out of business or experiences quality problems, can that raw material be obtained elsewhere? Has a second source been qualified in case the primary source is no longer available? Does the second source have the capacity to meet your needs? A QbD approach to raw material control requires that you understand the impact on your product’s critical quality attributes.

You will need to show that you understand the effect of raw material variability on your product as well as on your manufacturing process. Use of multiple lots during development can provide data on raw material lot-to-lot variability and its related effects on process and product. When that is not feasible, a manufacturer may consider including different lots of raw materials during bench-scale studies. In addition to the raw materials themselves, you should gain an understanding of whether and how raw material degradants might affect your process or product.

A QbD approach can use relevant knowledge to help you define how to go about setting specifications, in-process controls (IPCs), and handling conditions. Testing of Raw Materials The forum discussed what levels of testing are important for specific raw materials. A supplier’s certificate of analysis (CoA) is never sufficient for raw materials because good manufacturing practices (GMPs) require appropriate testing, and at a minimum, testing for identity. The material ordered may include additives, preservatives, degradation products, or contaminants. You must verify that the CoA is appropriate for control of the raw material, but you can’t assume that at the outset.

Similarly, CoA verification may be necessary only once a year once your experience with a given supplier has shown that quality is consistent. Vendor qualification is an important factor in defining your testing needs. To ensure the quality of raw materials against adulteration, identity testing is essential. Currently, tests with fingerprint techniques — e.g., nuclear magnetic resonance (NMR) imaging and Raman, nearinfrared (NIR), and Fourier-transform infrared (FTIR) spectroscopy — are used to assure the identity and quality of raw materials.

Whatever techniques you use, it is important to retain samples for future investigations. Photographic libraries of materials and their packaging have also proven useful for identifying and preventing use of counterfeit products. How often and in how much depth you need to verify a CoA through independent testing is an important consideration, especially for environments in which counterfeiting or contamination can occur.

Once you understand the CMAs of your raw materials, you need to identify which tests are relevant for testing specific quality attributes (QAs) of those raw materials. Sampling plans need careful consideration and should be risk based, dependent on the nature and use of the RM, and any regulatory requirements. Such plans should always be justified in a report available for inspection and/or filing.

It is important to consider RM stability and whether any special tests for degradants are needed for release of the material over time. A stability profile will dictate the purchasing program (storage of large quantities or buying as needed) as well as affect the associated testing strategy.

Supply Quality Management:

Ensuring Quality and Availability It is becoming increasingly evident in the current supply chain environment that management of suppliers and the “cold chain” is essential to assuring the quality of raw materials. How often and how thoroughly you perform vendor audits depends on your experience with a given vendor.

A manufacturer’s general experience with a vendor (prior knowledge) is an important criterion used to evaluate that vendor’s suitability to supply raw materials. Items to consider when selecting a vendor include its quality systems and its solvency, as well as its length of time in business, its geographic area, and whether it supplies multiple industries or just one or two drug manufacturers. Those form part of a risk assessment relating to suppliers to be described in more detail below.

Ensuring both the availability and qualification of secondary suppliers is important as well. Practices such as split purchasing may help ensure that you have good working relationships with multiple vendors. Strict change control sections should be included in supplier agreements and should include details requiring a vendor to notify you of changes in its product or suppliers. Such agreements should also provide for impact assessments from both supplier and manufacturer in the event that a supplier makes any changes. Supply chain traceability is not as straightforward as it might seem.

Although most manufacturers use country-of-origin (COO) questionnaires, those often prove less than ideal in revealing what you need to know. It is critical to craft questions that get the in-depth answers you need. For example, rather than asking “Do you purchase supplies from any high-risk countries?” you might ask “From what countries do you purchase supplies?” If the specified countries include any you consider to be high risk, you can follow up or choose another supplier.

It is critical to use risk-assessment techniques for determining traceability to avoid a false sense of security that can lead to costly or even deadly errors. It is sometimes unclear exactly what roles are played by whom in a supply chain.

Which companies are manufacturers, which are distributors, and which are intermediaries is not necessarily clear. A company that simply repackages a raw material from 55-gallon drums into smaller containers may consider itself a manufacturer. Due diligence will help ensure that you really know where your raw materials originated. As part of assessing supply chain complexity, forum participants were informed of a proposed program whereby industry creates a system of cooperative audits in which vendors would be audited by a selected team representing all industry rather than multiple auditors from each company continuously auditing suppliers.

The resulting audits would lead to certification that would assure all purchasers that each vendor meets certain defined criteria. Such a “360° Rx” program would enable increased depth of supplier audits and save manufacturers time and money (see box, right). The Role of Compendial Standards: Compendia provide some assurance of minimum quality standards for specified materials. However, compendial standards may differ among the pharmacopoeias.

Few of the complex raw materials (e.g., culture media, soy, yeastolates, most growth factors) used in biotechnology manufacturing are compendial, and those that are (e.g., insulin) may not have the appropriate compendial limits on specific quality attributes — or even test for quality attributes necessary to control pharmaceutical manufacturing. Even for standard chemical raw materials (e.g., trace metals), compendial standards may not focus on quality attributes relevant for biotechnology process and product quality assurance.

Those may be product- and/or process-specific. Furthermore, compendial standards do not necessarily help control for contamination, counterfeiting, or supply chain issues because a supplier can simply state it meets compendia — a statement that currently requires no certification

Risk Management

Risk assessments are an important tool for ensuring the safety, efficacy, consistency, and supply of pharmaceutical products. Many companies in both the United States and the European Union are using ICH Q9 as a basis for risk assessment, control, communication, and future review.

Risk assessments should begin by identifying all raw materials and assessing their criticality to product safety, efficacy, and supply. RM risk assessments require cross-functional input from all departments including supply, product development, manufacturing, quality control, quality assurance, clinical, and any other contributors. It was clear from this forum’s discussions that risk assessments are only as good as the people who carry them out. Having the right expertise over a spectrum of areas is vital if any risk assessment is to be meaningful. Multiple risk assessment tools exist, but in general, a good risk assessment must address concepts such as impact/ severity and likelihood/detectability.

One tool discussed at the forum (Figure 1) used nine blocks to score a supplier’s performance against material risk levels for audits, supplier qualification, supplier monitoring, change control, material specifications and testing, quality agreements, supplier certification, and sourcing, or other appropriate combinations of factors. Risk assessment should also be performed in relation to country of origin. It is critical to be able to trace your raw materials to their source. Just as a biopharmaceutical manufacturer audits its suppliers, those suppliers must also know, audit, and qualify their own distributors.

It is now well known that there are high-risk geographic areas where additional caution should be exercised to assure purity and identity of sourced materials. A potentially overlooked risk assessment issue is that manufacturers need to evaluate their raw materials and products in relation to opportunities for someone to make a profit through adulteration (e.g., by diluting a product to increase volume, and thus sales income). Any materials identified in such an evaluation should be managed with particular caution.

Risk assessments ensure that appropriate control strategies and raw materials (e.g., grade, origin) have been selected, which is relevant to a QbD approach. For regulatory filings, acceptable specifications, raw materials, and control strategies are tested with the necessary acceptance criteriia to ensure the performance of a process and the quality of its ultimate products. A periodic risk review should include more than a mere cursory review of individual risk assessments. It should reevaluate the risk program itself based on experience and lessons learned. Your risk assessment should be phase-appropriate, and as such it will change as data become available throughout development.

Early on, your raw materials risk assessment can be based on platform and previous knowledge, on the quality assurance of your suppliers, and adventitious agent introduction. As a manufacturing process develops, you will need to reevaluate that risk assessment including commercial considerations of scale and production frequency, highrisk raw materials control strategy, and handling and storage requirements.

During commercialization, design of experiments (DoEs) and collated knowledge will further define the CQAs of both product and RMs as well as potential and actual interactions among RMs, process, and product. At that point, you will be able to define and justify the raw materials for your commercial process and refine their specifications.

By the time your product is ready for market launch, you will have updated the failure modes and effects analysis (FMEA), completed your raw materials specifications, set your sourcing strategy, put in place your supplier qualification program, defined your raw material control strategy, and made your risk assessment ready for filing. The morning’s session resulted in a list of elements to be included in a raw materials risk assessment

 

Elements of Raw Material

Risk Assessments Is the raw material biological, chemical, or physical (such as tubing or stoppers, materials that are not actual components of the end product)? How likely is the raw material to introduce biological or chemical contamination?

Is the raw material or are its degradants able to directly affect the safety and/or efficacy of a drug substance (e.g., toxicity, chemical modifications)?

How complex is the raw material itself or its impurity profile? How much prior knowledge (e.g., historical or published knowledge, current experience) do you have regarding the raw material? What is the Intended use of the raw material (e.g., as a buffer, reagent, or excipient)?

Where in the manufacturing process will this raw material will be used (upstream/ downstream)?

What is the extent of supply chain traceability (considering country of origin, supply chain complexity, and supply chain security)?

What is the extent of supplier quality assurance (from audits, monitoring, historical experience)?

How extensive is the characterization of the raw material (how well can the raw material be characterized; standard existing methods or novel techniques; the RM’s impact on test methods)?

How stable is the raw material? Is the raw material new to the process or a result of a change to an existing raw material (if a change, what studies have been executed to assure comparability)?

What is the depth of knowledge of the RM’s own manufacturing process to assess the risk associated with its use (e.g., process contaminants)?

Does the use of the raw material in a manufacturing environment present safety and/or handling risks? Does your process have the ability to clear the raw material?

Are there associated business risks (e.g., a solesource or multiple-source material, unique or not to the pharmaceutical industry, custom-made or not, and the supplier’s ability to consistently meet specific requirements)?

What is your level of understanding of the raw material CMAs?

Benefits of Implementing QbD

Benefits for the FDAEnhances scientific foundation for review
Provides for better coordination across review, compliance, and inspection
Improves information in regulatory submissions Provides for better consistency
Improves quality of review (establishing a quality management system for CMC)
Provides for more flexibility in decision making
Ensures decisions made on scientific and not on empirical information
Involves various disciplines in decision making
Uses resources to address higher risks
Benefits for Industry
Ensures better design of products with fewer problems in manufacturing
Reduces number of manufacturing supplements required for postmarket changes; relies on process and risk understanding and risk mitigation
Allows for implementation of new technology to improve manufacturing without regulatory scrutiny
Allows for possible reduction in overall costs of manufacturing; creates less waste
Ensures less hassle during review, reduces deficiencies, speeds approvals Improves interaction with the FDA; operates on a scientific rather than on a process level
Allows for continuous improvements in products and manufacturing processes
Allows for better understanding of how APIs and excipients affect manufacturing
Relates manufacturing to clinical during design
Provides a better overall business model

Frequently Used QbD Terms 

 

Quality Attribute: A physical, chemical, or microbiological property or characteristic of a material that directly or indirectly alters quality Critical Quality Attribute (CQA): A quality attribute that must be controlled within predefined limits to ensure that a product meets its intended safety, efficacy, stability, and performance
Real-Time Release (RTR): Ability to evaluate and ensure acceptable quality of an in-process and/or final product based on process data, including valid combination of assessment of material attributes by direct and/or indirect process measurements and assessment of critical process parameters and their effects on in-process material attributes Process Parameter: An input variable or condition of a manufacturing process that can be directly controlled in the process. Typically, such parameters are physical or chemical (e.g., temperature, process time, column flow rate, column volume, reagent concentration, or buffer pH).
Critical Process Parameter (CPP): A process parameter whose variability has an influence on a CQA and therefore should be monitored or controlled to ensure a process produces a desired quality. Process Performance Attribute: An output variable or outcome that cannot be directly controlled but is an indicator that a process performed as expected
Key Process Parameter (KPP): An input process parameter that should be carefully controlled within a narrow range and is essential for process performance; a key process parameter does not affect product quality attributes. If the acceptable range is exceeded, it may affect the process (e.g., yield, duration) but not product quality. Non-Key Process Parameter: An input parameter that has been demonstrated to be easily controlled or has a wide acceptable limit. Such parameters may influence quality or process performance if acceptable limits are exceeded.
Design Space: The multidimensional combination and interaction of input variables (e.g., material attributes) and process parameters that have been demonstrated to provide assurance of quality; working within a design space is not considered to be a change requiring regulatory approval. Movement out of a design space is considered to be a change and would normally initiate a regulatory postapproval change process. Design space is proposed by an applicant and is subject to regulatory assessment and approval (ICH Q8). Control Strategy: A planned set of controls, derived from current product and process understanding, that ensures process performance and product quality; such controls can include parameters and attributes related to drug substance and drug product materials and components, facility and equipment operating conditions, in-process controls, finished-product specifications, and associated methods, and frequency of monitoring and control (ICH Q10).
Quality Target Product Profile (QTPP): A prospective summary of the quality characteristics of a drug product that ideally will be achieved to ensure desired quality, taking into account safety and efficacy of a drug product
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What is 35 U.S. Code § 112 – Specification, ………..it is so easy to understand, try

 PATENTS, regulatory  Comments Off on What is 35 U.S. Code § 112 – Specification, ………..it is so easy to understand, try
Feb 032015
 

 

                U.S. Code› Title 35 › Part II › Chapter 11 › § 112………more explanation see below

Law is easy, …. learn with me and explained by cornell

I picked this up from site………..http://www.law.cornell.edu/uscode/text
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U.S. Code: Table of Contents  U.S. Code

U.S. Code: Title 35 – PATENTS Title 35 ›

35 U.S. Code Part II – PATENTABILITY OF INVENTIONS AND GRANT OF PATENTS Part II ›

35 U.S. Code Chapter 11 – APPLICATION FOR PATENT Chapter 11 ›

 § 112. specification explained in this article

(a) In General.— The specification shall contain a written description of the invention, and of the manner and process of making and using it, in such full, clear, concise, and exact terms as to enable any person skilled in the art to which it pertains, or with which it is most nearly connected, to make and use the same, and shall set forth the best mode contemplated by the inventor or joint inventor of carrying out the invention.
(b) Conclusion.— The specification shall conclude with one or more claims particularly pointing out and distinctly claiming the subject matter which the inventor or a joint inventor regards as the invention.
(c) Form.— A claim may be written in independent or, if the nature of the case admits, in dependent or multiple dependent form.
(d) Reference in Dependent Forms.— Subject to subsection (e), a claim in dependent form shall contain a reference to a claim previously set forth and then specify a further limitation of the subject matter claimed. A claim in dependent form shall be construed to incorporate by reference all the limitations of the claim to which it refers.
(e) Reference in Multiple Dependent Form.— A claim in multiple dependent form shall contain a reference, in the alternative only, to more than one claim previously set forth and then specify a further limitation of the subject matter claimed. A multiple dependent claim shall not serve as a basis for any other multiple dependent claim. A multiple dependent claim shall be construed to incorporate by reference all the limitations of the particular claim in relation to which it is being considered.
(f) Element in Claim for a Combination.— An element in a claim for a combination may be expressed as a means or step for performing a specified function without the recital of structure, material, or acts in support thereof, and such claim shall be construed to cover the corresponding structure, material, or acts described in the specification and equivalents thereof.
SO EASY TO UNDERSTAND 35 U.S.C. § 112

35 U.S.C. 112  Specification.

[Editor Note: Applicable to any patent application filed on or after September 16, 2012. See 35 U.S.C. 112 (pre-AIA)for the law otherwise applicable.]

  • (a) IN GENERAL.—The specification shall contain a written description of the invention, and of the manner and process of making and using it, in such full, clear, concise, and exact terms as to enable any person skilled in the art to which it pertains, or with which it is most nearly connected, to make and use the same, and shall set forth the best mode contemplated by the inventor or joint inventor of carrying out the invention.
  • (b) CONCLUSION.—The specification shall conclude with one or more claims particularly pointing out and distinctly claiming the subject matter which the inventor or a joint inventor regards as the invention.
  • (c) FORM.—A claim may be written in independent or, if the nature of the case admits, in dependent or multiple dependent form.
  • (d) REFERENCE IN DEPENDENT FORMS.—Subject to subsection (e), a claim in dependent form shall contain a reference to a claim previously set forth and then specify a further limitation of the subject matter claimed. A claim in dependent form shall be construed to incorporate by reference all the limitations of the claim to which it refers.
  • (e) REFERENCE IN MULTIPLE DEPENDENT FORM.—A claim in multiple dependent form shall contain a reference, in the alternative only, to more than one claim previously set forth and then specify a further limitation of the subject matter claimed. A multiple dependent claim shall not serve as a basis for any other multiple dependent claim. A multiple dependent claim shall be construed to incorporate by reference all the limitations of the particular claim in relation to which it is being considered.
  • (f) ELEMENT IN CLAIM FOR A COMBINATION.—An element in a claim for a combination may be expressed as a means or step for performing a specified function without the recital of structure, material, or acts in support thereof, and such claim shall be construed to cover the corresponding structure, material, or acts described in the specification and equivalents thereof.

(Amended July 24, 1965, Public Law 89-83, sec. 9, 79 Stat. 261; Nov. 14, 1975, Public Law 94-131, sec. 7, 89 Stat. 691; amended Sept. 16, 2011, Public Law 112-29, sec. 4(c), 125 Stat. 284, effective Sept. 16, 2012.)

 

35 U.S.C. 112 (pre-AIA)   Specification.

[Editor Note: Not applicable to any patent application filed on or after September 16, 2012. See 35 U.S.C. 112 for the law otherwise applicable.]

The specification shall contain a written description of the invention, and of the manner and process of making and using it, in such full, clear, concise, and exact terms as to enable any person skilled in the art to which it pertains, or with which it is most nearly connected, to make and use the same, and shall set forth the best mode contemplated by the inventor of carrying out his invention.

The specification shall conclude with one or more claims particularly pointing out and distinctly claiming the subject matter which the applicant regards as his invention.

A claim may be written in independent or, if the nature of the case admits, in dependent or multiple dependent form.

Subject to the following paragraph, a claim in dependent form shall contain a reference to a claim previously set forth and then specify a further limitation of the subject matter claimed. A claim in dependent form shall be construed to incorporate by reference all the limitations of the claim to which it refers.

A claim in multiple dependent form shall contain a reference, in the alternative only, to more than one claim previously set forth and then specify a further limitation of the subject matter claimed. A multiple dependent claim shall not serve as a basis for any other multiple dependent claim. A multiple dependent claim shall be construed to incorporate by reference all the limitations of the particular claim in relation to which it is being considered.

An element in a claim for a combination may be expressed as a means or step for performing a specified function without the recital of structure, material, or acts in support thereof, and such claim shall be construed to cover the corresponding structure, material, or acts described in the specification and equivalents thereof.

(Amended July 24, 1965, Public Law 89-83, sec. 9, 79 Stat. 261; Nov. 14, 1975, Public Law 94-131, sec. 7, 89 Stat. 691.)

 SO EASY TO UNDERSTAND 35 U.S.C. § 112

 

 

 

SO EASY TO UNDERSTAND 35 U.S.C. § 112

 

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The Cornell Law Library is one of 12 national depositories for print records of briefs filed with the U.S. Supreme Court.

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LEARN A CASE STUDY WITH DR ANTHONY,    SO EASY TO UNDERSTAND 35 U.S.C. § 112

ME

case study on this

The Attack of 35 U.S.C. § 112

http://www.google.com/patents/US8598219

September 2, 2014, Accord Healthcare, Inc. (“Accord”) filed what appears to be the second-ever Post-Grant Review (“PGR”) (see Petition).  This PGR was for U.S. Patent No. 8,598,219 (“the ‘219 Patent”), which is jointly assigned to Helsinn Healthcare S.A. and Roche Palo Alto, LLC (collectively “Helsinn”). 

Helsinn Healthcare SaRoche Palo Alto Llc

As a reminder, PGRs are the third type of post-issuance review procedures established by the America Invents Act (“AIA”) — the other two being Inter Partes Review and Covered Business Method Patent Review (IPR and CBM, for short).  However, the reason that only one other PGR has been filed to date is because this type of proceeding only applies to patents that were examined pursuant to the new First Inventor to File scheme established by the AIA.

And because such applications could only be filed on or after March 16, 2013, there are only a limited number of such patents that are presently eligible for PGR.  One of the other significant differences between IPRs and PGRs is that the latter is not limited to certain types of prior art validity attacks (such as 102 or 103), but instead any type of validity challenge available in District Court is essentially available in front of the Patent Trial and Appeals Board (“PTAB”).

This includes attacks under 35 U.S.C. § 112, such as allegations of a lack of enablement, a lack of written description, and a failure to distinctly claim the invention.  Accord took full advantage of this in its petition for PGR2014-00010, in which Accord alleged that Helsinn’s patent related to liquid pharmaceutical formulations of palonosetron should not have been issued by the Patent Office.

Accord Healthcare

The ‘219 patent had been asserted in several Hatch-Waxman litigations involving ALOXI®, which is a palonosetron formulation indicated to help prevent nausea and vomiting following chemotherapy.  Palonosetron hydrochloride, the active pharmaceutical ingredient, has the following structural formula:

Structure
The ‘219 patent is a member of a family of patents directed to formulations of palonosetron hydrochloride.  Importantly, this patent was filed as a continuation-in-part application on May 23, 2013, with a letter that asserted that claim 9 only had support because of a newly added example, and therefore was subject to the AIA.  Only claims 1-5 and 8 of the ‘219 patent are the subject of this petition, with claim 1 reading:

1.    A pharmaceutical single-use, unit-dose formulation for intravenous administration to a human to reduce the likelihood of cancer chemotherapy-induced nausea and vomiting, comprising a 5 mL sterile aqueous isotonic solution, said solution comprising:
palonosetron hydrochloride in an amount of 0.25 mg based on the weight of its free base;
from 0.005 mg/mL to 1.0 mg/mL EDTA;
and from 10 mg/mL to 80 mg/mL mannitol,
wherein said formulation is stable at 24 months when stored at room temperature.

Claim 8 is the only other challenged independent claim, and it reads identically, except for a stability limitation of 18 months when stored at room temperature.  This patent issued on December 3, 2013, and the PGR petition was filed within the requisite nine months.

What is claimed is:

1. A pharmaceutical single-use, unit-dose formulation for intravenous administration to a human to reduce the likelihood of cancer chemotherapy-induced nausea and vomiting, comprising a 5 mL sterile aqueous isotonic solution, said solution comprising:

palonosetron hydrochloride in an amount of 0.25 mg based on the weight of its free base;
from 0.005 mg/mL to 1.0 mg/mL EDTA; and
from 10 mg/mL to 80 mg/mL mannitol,
wherein said formulation is stable at 24 months when stored at room temperature.
2. The pharmaceutical formulation of claim 1, wherein said EDTA is in an amount of 0.5 mg/mL.
3. The pharmaceutical formulation of claim 1, wherein said mannitol is in an amount of 41.5 mg/mL.
4. The pharmaceutical formulation of claim 1, wherein said solution further comprises a citrate buffer.
5. The pharmaceutical formulation of claim 4, wherein said citrate buffer is at a concentration of 20 millimolar.
6. The pharmaceutical formulation of claim 1, wherein said solution is buffered at a pH of 5.0 ±0.5.
7. The pharmaceutical formulation of claim 1, wherein said EDTA is in an amount of 0.5 mg/mL, wherein said mannitol is in an amount of 41.5 mg/mL, wherein said solution further comprises a citrate buffer at a concentration of 20 millimolar, and wherein said solution is buffered at a pH of 5.0 ±0.5.
8. A pharmaceutical single-use, unit-dose formulation for intravenous administration to a human to reduce the likelihood of cancer chemotherapy-induced nausea and vomiting, comprising a 5 mL sterile aqueous isotonic solution, said solution comprising:

palonosetron hydrochloride in an amount of 0.25 mg based on the weight of its free base;
from 0.005 mg/mL to 1.0 mg/mL EDTA; and
from 10 mg/mL to 80 mg/mL mannitol, wherein said formulation is stable at 18 months when stored at room temperature.

 SO EASY TO UNDERSTAND 35 U.S.C. § 112

The petition pointed out that during the prosecution of the ‘219 patent and its family, the Patent Office had rejected the claimed formulations as obvious.  In response, the applicants submitted a declaration from inventor Daniele Bonadeo (“the Bonadeo declaration”) and argued that one of skill in the art would not have combined the features of the invention as a matter of routine optimization.  Instead of routine, the applicants continued, the claimed formulations were obtained after a sequence of experiments, each of which built upon the others like building blocks.

If the experimental sequence had varied, the applicants alleged that they would have obtained a different formulation.  The Bonadeo declaration explained that the first two parameters studied were palonosetron concentration and pH.  None of the studies described in this declaration, however, occurred at a pH other than 5.0, which makes sense because palonosetron was described as extremely stable at this pH.

Considering that the ‘219 patent ultimately issued, the applicants were apparently successful in overcoming these obviousness rejections.  In other words, the applicants convinced the examiner that a person of ordinary skill in the art would not have found it obvious to combine the teachings in the prior art to derived the claimed inventions.

The positions taken by the applicant, however, were utilized by the petitioner, Accord, to allege that a person of ordinary skill in the art would not have, for example, found the specification enabling.  This highlights the problem that PGRs pose for patent applicants.  Before such procedure, arguments could be made without much fear that they would be coopted by the Office for making alternative rejections.  And, if the Office did, there would still an opportunity to provide a response or amend the claims.  Even if such arguments were made in district court litigation, the patent would at least enjoy a presumption of validity.

Now, all applicants must take extreme caution in making any arguments, because anything said can (and probably will) be used against them at the PTAB.

What follows is an identification of the 35 U.S.C. § 112 arguments made by Accord.  Considering that the patent owner has not yet filed any response, and the PTAB has not weighed in, no position is taken here as to the merits of these arguments.

Written Description – Stability

Accord first alleged that the ‘219 was unpatentable for failing to provide an adequate description of the claimed subject matter being stable at 18 or 24 months when stored at room temperature, as required by 35 U.S.C. § 112(a).  Specifically, the petition asserted that the specification does not show that the inventors were in possession of any formulation that would have achieved the stability limitations of the claims.

Instead, the argument went, the patent contained general statements that it is possible to increase the stability of the formulations, but did not provide any examples with stability beyond a couple of weeks.  Accord included a declaration from Dr. Arnold J. Repta, which explained how a person of ordinary skill in the art would have understood the teaching of the specification.  However, Dr. Repta did not include any additional testing of the formulations taught in the application in his declaration.

Enablement

The second assertion made in the petition was that the ‘219 patent does not enable a pH range for the claimed formation outside of about 4.0 to 6.0, and therefore it is not enabled as required by 35 U.S.C. § 112(a).  This is because, according the petition, the only relevant formulation in the specification was disclosed as having a pH of 5.0±0.5.  Moreover, the specification was alleged to claim that palonosetron is most stable at pH 5.0.

Accord also cited to the Bonadeo Declaration, which was submitted during prosecution by the applicants, which alleged claimed that palonosetron formulations containing mannitol or EDTA required a pH of 4-6.  Therefore, according to the petition, because the challenged claims do not recite any pH limitations, they were broader than the teaching of the specification.

“Regards as the Invention”

35 U.S.C § 112(b) requires that a patent “conclude with one or more claims particularly pointing out and distinctly claiming the subject matter which the inventor or a joint inventor regards as the invention.”  Accord challenged the claims of the ‘219 patent as not including the invention as regarded by the inventors.  Specifically, the petition alleges that the Bonadeo Declaration made clear that palonosetron was extremely stable at a pH of 5.0, and that there was no hint that a pH outside of the range of about 4.0 or 6.0 would be suitable.  A similar argument was made about the language found in the specification.  The petitioner concluded by pointing out that, even though the inventors believed that the inventive formation should be in a range of 4.0 to 6.0, such a limitation was not included in the claims.

Written Description – pH Range

Finally, Accord made a similar argument when alleging that the specification did not support claims that did not include a pH range of 4.0 to 6.0.  Citing to the Gentry Gallery, Inc. v. Berkline Corp., 134 F.3d 1473 (Fed. Cir. 1998), line of cases, the petitioner alleged that the pH range was an essential or critical feature which was omitted from that claims.  In other words, Accord alleged that the broad claims without a pH limitation were invalid because the “entirety of the specification” demonstrates that the invention was of much narrower scope.

Of course, similar to an IPR, the patent owner now has a chance to submit a preliminary response to the petition.  The standard used for instituting a PGR differs from that required for an IPR.  Instead of the “reasonable likelihood” standard, a PGR will only be instituted when it is more likely than not that at least one of the claims challenged is unpatentable.  In essence, this should be a slightly more stringent standard, because with both positions being equally likely, an IPR petition would have a reasonable likelihood of demonstrating claims as unpatentable, but a PGR petition would not be more likely than not to demonstrate unpatentable claims.

However, it remains to be seen if less PGRs are instituted than IPRs.  We will continue to monitor PGR2014-00010, and provide updates as warranted.

SO EASY TO UNDERSTAND 35 U.S.C. § 112

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Road map to 2015, The European Medicines Agency’s contribution to science, medicines and health

 EU, regulatory, Uncategorized  Comments Off on Road map to 2015, The European Medicines Agency’s contribution to science, medicines and health
Aug 182014
 

 

One of the European Medicines Agency’s long-term strategic goals is to foster researchand the uptake of innovative methods in the development of medicines.

READ………….Road map to 2015

The European Medicines Agency’s
contribution to science, medicines and health……………..http://www.ema.europa.eu/docs/en_GB/document_library/Report/2011/01/WC500101373.pdf

This helps the Agency to meet its objective of making safe and effective medicines available to patients in a timely manner, following evaluation using state-of-the-art methods.

The Agency also supports the development of new therapies and technologies by working with interested parties in the European Union (EU).

Activities at the Agency

In 2004, the Agency set up the European Medicines Agency/Committee for Medicinal Products for Human Use (CHMP) Think-Tank Group on Innovative Drug Development.

This group included Agency staff and members of the CHMP and its working parties. Its work focused on identifying scientific bottlenecks and emerging science in the development of medicines, both in industry research and development and in academia, and on generating recommendations for future activities at the Agency:

In 2008 the EMA and its Scientific Committees integrated the recommendations made by the Think Tank in its strategy for supporting innovative medicines developments. Key areas of action included the strengthening of the EU scientific network model, emphasis on communication during the lifecycle of medicinal products development and international activities. Overview of measures implemented in the period 2008-2010.

The recently published Road Map to 2015 further expands on the role the Agency plays to promote innovation in pharmaceuticals.

The Agency also contributes to the Innovative Medicines InitiativeExternal link icon (IMI). This is a public-private initiative that aims to speed up the development of better and safer medicines for patients:

Support for business

The Agency provides support for business on issues related to innovative medicines:

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Key steps in implementation of QbD for a biotech product…….Quality by design for biopharmaceuticals

 regulatory  Comments Off on Key steps in implementation of QbD for a biotech product…….Quality by design for biopharmaceuticals
Aug 052014
 

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Identifying target product profile (TPP). TPP has been defined as a “prospective and dynamic summary of the quality characteristics of a drug product that ideally will be achieved to ensure that the desired quality, and thus the safety and efficacy, of a drug product is realized”. This includes dosage form and route of administration, dosage form strength(s), therapeutic moiety release or delivery and pharmacokinetic characteristics (e.g., dissolution and aerodynamic performance) appropriate to the drug product dosage form being developed and drug product-quality criteria (e.g., sterility and purity) appropriate for the intended marketed product. The concept of TPP in this form and its application is novel in the QbD paradigm.

Identifying CQAs. Once TPP has been identified, the next step is to identify the relevant CQAs. A CQA has been defined as “a physical, chemical, biological, or microbiological property or characteristic that should be within an appropriate limit, range, or distribution to ensure the desired product quality”10. Identification of CQAs is done through risk assessment as per the ICH guidance Q9 . Prior product knowledge, such as the accumulated laboratory, nonclinical and clinical experience with a specific product-quality attribute, is key in making these risk assessments. Such knowledge may also include relevant data from similar molecules and data from literature references. Taken together, this information provides a rationale for relating the CQA to product safety and efficacy. The outcome of the risk assessment would be a list of CQAs ranked in order of importance. Use of robust risk assessment methods for identification of CQAs is novel to the QbD paradigm.

Defining product design space. After CQAs for a product have been identified, the next step is to define the product design space (that is, specifications for in-process, drug substance and drug product attributes). These specifications are established based on several sources of information that link the attributes to the safety and efficacy of the product, including, but not limited to, the following:

  • Clinical design space
  • Nonclinical studies with the product, such as binding assays, in vivo assays and in vitro cell-based assays
  • Clinical and nonclinical studies with similar platform products
  • Published literature on other similar products
  • Process capability with respect to the variability observed in the manufactured lots

The difference between the actual experience in the clinic and the specifications set for the product would depend on our level of understanding of the impact that the CQA under consideration can have on the safety and efficacy of the product. For example, taking host cell proteins as a CQA, it is common to propose a specification that is considerably broader than the clinical experience. This is possible because of a greater ability to use data from other platform molecules to justify the broader specifications. On the other hand, in the case of an impurity that is unique to the product, the specifications would rely solely on clinical and nonclinical studies.

In QbD, an improved understanding of the linkages between the CQA and safety and efficacy of the product is required. QbD has brought a realization of the importance of the analytical, nonclinical and animal studies in establishing these linkages and has led to the creation of novel approaches.

Defining process design space. The overall approach toward process characterization involves three key steps. First, risk analysis is performed to identify parameters for process characterization. Second, studies are designed using design of experiments (DOE), such that the data are amenable for use in understanding and defining the design space. And third, the studies are executed and the results analyzed to determine the importance of the parameters as well as their role in establishing design space.

Failure mode and effects analysis (FMEA) is commonly used to assess the potential degree of risk for every operating parameter in a systematic manner and to prioritize the activities, such as experiments, necessary to understand the impact of these parameters on overall process performance. A team consisting of representatives from process development, manufacturing and other relevant disciplines performs an assessment to determine severity, occurrence and detection. The severity score measures the seriousness of a particular failure and is based on an estimate of the severity of the potential failure effect at a local or process level and the potential failure effect at end product use or patient level. Occurrence and detection scores are based on an excursion (manufacturing deviation) outside the operating range that results in the identified failure. Although the occurrence score measures how frequently the failure might occur, the detection score indicates the probability of timely detection and correction of the excursion or the probability of detection before end product use. All three scores are multiplied to provide a risk priority number (RPN) and the RPN scores are then ranked to identify the parameters with a high enough risk to merit process characterization.  FMEA outcome for a process chromatography step in a biotech process. RPN scores are calculated and operating parameters with an RPN score >50 are characterized using a qualified scaled-down model. For the case study presented here, these include gradient slope, temperature, flow rate, product loading, end of pool collection, buffer A pH, start of pool collection, volume of wash 1, buffer B pH, buffer C pH and bed height. Process characterization focused on parameters such as temperature, that have a high impact on the process (severity = 6), occur frequently in the manufacturing plant (occurrence = 6) and are difficult to quickly correct if detected (detection = 7). In contrast, parameters such as equilibration volume, with a low impact on the process (severity = 3), low occurrence (occurrence = 2) and a limited ability to detect and correct (detection = 5), were not examined in process characterization.

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Feb 052014
 
Pharmaceutical API Polymorphs… case study of Trelagliptin
CASE STUDY WITH..Compound I having the formula
Figure imgf000073_0001
Links
WO2008067465A1 OR US8084605  IS THE PATENT USED AND WITH FORM “A” AND AMORPHOUS FORM
Active pharmaceutical ingredients (APIs), frequently delivered to the patient in the solid-state as part of an approved dosage form, can exist in such diverse solid forms as polymorphs, pseudopolymorphs, salts, co-crystals and amorphous solids. Various solid forms often display different mechanical, thermal, physical and chemical properties that can remarkably influence the bioavailability, hygroscopicity, stability and other performance characteristics of the drug.
Hence, a thorough understanding of the relationship between the particular solid form of an active pharmaceutical ingredient (API) and its functional properties is important in selecting the most suitable form of the API for development into a drug product. In past decades, there have been significant efforts on the discovery, selection and control of the solid forms of APIs and bulk drugs.
If you’re involved in late drug discovery, API manufacture, drug product formulation, clinical material production, or manufacture of final dosage form, a basic understanding and awareness of solid form issues could save you a great deal of difficulty, time, and money during drug development.
 
What is polymorphism?
Polymorphs are crystalline materials that have the same chemical composition but different molecular packing. The concept is well demonstrated by the different crystalline forms of carbon. Diamond, graphite, and fullerenes are all made of pure carbon, but their physical and chemical properties vary drastically. Polymorphs are one type of solid form. Other solid form types include solvates, hydrates, and amorphous forms.
Solvates are crystalline materials made of the same chemical substance, but with molecules of solvent regularly incorporated into a unique molecular packing. When water is the solvent, these are called hydrates. An amorphous form of a substance has the same chemical composition, but lacks the long-range molecular order of a crystalline form of the same substance. Many organic and inorganic compounds, including APIs, can exist in multiple solid forms.
Some APIs may have only one or two known solid forms. Others may exist in twenty different forms, each having different physical and chemical properties.
Solid form screening, including salt, polymorph, cocrystal and amorphous solid dispersions, is vitial for successful pharmaceutical development. With an increase in the size and complexity of the molecules that enter into drug development, companies face a larger number of compounds that are either poorly soluble, difficult to crystallize or problematic with respect to desired physical chemical properties hindering successful drug development.
Crystallics has an extensive track record in executing solid state research studies and its research team has a broad expertise in identifying new crystal forms as well as in solving problems related to polymorphism and crystallization.

Investigational new drug, writing an application for clinical trial authorization, permission marketing …The control of polymorphism in drug candidates is now ubiquitous.

Links

READ………….An Overview of Solid Form Screening During Drug Development, http://www.icdd.com/ppxrd/10/presentations/PPXRD-10_Ann_Newman.pdf

ANN NEWMAN

When addressing the subject of polymorphism, the first reference that comes to mind is that of the occurred during the manufacture of ritonavir incident. Abbott molecule inhibitor of HIV protease marketed as Norvir, is a cautionary example of the challenges of polymorphism.

Indeed, during the production of ritonavir in 1997, a new polymorph unmarked emerged. Its precipitation and unexpected outbreak led to the cessation of the production of Norvir and seriously compromise the process. The incident has deeply marked the pharmaceutical industry.

It is ironic that the process used to discover pharmaceutical drug targets is the same one that decreases the actual efficacy of those drugs once ingested. If you remember from basic chemistry, there are compounds that exist in highly ordered crystalline states and those that remain in amorphous form.

The discovery of drug targets has often been accomplished through X-ray crystallography, which requires a sample (for example, of a defective enzyme linked to cancer or high cholesterol) to be crystallized so that the diffraction patterns can be made sense of. Scientists may spend years trying to crystallize one molecule or compound so that they can identify regions that, for example, may be blocked by pharmaceuticals.

However, when it comes to the molecular arrangement of those pharmaceuticals, crystallization actually decreases their bioavailability and solubility. Thus, it may be better for these drugs to be in amorphous form. Pierric Marchand, general manager of the company Holodiag, dedicated to the study and characterization of solid state, summarizes that ” today, it is not reasonable to not worry about the problem of polymorphism ” .

” In recent years, manufacturers have realized the essential side of expertise , “says Jean-Rémi David, commercial director Calytherm. The services company specializing in the field of physico-chemical analysis, based in Herault, has just relocated last year in supporting pharmaceutical development to meet demand. ” This is a concern for all deal with potential impacts on the effectiveness or the formulation , “says Stéphane Suchet, quality manager in the group of fine and specialty chemicals Axyntis.

Polymorphic forms are the amorphous and crystalline forms such as hydrate or solvate forms. When a molecule of interest exists in polymorphic forms, it is called polymorphism, according to the definition of the FDA (Food and Drug Administration).

Polymorphism is present at all stages of development of a drug from research to marketing. ” Keep in mind that organic molecule loves to polymorphism , “says Marchand Pierric. However, for a marketing authorization for example, must learn the criteria for the polymorphism of the molecule. ” In terms of the formulation, for example we can check whether the selected polymorphism is unchanged , “explains Pierric Marchand.

A significant influence on several levels  Because the consequences of polymorphism are multiple. ” They are at three levels: bioequivalence, manufacturability and stability “lists Fabienne Lacoulonche, founder and scientific director of Calytherm.In terms of bioequivalence, different polymorphic forms may have different properties of solubility and dissolution rate … ” For poorly soluble active ingredients, you can have much more bioavailable than other crystalline forms , “Fabienne Lacoulonche information.

In terms of manufacturability, some parameters such as temperature, moisture can lead to changes in the crystalline form. ” The complexity is to anticipate changes polymorphism, both at laboratory scale, pilot and industrial , “adds the founder of Calytherm. Finally, polymorphism plays on stability. Active ingredient or finished product, are subjected to stability studies in this direction. ” When the molecule is identified, we try to highlight the existence of several forms of polymorphism, explains Stéphane Suchet (Axyntis) 

When developing a new substance, the assessment is systematic . ” Isolation of crystals from a screening is carried out in different solvents by various analytical techniques. Ideally, it will be concluded the absence of polymorphism. ” But if different polymorphic forms are present, we rework the terms of our crystallization process to control the formation of the same polymorph reproducibly ideally form the thermodynamically more stable , “says Stéphane Suchet. X-ray diffraction and other thermal analysis ”

The ICH guidelines provide decision trees to guide the industry in controlling polymorphism says Fabienne Lacoulonche (Calytherm.) We use it for writing the CTD (Common Technical Document) .

“Polymorphism is a phenomenon” complex and difficult to control, because the crystallization is dependent on many parameters , she develops. must understand the maximum . ” For this, several analytical methods are available to industry. The main technique is the X-ray diffraction ” It is a robust, rapid, which allows to characterize the different polymorphs , “summarizes Pierric Marchand (Holodiag).Non-destructive, it can work both on small quantities on large samples. Temperature and atmosphere are controlled, and analytical capabilities are broad.

But if this technique indispensable allows for routine and development, it is not sufficient in itself. Just to add a battery of additional tests, thermal analysis. ” It takes coupling methods “ confirms Fabienne Lacoulonche (Calytherm). The X-ray diffraction is a method of choice, but sometimes it is not sufficient.

The coupling with a thermal analysis method (technical ATG, or DSC thermal analysis, differential scanning calorimetry or thermomicroscopique) allows to distinguish between two polymorphic whose RX diffractograms obtained are comparable.

TGA can be coupled with IR or mass spectrometry, DSC with RX. Raman spectroscopy is also part of complementary methods. ” The difficulty increases when we want to characterize the shape of the active ingredient in the finished product , says Fabienne Lacoulonche. example, by X-ray diffraction, the peaks related to the active ingredient in the diffractogram of the finished product may be masked by those excipients: it is then necessary to use other methods, such as Raman microscopy. “In general, a single method of analysis is not sufficient to characterize the polymorphism of an active substance in the active substance or finished product: the complementarity of different methods that will conclude precisely on the polymorphism of a crystalline substance.

In addition, ” the diffractometer remains an expensive device, which requires installation in an air-conditioned and a cooling room , “says Marchand Pierric (Holodiag). To this is added the need to have expertise and qualified personnel to carry out the analyzes. ” We must master these techniques and the ability to interpret the results , “says Jean-Rémi David (Calytherm). However, polymorphism is a “problem well under control , “said Stéphane Suchet (Axyntis),” systematically evaluated although it is however not always immune to miss a polymorphic form, knowing that the screening performed in the development can never be completely comprehensive … ”

FDA

FDA may refuse to approve an ANDA referencing a listed drug if the application contains insufficient information to show that the drug substance is the “same” as that of the reference listed drug. A drug substance in a generic drug product is generally considered to be the same as the drug substance in the reference listed drug if it meets the same standards for identity.

In most cases, the standards for identity are described in the USPalthough FDA may prescribe additional standards when necessary. Because drug product performance depends on the product formulation, the drug substance in a proposed generic drug product need not have the same physical form (particle size, shape, or polymorph form) as the drug substance in the reference listed drug. An ANDA applicant is required to demonstrate that the proposed product meets the standards for identity, exhibits sufficient stability and is bioequivalent to the reference listed drug.

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FDA PRESENTATION……polymorphs and co-crystals – ICDD      Regulatory Considerations on Pharmaceutical Solids: Polymorphs/Salts and Co-Crystals.. THIS IS A MUST READ ITEM

Over the years FDA has approved many generic drug products based upon a drug substance with different physical form from that of the drug substance in the respective reference listed drug (e.g., warfarin sodium, famotidine, and ranitidine). Also many ANDAs have been approved in which the drug substances differed from those in the corresponding reference listed drugs with respect to solvation or hydration state (e.g., terazosin hydrochloride, ampicillin, and cefadroxil). Several regulatory documents and literature reports (67-69) address issues relevant to the regulation of polymorphism.

The concepts and principles outlined in these are applicable for an ANDA. However, certain additional considerations may be applicable in case of ANDAs. Often at the time FDA receives an ANDA a monograph defining certain key attributes of the drug substance and drug product may be available in the Unites States Pharmacopoeia (USP). These public standards play a significant role in the ANDA regulatory review process and in case of polymorphism, when some differences are noted, lead to additional requirements and considerations.

This commentary is intended to provide a perspective on polymorphism in pharmaceutical solid in the context of ANDAs. It highlights major considerations for monitoring and controlling drug substance polymorphs and describes a framework for regulatory decisions regarding drug substance “sameness” considering the role and impact of polymorphism in pharmaceutical solids.

Since polymorphs exhibit certain differences in physical (e.g., powder flow and compactability, apparent solubility and dissolution rate) and solid state chemistry (reactivity) attributes that relate to stability and bioavailability it is essential that the product development and the FDA review process pay close attention to this issue.

This scrutiny is essential to ensure that polymorphic differences (when present) are addressed via design and control of formulation and process conditions to physical and chemical stability of the product over the intended shelf-life, and bioavailability/bioequivalence.

Most pharmaceuticals are distributed as solid doseages. In order to take action, they must dissolve in the gut and be absorbed into the blood stream. In many cases, the rate at which the drug dissolves can limit its effectiveness. Pharmaceutical compounds can be packed into more than one arrangement in the solid states known as polymorphs. Rapid and efficient methods of polymorph formation can be used to increase drug efficacy and shelf life.

Regulatory agencies worldwide require that, as part of any significant filing, a company has to demonstrate that it has made a reasonable effort to identify the polymorphs of their drug substance and has checked for polymorph interconversions. Due to the unpredictable behaviour of polymorphs and their respective differences in physicochemical properties, companies also have to demonstrate consistency in manufacturing between batches of the same product. Proper understanding of the polymorph landscape and nature of the polymorphs will contribute to manufacturing consistency.

Links

POLYMORPHISM AND PATENTS http://www.collegio.unibo.it/uploads/ideas/joelbernstein.pdf  A MUST CLICK FOR PHARMA CHEMISTS

Triclinic Labs approach to solid-state (solid form) screening and selection for optimal properties of an active pharmaceutical ingredient

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READ………..High-throughput crystallization: polymorphs, salts, co-crystalsand solvates of pharmaceutical solidshttp://citeseerx.ist.psu.edu/viewdoc/download?doi=10.1.1.85.5397&rep=rep1&type=pdf

Definitions

“Crystalline”, as the term is used herein, refers to a material, which may be hydrated and/or solvated, and has sufficient ordering of the chemical moiety to exhibit a discernable diffraction pattern by XRPD or other diffraction techniques. Often, a crystalline material that is obtained by direct crystallization of a compound dissolved in a solution or by interconversion of crystals obtained under different crystallization conditions, will have crystals that contain the solvent used in the crystallization, termed a crystalline solvate. Also, the specific solvent system and physical embodiment in which the crystallization is performed, collectively termed crystallization conditions, may result in the crystalline material having physical and chemical properties that are unique to the crystallization conditions, generally due to the orientation of the chemical moieties of the compound with respect to each other within the crystal and/or the predominance of a specific polymorphic form of the compound in the crystalline material.

Depending upon the polymorphic form(s) of the compound that are present in a composition, various amounts of the compound in an amorphous solid state may also be present, either as a side product of the initial crystallization, and/or a product of degradation of the crystals comprising the crystalline material. Thus, crystalline, as the term is used herein, contemplates that the composition may include amorphous content; the presence of the crystalline material among the amorphous material being detectably among other methods by the composition having a discernable diffraction pattern.

The amorphous content of a crystalline material may be increased by grinding or pulverizing the material, which is evidenced by broadening of diffraction and other spectral lines relative to the crystalline material prior to grinding. Sufficient grinding and/or pulverizing may broaden the lines relative to the crystalline material prior to grinding to the extent that the XRPD or other crystal specific spectrum may become undiscernable, making the material substantially amorphous or quasi-amorphous. Continued grinding would be expected to increase the amorphous content and further broaden the XRPD pattern with the limit of the XRPD pattern being so broadened that it can no longer be discerned above noise. When the XRPD pattern is broadened to the limit of being indiscernible, the material may be considered no longer a crystalline material, but instead be wholly amorphous. For material having increased amorphous content and wholly amorphous material, no peaks should be observed that would indicate grinding produces another form.

“Amorphous“, as the term is used herein, refers to a composition comprising a compound that contains too little crystalline content of the compound to yield a discernable pattern by XRPD or other diffraction techniques. Glassy materials are a type of amorphous material. Glassy materials do not have a true crystal lattice, and technically resembling very viscous non-crystalline liquids. Rather than being true solids, glasses may better be described as quasi-solid amorphous material. “Broad” or “broadened”, as the term is used herein to describe spectral lines, including XRPD, NMR and IR spectroscopy, and Raman spectroscopy lines, is a relative term that relates to the line width of a baseline spectrum. The baseline spectrum is often that of an unmanipulated crystalline form of a specific compound as obtained directly from a given set of physical and chemical conditions, including solvent composition and properties such as temperature and pressure.

For example, broadened can be used to describe the spectral lines of a XRPD spectrum of ground or pulverized material comprising a crystalline compound relative to the material prior to grinding. In materials where the constituent molecules, ions or atoms, as solvated or hydrated, are not tumbling rapidly, line broadening is indicative of increased randomness in the orientation of the chemical moieties of the compound, thus indicative of an increased amorphous content. When comparisons are made between crystalline materials obtained via different crystallization conditions, broader spectral lines indicate that the material producing the relatively broader spectral lines has a higher level of amorphous material.

“About” as the term is used herein, refers to an estimate that the actual value falls within ±5% of the value cited. “Forked” as the term is used herein to describe DSC endotherms and exotherms, refers to overlapping endotherms or exotherms having distinguishable peak positions

Classes of multicomponent pharmaceutical materials. (a) Schematic of crystalline materials showing neutral and charged species. The red box indicates polymorphs are possible for all the multicomponent crystals contained within the box (adapted from Reference 7). (b) Schematic of amorphous solid dispersions showing binary, ternary, and quaternary possibilities for polymers and surfactants. Other solubilization techniques using cyclodextrins and phospholipids are included for completeness but have a different mechanism for solubilization when compared to polymer and surfactant systems.

The red box indicates that properties can change with water or solvent content. General methods for precipitating and crystallizing a compound may be applied to prepare the various polymorphs described herein. These general methods are known to those skilled in the art of synthetic organic chemistry and pharmaceutical formulation, and are described, for example, by J. March, “Advanced Organic Chemistry: Reactions, Mechanisms and Structure ” 4th Ed. (New York: Wiley-Interscience, 1992).

In general, a given polymorph of a compound may be obtained by direct crystallization of the compound or by crystallization of the compound followed by inter-conversion from another polymorphic form or from an amorphous form. Depending on the method by which a compound is crystallized, the resulting composition may contain different amounts of the compound in crystalline form as opposed to as an amorphous material.

Also, the resulting composition may contain differing mixtures of different polymorphic forms of the compound. Compositions comprising a higher percentage of crystalline content {e.g., forming crystals having fewer lattice defects and proportionately less glassy material) are generally prepared when using conditions that favor slower crystal formation, including slow solvent evaporation and those affecting kinetics.

Crystallization conditions may be appropriately adjusted to obtain higher quality crystalline material as necessary. Thus, for example, if poor crystals are formed under an initial set of crystallization conditions, the solvent temperature may be reduced and ambient pressure above the solution may be increased relative to the initial set of crystallization conditions in order to slow down crystallization. Precipitation of a compound from solution, often affected by rapid evaporation of solvent, is known to favor the compound forming an amorphous solid as opposed to crystals. A compound in an amorphous state may be produced by rapidly evaporating solvent from a solvated compound, or by grinding, pulverizing or otherwise physically pressurizing or abrading the compound while in a crystalline state.

Seven crystalline forms and one amorphous solid were identified by conducting a polymorph screen (Example 3). Described herein are Form A, Form B, Form C, Form D, Form E, Form F, Form G, and Amorphous Form of Compound I. Where possible, the results of each test for each different polymorph are provided. Forms A, C, D and E were prepared as pure forms. Forms B, F, and G were prepared as mixtures with Form A.
Various tests were performed in order to physically characterize the polymorphs of Compound I including X-ray powder diffraction (XRPD), differential scanning calorimetry (DSC), thermogravimetric analysis (TGA), hot stage microscopy, Fourier transform infrared spectroscopy (FT-IR), Fourier transform Raman spectrometry, linked thermogravimetric-infrared spectroscopy (TG-IR), solution proton nuclear magnetic resonance (1H-NMR), solid state 13carbon nuclear magnetic resonance (13C-NMR), and moisture sorption and desorption analysis (M S/Des).

 

Salt screening

Physicochemical properties of drug substances, such as solubility, dissolution rate, and physicochemical stability can be altered significantly by salt formation. Consequently, important properties of the drug product such as bioavailability or shelve life can be radically influenced. Crystallics’ technology platform for crystallization screening accommodates salt screening studies using only minimal amounts of drug substance while still performing a large number of experiments. High-throughput salt screening is used for both early phase salt selection studies and broad patent protection.

Salt selection – A powerful strategy for crystal form optimization

Pharmaceutical developers have focused efforts on finding and formulating a thermodynamically stable crystalline form with acceptable physical properties for a given compound. This is reasonable, given the need to avoid cascading from a meta-stable form to a more stable one in unpredictable fashion.

Occasionally certain physical properties, such as low aqueous solubility, are limiting to performance of the compound, leading to poor oral bioavailability or insufficient solubility for an injection formulation. One of the main strategies used to affect physical performance of a compound and one that is often employed by pharmaceutical scientists is the practice of salt selection (23). At least half of compounds in marketed products are in the form of a salt for one reason or another.

This fact alone speaks to the versatility of the salt selection approach. Salt forms of a pharmaceutical can have many benefits, such as improved stability characteristics, optimal bioavailability and aqueous solubility for an injectable formulation. Salts, like all other crystalline forms, are subject to polymorphism and solvate formation, thus requiring the same form identification studies as are needed for a neutral compound.

A remarkable example of co-optimization of properties is indinavir (HIV protease inhibitor), which is marketed as the sulfate salt ethanol solvate (24,25) The crystalline free base has variable oral bioavailability in dogs (26,27) and humans (28). While acidic solutions of the base compound showed good oral pharmacokinetics, the stability of the drug in acidic solution is not consistent with a product (26). Therefore, the discovery of the salt form ensured both shelf stability and robust bioavailability performance. The salt selection strategy is limited in two ways.

First, salt formation relies on the presence of one or more ionizable functional groups in the molecule; many drugs and development compounds lack this feature.

Second, our ability to predict a priori whether a given compound will form a crystalline salt (or salts) is non-existent. The ability to actively identify crystalline salt forms has been confined to manual empirical evaluation using multiple salt formers for a given acid or base. Recently advances have been made in the area of high-throughput salt selection and crystal engineering strategies associated with salt formation (14,29-32).

In one case, we have advocated the simultaneous assessment of polymorphism as a way to help rank the developability of different crystalline salts (14). While salt forms will continue to have a prominent place in pharmaceutical science, the need for enhanced productivity dictates that every advantage must be sought to aid the design of an appropriate crystalline form of an active molecule.

Specifically, the ability to design scaffolds into crystalline forms will enhance our capacity to convert interesting molecules into effective drugs. Crystal engineering offers some additional tools in this regard. 

CASE STUDY FORM A ONLY US8084605

Figure imgf000073_0001TRELAGLIPTIN SUCCINATE

Form A may be prepared by crystallization from the various solvents and under the various crystallization conditions used during the polymorph screen (e.g., fast and slow evaporation, cooling of saturated solutions, slurries, and solvent/antisolvent additions). Tables B and C of Example 3 summarize the procedures by which Form A was prepared.

For example, Form A was obtained by room temperature slurry of an excess amount of Compound I in acetone, acetonitrile, dichloromethane, 1,4-dioxane, diethyl ether, hexane, methanol, isopropanol, water, ethylacetate, tetrahydrofuran, toluene, or other like solvents on a rotating wheel for approximately 5 or 7 days.

The solids were collected by vacuum filtration, and air dried in the hood. Also, Form A was precipitated from a methanol solution of Compound I by slow evaporation (SE). Form A was characterized by XRPD, TGA, hot stage microscopy, IR, Raman spectroscopy, solution 1H-NMR, and solid state 13C-NMR. Figure 1 shows a characteristic XRPD spectrum (CuKa, λ=1.5418A) of Form A. The XRPD pattern confirmed that Form A was crystalline. Major X-Ray diffraction lines expressed in °2Θ and their relative intensities are summarized in Table 1. Table 1. Characteristic XRPD Peaks (CuKa) of Form A

Figure imgf000018_0001 Figure imgf000019_0001

The above set of XRPD peak positions or a subset thereof can be used to identify Form A. One subset comprises peaks at about 11.31, 11.91, 12.86, 14.54, 15.81, 16.83, 17.59, 19.26, 19.52, 21.04, 22.32, 26.63, and 29.87 °2Θ. Another subset comprises peaks at about 11.31, 11.91, 19.26, 21.04, and 22.32 °2Θ; the peaks of this subset show no shoulder peaks or peak split greater than 0.2 °2Θ. Another subset comprises peaks at about 11.31, 11.91 and 22.32 °2Θ. Figure 2 is a TGA thermogram of Form A. TGA analysis showed that Form A exhibited insignificant weight loss when heated from 25 0C to 165 0C; this result is indicative that Form A was an anhydrous solid. Figure 3 shows a characteristic DSC thermogram of Form A. DSC analysis showed a single endothermic event occurred at approximately 195 0C (peak maximum). This endothermic event was confirmed by hot stage microscopy which showed the melting of Form A, which onset around 177 0C and the melting point estimated to be at approximately 184 0C. 

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US8084605

Figure 4 (A-D) shows a characteristic FT-IR spectrum of Form A. The major bands expressed in reciprocal wavelengths (wavenumber in cm”1) are positioned at about 3815, 3736, 3675, 3460, 3402, 3141, 3098, 3068, 3049, 2953, 2934, 2854, 2760, 2625, 2536, 2481, 2266, 2225, 2176, 1990, 1890, 1699, 1657, 1638, 1626, 1609, 1586, 1553, 1517, 1492, 1478, 1450, 1419, 1409, 1380, 1351, 1327, 1289, 1271, 1236, 1206, 1180, 1158, 1115, 1087, 1085, 1064, 1037, 1027, 971, 960, 951, 926, 902, 886, 870, 831, 820, 806, 780, 760, 740, 728, 701, 685, 668, 637, 608, 594, 567, 558, and 516 cm”1 (values rounded to the nearest whole number). This unique set of IR absorption bands or a subset thereof can be used to identify Form A.

One such subset comprises absorption bands at about 3141, 3098, 3068, 3049, 2953, 2934, 2854, 2266, 2225, 1699, 1657, 1609, 1586, 1553, 1517, 1492, 1478, 1450, 1380, 1351, 1327, 1236, 1206, 1115, 1063, 902, 886, 870, 820, 780, 760, 685, 608, 594, and 516 cm 1. Another subset comprises absorption bands at about 3141, 2953, 2934, 2854, 2266, 2225, 1699, 1657, 1450, 1206, 886, 760, 685, 594, and 516 cm 1. Yet another subset comprises absorption bands at about 3141, 2953, 2934, 2266, 1699, 1657, 1450, and 1206 cm 1.

Links

Aprepitant case study FTIR.. READING MATERIAL http://alpha.chem.umb.edu/chemistry/ch361/spring%2005/ftir%20polymorph.pdf

Figure 5 (A-D) shows a characteristic Raman spectrum of Form A. The major Raman bands expressed in reciprocal wavelengths (wavenumber in cm”1) are positioned at about 3100, 3068, 3049, 2977, 2954, 2935, 2875, 2855, 2787, 2263, 2225, 2174, 1698, 1659, 1626, 1607, 1586, 1492, 1478, 1451, 1439, 1409, 1400, 1382, 1351, 1328, 1290, 1281, 1271, 1237, 1223, 1213, 1180, 1155, 1134, 1115, 1084, 1063, 1035, 971, 952, 926901, 868, 805, 780, 759, 740, 727, 701, 686, 669, 609, 594, 566, 558, 516, 487, 479, 433, 418, 409, 294, 274, 241, 218, 191 and 138 cm”1 (values rounded to the nearest whole number). This unique set of Raman bands or a subset thereof may be used to identify Form A.

One such subset comprises Raman bands at about 2954, 2935, 2225, 1698, 1659, and 1607 cm”1. Another subset comprises Raman bands at about 3068, 2954, 2935, 2225, 1698, 1659, 1607, 1586, 1223, 1180, 901, 780, 759, 669, and 516 cm”1. Yet another subset comprises Raman bands at about 3100, 3068, 2225, 1698, 1659, 1607, 1586, 1351, 1237, 1223, 1180, 1155, 1134, 1115, 1063, 952, 926, 901, 868, 805, 780, 759, 740, 669, 609, and 516 cm”1.

Form A was further characterized by solution 1H NMR and solid-state 13carbon NMR. The spectra are reported in Figures 6 and 7, respectively. Chemical assignments were not performed; however, the spectra are consistent with the known chemical structure of Compound I. US8084605

Figure imgf000073_0001 Example 11. Characterization of Form A Material prepared by the procedure of Example 1 was designated as Form A. The material was characterized by XRPD, TGA, DSC, hot stage microscopy, FT-IR, FT- Raman, 1H NMR, and 13C NMR. The analyses were conducted according to the procedures outlined in Section B of Example 3.

The characteristic spectra and thermograms for Form A are reported in Figures 1-7. The characterization data are summarized in Table D. Table D. Characterization Data of Form A of Compound I US8084605

Figure imgf000064_0001

Amorphous solid dispersion screening

Using the amorphous form of a drug substance offers several advantages with respect to dissolution rate and solubility of the substance. However, reduced chemical stability, increased hygroscopicity and, most important, physical instability are the major drawbacks of using the amorphous phase in the final drug product. These drawbacks can be overcome by stabilizing the amorphous phase of the API in a polymer matrix, e.q. an amorphous solid dispersion. Amorphous phases dissolve more rapidly than crystalline forms, and can significantly increase bioavailability of poorly water soluble drugs substances. However, the use of amorphous materials requires confidence that crystallization will not occur during the product lifespan. For a material that has never been obtained in a crystalline form, focus should be put on attempting to crystallize it. Crystallics has extensive experience of obtaining crystalline phases from amorphous materials.

Dispersions of a drug substance onto a polymeric matrix has received increased attention in recent years. A successful dispersion results in an amorphous solid material and will show improved dissolution rates and higher apparent solubility characteristics, as well as, sufficient resistance to chemical degradation and should be physically stable e.q. sufficient high glass transition temperature avoiding crystallization of the API.

A variety of factors contribute to the formation of a suitable Amorphous Solid Dispersion (ASD), including the nature of the polymer, the drug polymer ratio, the impact of surfactants and the solvent used in the process. Crystallics has developed high-throughput solid dispersion screening technology in order to find the optimal combination of these factors.

Example 10. Preparation of Amorphous Form US8084605

A sample of Compound I (40 mg) was dissolved in 1000 μl of water. The solution was filtered through a 0.2 μm nylon filter into a clean vial then frozen in a dry ice/acetone bath. The vials were covered with a Kimwipe then placed on a lyophilizer overnight. The resulting solids yielded Amorphous Form. 8. Amorphous Form The Amorphous Form of Compound I was prepared by lyophilization of an aqueous solution of Compound I (Example 10). The residue material was characterized by XRPD and the resulting XRPD spectrum displayed in Figure 26. The XRPD spectrum shows a broad halo with no specific peaks present, which confirms that the material is amorphous. The material was further characterized by TGA, DSC, hot stage microscopy, and moisture sorption analysis. 

TGA analysis (Figure 27) showed a 1.8% weight loss from 25 0C to 95 0C, which was likely due to loss of residual solvent. 

DSC analysis (Figure 28) showed a slightly concave baseline up to an exotherm at 130 0C (recrystallization), followed by an endotherm at 194 0C, which results from the melting of Form A. Hot stage microscopy confirmed these recrystallization and melting events (micrographs not included). An approximate glass transition was observed (Figure29) at an onset temperature of 82 0

C. 

Moisture sorption/desorption data (Figure 30 and Example 25) showed a 1.0% weight loss on equilibration at 5% relative humidity. Approximately 8% of weight was gained up to 65% relative humidity. Approximately 7% of weight was lost at 75% relative humidity. This is likely due to the recrystallization of the amorphous material to a crystalline solid. A 4.4% weight gain was observed on sorption from 75% to 95% relative humidity. Approximately 4.7% weight was lost on desorption from 95% to 5% relative humidity. 

The solid material remaining after the moisture sorption analysis was determined to be Form A by XRPD (Figure 31). Table H. Characterization Data of Amorphous Form US8084605

Figure imgf000068_0001

T=temperature, RH=relative humidity, MB = moisture sorption/desorption analysis Example 19: Relative Humidity Stressing Experiments

 Moisture Sorption/Desorption Study of Amorphous Form.
Mositure sorption and desorption study was conducted on a sample of Amorphous Form. The sample was prepared by lyophilolization of a solution of Compound I in water (Example 3, section A.9). The mositure sorption and desorption study was conducted according to the procedures outlined in Example 3, section B.10. The data collected is plotted in Figure 29 and summarized in Table N .Table N. Moisture Sorption/Desorption of Amorphous Form
Figure imgf000072_0001

Table B. Crystallization Experiments of Compound I from Solvents

Figure imgf000059_0001
Figure imgf000060_0001
Figure imgf000061_0001
Figure imgf000062_0001

a) FE = fast evaporation; SE = slow evaporation; RT = room temperature; SC = slow cool; CC = crash cool, MB = moisture sorption/desorption analysis b) qty = quantity; PO = preferred orientation Table C. Crystallization Experiments of Compound I in Various Solvent/Antisolvent

Figure imgf000062_0002

a precipitated by evaporation of solvent Table A. Approximate Solubilities of Compound I US8084605

Figure imgf000052_0001
Figure imgf000053_0001

a) Approximate solubilities are calculated based on the total solvent used to give a solution; actual solubilities may be greater because of the volume of the solvent portions utilized or a slow rate of dissolution. Solubilities are reported to the nearest mg/mL.

Example 3.

Polymorph Screen Compound I as prepared by the method described in Example 1 was used as the starting material for the polymorph screen. Solvents and other reagents were of ACS or HPLC grade and were used as received. A. Sample Generation. Solids for form identification were prepared via the following methods from Compound I.

1. Fast Evaporation (FE) A solution of Compound I was prepared in test solvents. The sample was placed in the hood, uncovered, to evaporate under ambient conditions. The solids were analyzed by XRPD for form identification.

2. Slow Evaporation (SE) A solution of Compound I was prepared in test solvents. The sample was placed in the hood, covered with foil rendered with pinholes, to evaporate under ambient conditions. The solids were analyzed by XRPD for form identification.

3. Room Temperature (RT) Slurries An excess amount of Compound I was slurried in test solvent on a rotating wheel for approximately 5 or 7 days. The solids were typically collected by vacuum filtration, air dried in the hood, and analyzed by XRPD for form identification.

4. Elevated Temperature Slurries Excess Compound I was slurried in test solvents at 47 0C on a shaker block for approximately 5 days. The solids were collected by vacuum filtering, dried in the hood, and then analyzed by XRPD for form identification.

5. Slow Cooling Crystallization (SC)

A saturated or near saturated solution of Compound I was prepared at elevated temperature. The samples were filtered through warmed 0.2 μm filters into warmed vials. The heat source was turned off and the samples slowly cooled to ambient temperature. If precipitation did not occur within a day the samples were placed in the refrigerator. The samples were transferred to a freezer if precipitation did not occur within several days. The solids were collected by decanting the solvent or vacuum filtration, dried in the hood and analyzed by XRPD for form identification.

6. Crash Cooling Crystallization (CC) A saturated or near saturated solution of Compound I was prepared at elevated temperature. The samples were filtered through warmed 0.2 μm filters into warmed vials then rapidly cooled in an acetone/dry ice or ice bath. If precipitation did not occur after several minutes the samples were placed in the refrigerator or freezer. Solids were collected by decanting solvent or vacuum filtration, dried in the hood, and then analyzed by XRPD. Samples that did not precipitate under subambient conditions after several days were evaporated in the hood and analyzed by XRPD for form identification.

7. Solvent/Antisolvent Crystallization (S/AS) A solution of Compound I was prepared in test solvent. A miscible antisolvent was added with a disposable pipette. Precipitate was collected by vacuum filtration or decanting solvent. The samples were stored under subambient conditions if precipitation did not occur. If solids were not observed after several days the samples were evaporated in the hood. Collected solids were analyzed by XRPD for form identification.

8. Relative Humidity (RH) Stressing Experiments Samples of Compound I were placed uncovered in approximately 58%, 88%, and 97% relative humidity jars. The samples were stored in the jars for approximately 8 days. The solids were collected and analyzed by XRPD for form identification.

9. Lyophilization Compound I was dissolved in water in a glass vial. The solution was frozen by swirling the vial in an acetone/dry ice bath. The frozen sample was placed on the lyophilizer until all of the frozen solvent was removed. The solids were collected and analyzed by XRPD for form identification.

10. Grinding Experiments Aliquots of Compound I were ground manually with a mortar and pestle as a dry solid and a wet paste in water. The samples were ground for approximately three minutes. The solids were collected and analyzed by XRPD for form identification.

11. Dehydration Experiments Hydrated samples of Compound I were dehydrated at ambient conditions (2 days) and in an ambient temperature vacuum oven (1 day). The solids were collected and analyzed by XRPD for form identification.

12. Vapor Stress Experiments Amorphous Compound I was placed in acetone, ethanol, and water vapor chambers for up to eight days. The solids were collected and analyzed by XRPD for form identification.

STABILITY STUDY Stability studies are commonly performed for new drug entities with chemical stability and impurity formation being investigated. It is also important to monitor the physical stability under these same conditions to anticipate any form changes that may occur. As an example, many hydrates will dehydrate to a lower hydrate or anhydrous form at elevated temperatures. Anhydrous materials can also undergo form transformations to other anhydrous forms upon heating.

These types of changes can be monitored using heating studies in an oven with subsequent XRPD analysis or in-situ variable temperature XRPD can be used to look for changes. In other cases, anhydrates will convert to hydrates or the API in an amorphous solid dispersion may crystallize under elevated relative humidity (RH) conditions.

Equilibration in RH chambers with subsequent analysis by XRPD or in-situ variable RH XRPD experiments can be used to readily identify these form changes. Once the effect of temperature and RH on form changes is understood, this can be factored into other processes such as drying, formulation, storage, and packaging B. Sample Characterization. The following analytical techniques and combination thereof were used determine the physical properties of the solid phases prepared.

1. X-Ray Powder Diffraction (XRPD)

XRPD is commonly used as the initial method of analysis for form screens. For polymorph, salt, and co-crystal screens XRPD is used to determine if a new form has been produced by comparing the powder pattern to all known forms of the API and the counterion/guest. If a new form is found by XRPD, additional characterization by other methods is in order. For amorphous solid dispersion screens, XRPD is used to confirm a lack of crystallinity indicated by an amorphous halo in the powder pattern.

The halos will move depending on the concentration and interactions of the API and polymer. Computational methods have also been used with XRPD data to establish miscibility of amorphous solid dispersions X-ray powder diffraction is a front line technique in solid form screening and selection based on its ability to give a fingerprint of the solid-state structure of a pharmaceutical material. Understanding the solid forms of a pharmaceutical compound provides a road map to help direct a variety of development activities ranging from crystallization, formulation, packaging, storage, and performance.

Different screening and selection strategies are warranted in early and late development because different information is needed at the various stages. Solid form selection and formulation approaches need to be investigated together and tailored to the situation. It is important to include solid form selection and possible changes in form as part of the risk management strategy throughout the drug development process.

X-ray powder diffraction (XRPD) analyses were performed using an Inel XRG- 3000 diffractometer equipped with a CPS (Curved Position Sensitive) detector with a 2Θ (2Θ) range of 120°. Real time data were collected using Cu-Ka radiation starting at approximately 4 °2Θ at a resolution of 0.03 °2Θ. The tube voltage and amperage were set to 40 kV and 30 mA, respectively. The pattern is displayed from 2.5 to 40 °2Θ. Samples were prepared for analysis by packing them into thin- walled glass capillaries. Each capillary was mounted onto a goniometer head that is motorized to permit spinning of the capillary during data acquisition. The samples were analyzed for approximately 5 minutes.

Instrument calibration was performed using a silicon reference standard. Peak picking was performed using the automatic peak picking in the Shimadzu XRD-6000 Basic Process version 2.6. The files were converted to Shimadzu format before performing the peak picking analysis. Default parameters were used to select the peaks.

2. Thermogravimetric Analysis (TGA)

Thermogravimetric (TG) analyses were performed using a TA Instruments 2950 thermogravimetric analyzer. Each sample was placed in an aluminum sample pan and inserted into the TG furnace. The furnace was first equilibrated at 25 0C, then heated under nitrogen at a rate of 10 °C/min, up to a final temperature of 350 0C. Nickel and Alumel™ were used as the calibration standards.

3. Differential Scanning Calorimetry (DSC)

Differential scanning calorimetry (DSC) was performed using a TA Instruments differential scanning calorimeter 2920. The sample was placed into an aluminum DSC pan, and the weight accurately recorded. The pan was covered with a lid and then crimped. The sample cell was equilibrated at 25 0C and heated under a nitrogen purge at a rate of 10 °C/min, up to a final temperature of 350 0C. Indium metal was used as the calibration standard. Reported temperatures are at the transition maxima. For studies of the glass transition temperature (Tg) of the amorphous material, the sample cell was equilibrated at ambient temperature, then heated under nitrogen at a rate of 20 °C/min, up to 100 0C. The sample cell was then allowed to cool and equilibrate at -20 0C. It was again heated at a rate of 20 °C/min up to 100 0C and then cooled and equilibrated at -20 0C. The sample cell was then heated at 20 °C/min up to a final temperature of 350 0C. The Tg is reported from the onset point of the transition.

4. Hot Stage Microscopy.

Hot stage microscopy was performed using a Linkam hot stage (model FTIR 600) mounted on a Leica DM LP microscope. The samples were prepared between two cover glasses and observed using a 20χ objective with crossed polarizers and first order compensator. Each sample was visually observed as the stage was heated. Images were captured using a SPOT Insight™ color digital camera with SPOT Software v. 3.5.8. The hot stage was calibrated using USP melting point standards.

5. Thermogravimetric-Infrared (TG-IR)

Thermogravimetric infrared (TG-IR) analyses were acquired on a TA Instruments thermogravimetric (TG) analyzer model 2050 interfaced to a Magna 560® Fourier transform infrared (FT-IR) spectrophotometer (Thermo Nicolet) equipped with an Ever-Glo mid/far IR source, a potassium bromide (KBr) beamsplitter, and a deuterated triglycine sulfate (DTGS) detector. The TG instrument was operated under a flow of helium at 90 and 10 cc/min for the purge and balance, respectively. Each sample was placed in a platinum sample pan, inserted into the TG furnace, accurately weighed by the instrument, and the furnace was heated from ambient temperature to 250 0C at a rate of 20 °C/min.

The TG instrument was started first, immediately followed by the FT-IR instrument. Each IR spectrum represents 32 co-added scans collected at a spectral resolution of 4 cm“1. A background scan was collected before the beginning of the experiment. Wavelength calibration was performed using polystyrene. The TG calibration standards were nickel and Alumel™. Volatiles were identified from a search of the High Resolution Nicolet TGA Vapor Phase spectral library.

6. Fourier Transform Infrared Spectroscopy (FT-IR)

Infrared spectra were acquired on a Magna-IR 560® or 860® Fourier transform infrared (FT-IR) spectrophotometer (Thermo Nicolet) equipped with an Ever-Glo mid/far IR source, an extended range potassium bromide (KBr) beamsplitter, and a deuterated triglycine sulfate (DTGS) detector. A diffuse reflectance accessory (the Collector™, Thermo Spectra-Tech) was used for sampling. Each spectrum represents 256 co-added scans collected at a spectral resolution of 4 cm“1. Sample preparation consisted of physically mixing the sample with KBr and placing the sample into a 13 -mm diameter cup. A background data set was acquired on a sample of KBr. A Log 1/R (R = reflectance) spectrum was acquired by taking a ratio of these two data sets against each other. Wavelength calibration was performed using polystyrene. Automatic peak picking was performed using Omnic version 7.2.

7. Fourier Transform Raman Spectroscopy (FT-Raman)

FT-Raman spectra were acquired on a Raman accessory module interfaced to a Magna 860® Fourier transform infrared (FT-IR) spectrophotometer (Thermo Nicolet). This module uses an excitation wavelength of 1064 nm and an indium gallium arsenide (InGaAs) detector. Approximately 0.5 W of Nd)YVO4 laser power was used to irradiate the sample. The samples were prepared for analysis by placing the material in a glass tube and positioning the tube in a gold-coated tube holder in the accessory. A total of 256 sample scans were collected from at a spectral resolution of 4 cm“1, using Happ-Genzel apodization. Wavelength calibration was performed using sulfur and cyclohexane. Automatic peak picking was performed using Omnic version 7.2.

8. Solid State Nuclear Magnetic Resonance Spectroscopy (13C-NMR)

The solid-state 13C cross polarization magic angle spinning (CP/MAS) NMR spectrum was acquired at ambient temperature on a Varian UN1TYINOVA-400 spectrometer (Larmor frequencies: 13C = 100.542 MHz, 1H = 399.799 MHz). The sample was packed into a 4 mm PENCIL type zirconia rotor and rotated at 12 kHz at the magic angle. The spectrum was acquired with phase modulated (SPINAL-64) high power 1H decoupling during the acquisition time using a 1H pulse width of 2.2 μs (90°), a ramped amplitude cross polarization contact time of 5 ms, a 30 ms acquisition time, a 10 second delay between scans, a spectral width of 45 kHz with 2700 data points, and 100 co-added scans. The free induction decay (FID) was processed using Varian VNMR 6.1C software with 32768 points and an exponential line broadening factor of 10 Hz to improve the signal-to- noise ratio. The first three data points of the FID were back predicted using the VNMR linear prediction algorithm to produce a flat baseline. The chemical shifts of the spectral peaks were externally referenced to the carbonyl carbon resonance of glycine at 176.5 ppm. 9. Solution Nuclear Magnetic Resonance Spectroscopy (1H-NMR) The solution 1H NMR spectrum was acquired at ambient temperature with a

Figure imgf000058_0001

spectrometer at a 1H Larmor frequency of 399.803 MHz. The sample was dissolved in methanol. The spectrum was acquired with a 1H pulse width of 8.4 μs, a 2.50 second acquisition time, a 5 second delay between scans, a spectral width of 6400 Hz with 32000 data points, and 40 co-added scans. The free induction decay (FID) was processed using Varian VNMR 6.1C software with 65536 points and an exponential line broadening factor of 0.2 Hz to improve the signal-to-noise ratio. The spectrum was referenced to internal tetramethylsilane (TMS) at 0.0 ppm. 10.

Moisture Sorption/Desorption Analysis Moisture sorption/desorption data were collected on a VTI SGA-100 Vapor Sorption Analyzer. Sorption and desorption data were collected over a range of 5% to 95% relative humidity (RH) at 10% RH intervals under a nitrogen purge. Samples were not dried prior to analysis. Equilibrium criteria used for analysis were less than 0.0100% weight change in 5 minutes, with a maximum equilibration time of 3 hours if the weight criterion was not met. Data were not corrected for the initial moisture content of the samples. NaCl and PVP were used as calibration standards

Does solid form matter? 

Sometimes the properties of two solid forms of a drug are quite similar. In other cases, the physical and chemical properties can vary dramatically and have great impact on pharmacokinetics, ease of manufacturing, and dosage form stability. Properties that can differ among solid forms of a substance include color, solubility, crystal shape, water sorption and desorption properties, particle size, hardness, drying characteristics, flow and filterability, compressibility, and density.

Different solid forms can have different melting points, spectral properties, and thermodynamic stability. In a drug substance, these variations in properties can lead to differences in dissolution rate, oral absorption, bioavailability, levels of gastric irritation, toxicology results, and clinical trial results. Ultimately both safety and efficacy are impacted by properties that vary among different solid forms. Stability presents a special concern, since it’s easy to inadvertently generate the wrong form at any point in the development process.

Because energy differences between forms are usually relatively small, form interconversion is common and can occur during routine API manufacturing operations and during drug product formulation, storage, and use. The stakes are high. Encountering a new solid form during late stages of development can delay filing. A new form appearing in drug product can cause product withdrawal.  

When should a search for solid forms begin?

The key to speed in the drug development process is to do it right the first time. For solid pharmaceuticals, that means:

  • identify the optimum solid form early in drug development
  • make the same form for clinical material and commercial API
  • develop a crystallization process that assures control of solid form
  • produce a drug product with solid form stability through expiration

scientists strongly recommend that investigation of possible solid forms of a new chemical entity be carried out as early in the development process as drug supply will allow. The best approach has three stages. The first stage, more relevant to some development processes than to others, is a milligram-scale abbreviated screen on efficacious compounds prior to final IND candidate selection. This early information can be used to guide selection of salts and solid forms for scale-up and toxicology studies. The second stage is full polymorph screening and selection of optimum solid form. This stage is important to all development processes and should certainly occur before the first GMP material is produced. In the case of ionic drugs, various salts should be prepared and screened for polymorphs and hydrates. The third stage, an exhaustive screen carried out before drug launch, is an effort to find and patent all of the forms of a high-potential drug. Staging the screening in this way optimizes the balance among the factors of early knowledge of options, probability of commercial success, and judicious investment of R&D money.

Delay in understanding solid form issues results in problems like different batches of clinical material having different solid forms. Another common and preventable dilemma arises when clinical trials are carried out with one form while commercial production generates another. In this case, bridging studies are required to demonstrate to regulatory agencies that the clinicals are relevant. ICH guidelines require a search for solid forms, comparison of properties that might affect product efficacy, and, if appropriate, setting of solid form specifications.

How is solid form controlled in API manufacture? 

It is important to control solid form during API synthesis in order to demonstrate complete process control to regulatory agencies. Different solid forms can have different solubilities and can affect recovery of API. Purification efficiencies can vary due to differential exclusion of impurities. Filtration and transfer characteristics often differ between forms. Ease of drying can vary due to different abilities to bind solvent and water in the crystal lattice. A prevalent but incorrect belief is that solid form is determined primarily by choice of crystallization solvent. In fact, it is well established that parameters like temperature, supersaturation level, rate of concentration or cooling, seeding, and ripening can have an overriding effect. These variables must be controlled to ensure consistency of solid form in API.

Can solid form problems arise in drug products, too? 

The potential for solid form variation does not end at API production. Solid form issues remain through formulation, manufacture, storage, and use of drug product. It is common to observe form transformation during standard manufacturing operations like wet granulation and milling. Excipient interactions and compaction can induce form changes. Changes can occur in the final dosage form over time. Suspensions, including those in transdermal patches, are particularly vulnerable because they provide a low-energy pathway (dissolution/recrystallization) for form interconversion. Lyophile cakes are normally amorphous, but can crystallize on storage leading to difficulty in reconstitution. Even products containing drug in solution, such as filled gel caps, can be affected if the solution is or becomes supersaturated with respect to one of the possible solid forms of the drug.

How can you tell when you have a solid form problem? 

Whenever there is a specification failure in drug product or drug substance, solid form changes should be considered in the search for causes. Particularly symptomatic is failure to meet melting point or dissolution specifications. Changes in humidity, crystallization conditions, or crystallization solvent can produce unwanted forms. Solvents known to readily produce solvates include water, alcohols, chlorinated hydrocarbons, cyclic ethers, ketones, nitriles, and amides. Changes in the appearance of gel caps or cracking of tablet coatings can indicate solid form problems. Various solid-state analytical techniques can be used to identify solid form in API. Some techniques can even determine solid form of API in intact final dosage form. Among the most useful techniques for solid-state characterization are melting point, DSC, TGA, hot stage and optical microscopy, solid-state NMR, IR and Raman spectroscopy, and X-ray powder diffraction.

Is there any good news about polymorphism? 

Polymorphism presents opportunities as well as challenges. Investigation of the properties of different forms of a commercial drug can lead to new products with improved onset time, greater bioavailability, sustained release properties, or other therapeutic enhancements. New forms can bring improvements in manufacturing costs or API purity. These improvements are patentable and can provide a competitive advantage. An underutilized potential of polymorphism is to solve formulation problems that cause the abandonment of potentially useful drugs in which much investment has already been made. 

SOLUBILITY

Solubility is an important parameter for new molecules especially with the emergence of many poorly soluble compounds in the drug discovery and development pipeline. Polymorphic forms can exhibit solubility differences that vary within a factor of 1-5, amorphous solid dispersions show an improvement one or two orders of magnitude higher, and salts and co-crystals fall between these extremes . A comparison of solubility values of pure forms will provide important information when deciding on a solid form or dosage form. X-ray powder diffraction will allow identification of pure forms for these types of measurements.

However, form changes during solubility and dissolution experiments are also possible and need to be investigated. Solids remaining at the end of solubility and dissolution experiments should always be analyzed initially by XRPD to determine if a form transformation has occurred under these conditions. If a form change has occurred, XRPD patterns can be compared to known forms (polymorphs, hydrates, salts, free acid/base) in order to identify the solids remaining. If a pattern is obtained that does not correspond to known forms, complementary methods will be needed to determine properties such as hydration state or a change in stoichiometry as would be observed from breaking a salt and forming the free acid/base or the formation of salts in buffered solutions.

FORMULATION

Formulators are charged with the responsibility to formulate a product which is physically and chemically stable, manufacturable, and bioavailable. Most drugs exhibit structural polymorphism, and it is preferable to develop the most thermodynamically stable polymorph of the drug to assure reproducible bioavailability of the product over its shelf life under a variety of real-world storage conditions. There are occasional situations in which the development of a metastable crystalline or amorphous form is justified because a medical benefit is achieved. Such situations include those in which a faster dissolution rate or higher concentration are desired, in order to achieve rapid absorption and efficacy, or to achieve acceptable systemic exposure for a low-solubility drug.

Another such situation is one in which the drug remains amorphous despite extensive efforts to crystallize it. If there is no particular medical benefit, there is less justification for accepting the risks of intentional development of a metastable crystalline or amorphous form. Whether or not there is medical benefit, the risks associated with development of a metastable form must be mitigated by laboratory work which provides assurance that (a) the largest possible form change will have no substantive effect on product quality or bioavailability, and/or (b) a change will not occur under all reasonable real-world storage conditions, and/or (c) analytical methodology and sampling procedures are in place which assure that a problem will be detected before dosage forms which have compromised quality or bioavailability can reach patients.

Crystal engineering and co-crystals

Crystal engineering is generally considered to be the design and growth of crystalline molecular solids with the aim of impacting material properties. A principal tool is the hydrogen bond, which is responsible for the majority of directed intermolecular interactions in molecular solids. Co-crystals are multi-component crystals based on hydrogen bonding interactions without the transfer of hydrogen ions to form salts – this is an important feature, since Brønsted acid-base chemistry is not a requirement for the formation of a co-crystal.

Co-crystallization is a manifestation of directed self-assembly of different components. Co-crystals have been described of various organic substances over the years (33,34) and given various names, such as addition compounds (35,36) molecular complexes (37,38) and heteromolecular co-crystals (39). Regardless of naming convention, the essential meaning is that of a multi-component crystal where no covalent chemical modification of the constituents occurs as a result of the crystal formation. Pharmaceuticals co-crystals have only recently been discussed as useful materials for drug products.  

Pharmaceutical co-crystals

Pharmaceutical co-crystals can be defined as crystalline materials comprised of an active pharmaceutical ingredient (API) and one or more unique co-crystal formers, which are solids at room temperature. Co-crystals can be constructed through several types of interaction, including hydrogen bonding, p-stacking, and van der Waals forces. Solvates and hydrates of the API are not considered to be co-crystals by this definition. However, co-crystals may include one or more solvent/water molecules in the crystal lattice. An example of putative design, a construction and preparation process is shown in Figure 2 for the 5-fluororuracil:urea 1:1 co-crystal(40).

This real example neatly illustrates the opportunity and challenge that exists currently with designing pharmaceutical co-crystals. Firstly, the ‘design’ is challenging because we have no ability to predict the exact crystal structure that may result from a crystallization attempt. By analogy to the challenge of deriving protein structure from first principles, the primary sequence (chemical structure in our case) is known and elements of secondary structure (the 2-D tape construction in Figure 2) are somewhat discernible from primary information. Prediction of the actual 3-D folded conformation (tertiary structure or obtained by self-assembly) is not possible. In other words, while we currently have the ability to project which things associate in what approximate manner on the secondary level, crystal structure prediction is essentially an intractable proposition.

By extension, and just as the exact function of a protein and quantitative parameters of activity are not predictable from primary and secondary structure, the prediction of crystal properties is not possible in the absence of structural information and measurements. There is early evidence that practitioners were aware that apparent co-crystallization of drugs could lead to useful preparations (41). In fact, a ‘chemical compound’ composed of sulfathiazole and proflavin dubbed flavazole was used to treat bacterial infection during the Second World War (42).

The case of flavazole reveals insight into how two different molecules might interact in a putative co-crystal:“… flavazole is definitely a chemical compound containing equimolar proportions of sulphathiazole and proflavin base. It is believed that combination occurs through the acidic sulphonamide group (SO2NH) of the sulphathiazole and the basic centres of the proflavin. Perhaps the most realistic expression of the formula would be to place proflavin and sulphathiazole side by side with a comma between them.” (42)  In the second half of the 20th century, interest in co-crystals evolved into the directed study of intermolecular interactions in crystalline solids (43-45). The technical development of routine single-crystal structure determination led to a watershed of data, now largely accessible through the Cambridge Structural Database (CSD) (46,47).

The structural data have become useful for understanding the intermolecular interactions in co-crystals in atomic level detail (48). Using insight gained from analysis of the CSD and directed experimentation, scientists attempt design of co-crystals with specific properties, such as color or non-linear optical response, by selecting starting components with appropriate molecular properties likely to exhibit specific intermolecular interactions in a crystal (49-52).

However, even when chemically compatible functional groups are present it is not possible to accurately predict if a co-crystal, a eutectic mixture or simply a physical mixture will result from any given experiment. As a result of these complexities, attention has been directed at the identification and characterization of intermolecular packing motifs with the goal of developing principles for co-crystal materials (53).

Figure 2.  Steps involved in crystal engineering of a pharmaceutical phase, exemplified by the real example of co-crystallization of 5-fluorouracil and urea. Scientists in India have reported a rare example of synthon polymorphism in co-crystals of 4,4′-bipyridine and 4-hydroxybenzoic acid.

Graphical abstract: Synthon polymorphism and pseudopolymorphism in co-crystals. The 4,4′-bipyridine–4-hydroxybenzoic acid structural landscape

Polymorphism is defined as the ability of a material to exist in more than one form or crystal structure. It has important implications for the properties of such materials; for example in pharmaceuticals, the dissolution rate of a drug can be dependent on the polymorphic form. While this is a common phenomenon in single crystals it is much less common in co-crystals, systems where the structure has at least two distinct components. Gautam Desiraju from the Indian Institute of Science, found that when 4,4′-bipyridine and 4-hydroxybenzoic acid were dissolved together in a solvent such as methanol they would co-crystallise to form two different polymorphs. They noticed that a third form, a pseudopolymorph, was also present.

PROSPECTS FOR CRYSTAL ENGINEERING AND PHARMACEUTICAL CO-CRYSTALS

At the beginning of the 21st century, the field of crystal engineering has experienced significant development. Importantly, crystal engineering principles are now being actively considered for application to pharmaceuticals to modulate the properties of these valuable materials (54).

Because the physical properties that influence the performance of pharmaceutical solids are reasonably well appreciated, there is a unique opportunity to apply crystal engineering techniques and the appropriate follow-up studies to solve real world problems, such as poor physical and chemical stability or inadequate dissolution for appropriate biopharmaceutical performance of an oral drug. As structures and series of pharmaceutical co-crystals have begun to appear, we again find that properties cannot be predicted from the structures.  Nevertheless, occasional trends have been suggested.

For example, insoluble drug compounds co-crystallized with highly water soluble complements tend to achieve kinetic solubilities in aqueous media several times greater than the pure form (55,56).

There are also more possible phases for each given active compound to consider, thus there will arguably be a greater opportunities for property enhancement. In terms of stability enhancement and solubilization, the example of the series of itraconazole co-crystals with pharmaceutically acceptable 1,4-diacids (55) suggests a strategy alternative to amorphous drug formulation. The co-crystal options presented retain the stability inherent in a crystalline state, while allowing for solubilization that significantly exceeds that of crystalline itraconazole base and rivals the performance of the engineered amorphous bead formulation (Sporanox®).

Where are we now? From recent literature it appears that knowledge gained over the past century and increasingly sophisticated screening techniques developed within the last decade are paving the way towards design of co-crystals with potentially improved pharmaceutical properties (55-58) In terms of the application to pharmaceutical systems, the field of crystal engineering is developing the retro-synthetic understanding of crystal structure using reasoning that is analogous to that applied by organic chemists.  For example, the retro-synthetic approach in covalent synthesis operates on the level of a single molecule, while the analogous effort in crystal engineering focuses on the “supermolecule”:

 piracetam

The assemblies that define the crystalline arrangement of the molecules as they self-organize into the solid-state. The parallels between the development of crystal engineering and synthetic organic chemistry run still deeper. Methodologies for carrying out these crystallizations are being developed alongside the development of new robust motifs (6,53,55,57,60). The importance of the solubility and dissolution relationships of the components of a putative co-crystal is becoming a matter of significant investigation (56,60). The same can be said for the roles of additives in templating novel forms.

Mechanical milling of materials has also been documented as a means to make co-crystals, and a recent example of polymorphic forms of caffeine:glutaric acid illustrates the opportunities of this type of processing to influence crystal form (61). With an increase in the understanding of the modes of self-assembly, one can start to address the design aspect towards making pharmaceutical co-crystals.

There remain several limitations to the application of what is currently known to the design of useful materials. As mentioned earlier, it remains intractable to reliably predict crystal structure.  Multi-component crystals are well out of reach for prediction due in part to complex energetic landscapes, lack of appropriate charge density models and a large number of degrees of freedom, making computation unfeasible. Moreover, there is only a qualitative understanding of the interplay between intermolecular interactions and materials performance, especially for properties relevant to pharmaceuticals such as solubility, dissolution profile, hygroscopicity and melting point.

But the saving grace of the co-crystal approach comes in two guises: Complementarity and diversity. On the topic of complementarity, it is possible, by way of CSD database mining for instance, to identify trends of hetero-synthon occurrence in model systems. As for the diversity aspect, the space of possible co-crystal formers is large, limited only by pharmaceutical acceptability. Coupled with parameters such as stoichiometry variation and increase in the number of components (binary systems can be expanded into ternary ones, etc.), the opportunities appear vast.

THE FUTURE OF CRYSTAL ENGINEERING IN PHARMACEUTICAL SCIENCE

Links

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Novel Challenges in Crystal Engineering: Polymorphs and New 

www.intechopen.com/…/novel-challenges-in-crystal-engineering-polym‎Novel Challenges in Crystal Engineering: Polymorphs and New Crystal Forms of ActivePharmaceutical Ingredients

Where are we going?  At this point, we have only just scratched the surface of materials science-driven pharmaceutical product design. In the 21st century, practitioners of pharmaceutical chemistry need to enumerate and exploit the opportunities of crystal form design that nature affords us, and thus gain increasing ability to design the materials we need from the molecules that we seek to convert into pharmaceuticals.

Learning will be facilitated by advances in crystallization automation (6,62), microscopy-spectroscopy techniques (Raman and IR microscopy) and new techniques such as terahertz spectroscopy and AFM, along with increasingly sophisticated X-ray diffraction lab instrumentation. In addition, further enhancements in the data mining tools associated with the CSD operating on an ever increasing number of high-quality crystal structures will undoubtedly lead to new knowledge and principles of interaction. 

The challenge placed before pharmaceutical scientists, now and in the future, is the following: (i) to understand the requirement of a particular compound in terms of materials structure and properties, and (ii) to creatively integrate crystal engineering within the limits of pharmaceutical acceptability of components to obtain new forms of active ingredients with desirable properties for formulation and delivery. It should become the collective mantra of medicinal chemists, process engineers and pharmaceutical scientists to “design and make the material we need.” This mantra can form the common aspiration for an industry that is in significant need of innovation and productivity enhancement.

Applications and Advantages

Applications

  • Drug companies can use this technology to protect themselves against others generating and patenting polymorphs

Advantages

  • Having more than one solid form of a drug allows optimization of drug dissolution behavior and shelf life

IP AND POLYMORPHS

In order for a new drug to enter the market, pharmaceutical companies must invest for many years in very expensive clinical trials and a lengthy regulatory approval process.Market protection plays therefore a major role in the growth of the pharmaceutical industry and Intellectual Property (IP) laws are intended to give the investors an opportunity to recover their costs. Patent filing is one way of efficiently protecting various aspects of an innovative drug.
The duration of the new drug’s market protection is, however, limited in time and once the original drug is no longer protected, legal copies (generic medicines) can be developed and marketed by competitors at more accessible prices, since the expensive basic research, as well as pre-clinical and clinical trials (at least for small molecules) are no longer necessary. Generic medicines are either identical copies of the original drug or so-called bioequivalent versions of it.
Bioequivalent means that they behave as the original drug when administered to patients. For a generic drug to be a bioequivalent its Active Pharmaceutical Ingredient (API) does not need to be the same solid form as in the original drug. A different polymorph or a pseudo-polymorph (i.e. solvate, hydrate) of the API and different excipients are acceptable variants, as long as the final generic drug product behaves as the original one.
Solid Forms Screening
Screening of solid forms, in particular polymorphs of APIs, is therefore an essential part of pharmaceutical development and lifecycle management, not only for scientific and regulatory reasons, but also because of the key role that pharmaceutical solid forms play in the area of IP, for innovators as well as for generic companies. The knowledge generated by conducting solid form screening, in fact, can provide an innovator company the opportunity to build a strong patent portfolio around different solid forms and therefore a way to maximize returns from drug development.
This allows innovator companies to gain several years of additional protection for their product after the expiry of the basic molecule patent, since various pharmaceutical solid forms are individually patentable. In the US, for instance, innovator companies are required to identify, in the so-calledOrange Book, their patents covering different solid forms performing the same as the product described in the corresponding NDA. In return, they can benefit from a 30-months stay over a generic company which would eventually file an ANDA with aParagraph IV Certification for any of these listed patents.
Thus, by patenting a maximum number of possible solid forms, even if these are not further developed and used, innovator companies can more efficiently protect their own products. Such patents must obviously meet the same patentability criteria as other inventions. Conversely, a generic company can launch its own product if, after the basic molecule patent has expired, it discovers a new solid form, i.e. a form with no IP protection and suitable characteristics for product development.
In both cases, a very sensitive tool as SR-XRPD can play a key role in helping the detection and characterization of a maximum number of polymorphs.
 Accurate and direct characterization of the API polymorphic forms and detection of trace amounts has proven to be of paramount importance (e.g. Paxil®, Cefdinir) whereas poorly conducted screens and unsuccessful patenting strategies, on the other hand, can have significant negative commercial consequences (e.g. Ritonavir).
Interestingly, in the US the first ANDA approved by FDA with paragraph IV certification is entitled to 180-days marketing exclusivity. Initially granted only when theANDA applicant having filed Paragraph IV Certification could prevail in the litigation with the originator, the new FDA guidance suppresses the “successul defence”requirement and the 180-days exclusivity is decided on a case-by-case basis and can therefore be granted even if the case is settled.
While there has been much discussion by policymakers and stakeholders about the effects of “secondary patents” on the pharmaceutical industry, there is no empirical evidence on their prevalence or determinants. Characterizing the landscape of secondary patents is important in light of recent court decisions in the U.S. that may make them more difficult to obtain, and for developing countries considering restrictions on secondary patents.
It is seen the claims of the 1304 Orange Book listed patents on all new molecular entities approved in the U.S. between 1988 and 2005, and coded the patents as including chemical compound claims (claims covering the active molecule itself) and/or one of several types of secondary claims. It is seen that  distinguish between patents with any secondary claims, and those with only secondary claims and no chemical compound claims (“independent” secondary patents).
It is seen  that secondary claims are common in the pharmaceutical industry. It is seen that independent secondary patents tend to be filed and issued later than chemical compound patents, and are also more likely to be filed after the drug is approved. When present, independent formulation patents add an average of 6.5 years of patent life (95% C.I.: 5.9 to 7.3 years), independent method of use patents add 7.4 years (95% C.I.: 6.4 to 8.4 years), and independent patents on polymorphs, isomers, prodrug, ester, and/or salt claims add 6.3 years (95% C.I.: 5.3 to 7.3 years). evidence that late-filed independent secondary patents are more common for higher sales drugs
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Polymorph quantification. REF 79
SEE A SLIDESHARE PRESENTATION
The ability to detect and quantify polymorphism of pharmaceuticals is critically important in ensuring that the formulated product delivers the desired therapeutic properties because different polymorphic forms of a drug exhibit different solubilities, stabilities and bioavailabilities. The purpose of this study is to develop an effective method for quantitative analysis of a small amount of one polymorph within a binary polymorphic mixture. Sulfamerazine (SMZ), an antibacterial drug, was chosen as the model compound. The effectiveness and accuracy of powder X-ray diffraction (PXRD), Raman microscopy and differential scanning calorimetry (DSC) for the quantification of SMZ polymorphs were studied and compared.
Low heating rate in DSC allowed complete transformation from Form I to Form II to take place, resulting in a highly linear calibration curve. Our results showed that DSC and PXRD are capable in providing accurate measurement of polymorphic content in the SMZ binary mixtures while Raman is the least accurate technique for the system studied.
DSC provides a rapid and accurate method for offline quantification of SMZ polymorphs, and PXRD provides a non-destructive, non-contact analysis.A novel method of detecting very low levels of different polymorphs using high-resolution X-ray powder diffraction with a synchrotron light source has been developed by Zach-Zambon Chemicals of Italy. Key to the project has been development of software to enable appropriate data presentation.The issue of polymorphism in pharmaceuticals has attracted increasing attention over the past 20 years and is something to which development scientists and the regulatory authorities pay considerable attention.
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REFERENCES

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63……..POLYMORPHISM AND PATENTS http://www.collegio.unibo.it/uploads/ideas/joelbernstein.pdf 64…Aprepitant case study FTIR.. READING MATERIALhttp://alpha.chem.umb.edu/chemistry/ch361/spring%2005/ftir%20polymorph.pdf 65…..READ………….An Overview of Solid Form Screening During Drug Development, http://www.icdd.com/ppxrd/10/presentations/PPXRD-10_Ann_Newman.pdf 66…..CRYSTALLIZATION..http://www.intechopen.com/books/advanced-topics-on-crystal-growth/crystallization-from-the-conformer-to-the-crystal

67International Conference on Harmonization Q6A Guideline: Specifications for New Drug Substances and Products: Chemical Substances, October 1999.

68Center for Drug Evaluation and Research Guidance: Submitting Supporting Documentation in Drug Applications for the Manufacture of Drug Substances, February 1987.

69S. Byrn, R. Pfeiffer, M. Ganey, C. Hoiberg, and G. Poochikian. Pharmaceutical solids: A strategic approach to regulatory considerations. Pharm. Res. 12:945-954 (1995). 70

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71 CRYSTALS POLYMORPHS IN PHARMAhttp://www.fcfar.unesp.br/arquivos/475753.pdf

72 API………….POLYMORPHISM pharmaceutical ingredients (APIs).http://www.ncbi.nlm.nih.gov/pubmed/19275600

73 polymorphs and co-crystals – ICDD  POWER POINT PRESENTATION

74Thermodynamic stability and transformation of pharmaceutical  http://pac.iupac.org/publications/pac/pdf/2005/pdf/7703×0581.pdf

75http://www.imc.cas.cz/nmr/projekt/ws/springer.pdf

76  High-throughput crystallization: polymorphs, salts, co-crystalsand solvates of pharmaceutical solidshttp://citeseerx.ist.psu.edu/viewdoc/download?doi=10.1.1.85.5397&rep=rep1&type=pdf

77 Crystalline Solid – University of Utah College of Pharmacy Homepharmacy.utah.edu/pharmaceutics/pdf/Crystalline.pdf‎Form – a term encompassing all solids – polymorphs, solvates, amorphous  inPolymorphism in Pharmaceutical Solids

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  8. Campbell Roberts, S.N., Williams A.C., Grimsey, I.M., and Booth S.W., Quantitative analysis of mannitol polymorphs. X-ray powder diffractometry—exploring preferred orientation effects J. Pharm. Biomed. Anal., 2002, 28, 1149-1159.

COMPILED BY…..

ANTHONY MELVIN CRASTO

DR ANTHONY MELVIN CRASTO Ph.D

amcrasto@gmail.com

MOBILE-+91 9323115463
GLENMARK SCIENTIST ,  INDIA
web link
http://anthonycrasto.jimdo.com/

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