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DR ANTHONY MELVIN CRASTO, WORLDDRUGTRACKER

Worldwide Hepatitis C Market: CV Drugs Clinical Trials, Hepatitis C Pipeline Drugs Sales & Forecast 2018

 Uncategorized  Comments Off on Worldwide Hepatitis C Market: CV Drugs Clinical Trials, Hepatitis C Pipeline Drugs Sales & Forecast 2018
Jun 192014
 
WhaTech Channel: Reports Industrial
Published: Wednesday, 18 June 2014 20:34
Submitted by Market Research WhaTech Premium
News from: RnR Market Research

Hepatitis C market by 2018 is expected to grow more than 3 times from its current market size of 2012. Hepatitis C virus (HCV) infection is a complex public health problem, characterized by a high prevalence of chronic infection, an increasing burden of HCV-associated disease, low rates of testing, treatment and the prospect of increasing incidence associated with the epidemic of injection drug use.

http://www.whatech.com/members-news/reports-industrial/22195-worldwide-hepatitis-c-market-cv-drugs-clinical-trials-hepatitis-c-pipeline-drugs-sales-forecast-2018

Hepatitis C Market Overview

Hepatitis C is a leading cause of chronic liver disease, end-stage cirrhosis and liver cancer. Because of the slow progression and asymptomatic character of the infection, many people are unaware of having it. As a consequence, the infection is often diagnosed at a late stage when treatment options are limited. As no effective vaccine against the Hepatitis C virus (HCV) has been discovered so far the market is driven by therapeutics. The increase in the prevalence of the disease and the availability of new first-in-class therapies with better safety and efficacy profiles are expected to drive the growth of the HCV market. The growth in HCV drugs market is primarily attributed to high unmet need in the market which is expected to be fulfilled by strong pipeline candidates. Low levels of awareness and knowledge about HCV have been identified as a formidable challenge to prevention and care.

Complete report is available @ http://www.rnrmarketresearch.com/hepatitis-c-market-forecast-hcv-drugs-clinical-trials-hepatitis-c-pipeline-drugs-sales-forecast-worldwide-market-report.html .

Renub Research study titled “Hepatitis C Market & Forecast, HCV Drugs Clinical Trials, Hepatitis C Pipeline Drugs Sales & Forecast – Worldwide” provides a comprehensive assessment of the fast-evolving, high-growth of Hepatitis sector. This 164 page report with 25 Figures and 2 Tables studies the Hepatitis C Drug Market Landscape. This report contains 7 chapters.

  • Hepatitis C Drugs Market & Forecast (Chapter 2)
  • Hepatitis C Approved Drugs Sales & Forecast (Chapter 3)
  • Hepatitis C Deals & Acquisitions (Chapter 4)
  • Hepatitis C – Pipeline Drugs Clinical Trials (Drugs in Phase III) (Chapter 5)
  • Hepatitis C – Pipeline Drugs Clinical Trials (Drugs in Phase II) (Chapter 6)
  • Hepatitis C – Pipeline Drugs Sales Forecast (Chapter 7)

Hepatitis C – Approved Drugs sales & Forecast Analysis (To 2016) (Chapter No. 3)

  1. Pegasys
  2. Pegintron
  3. Incivek
  4. Victrelis

Hepatitis C – Pipeline Drugs Clinical Trials (Drugs in Phase III) (Chapter No. 5)

  • Simeprevir (TMC 435) (Company: Janssen Pharmaceutical)
  • Faldaprevir (BI 201335) (Company: Boerhinger Ingelheim)
  • Asunaprevir (BMS-650032) (Company: Bristol-Myers Squibb)
  • PEG-Interferon Lambda (Company: Bristol-Myers Squibb)
  • Sofosbuvir (PSI-7977 or GS-7977) (Company: Gilead Sciences)
  • Daclatasvir (BMS-790052) (Company: Bristol-Myers Squibb)
  • BI-207127 (Company: Boerhinger Ingelheim)
  • ABT-450/r (Ritonavir) (Company: Abbott Laboratories)
  • ABT-267 (Company: Abbott Laboratories)
  • ABT-072/333 (Company: Abbott Laboratories)
  • Alisporivir (Company: Novartis)

Purchase a copy of this report @ http://www.rnrmarketresearch.com/contacts/purchase?rname=186104 .

Hepatitis C – Pipeline Drugs Clinical Trials (Drugs in Phase II) (Chapter No. 6)

  • Mericitabine (RG-7128) (Company: Roche)
  • Danoprevir/r (Ritonavir) (RG7227) (Company: Roche)
  • GS-9256 (Company: Gilead Sciences)
  • GS-9451 (Company: Gilead Sciences)
  • MK-5172 (Company: Merck)
  • Sovaprevir (ACH-1625) (Company: Achillion)
  • IDX-320 (Company: Idenix)
  • MK-8742 (Company: Merck)
  • ACH-3102 (Company: Achillion Pharmaceuticals, Inc)
  • IDX-719 (Company: Idenix)
  • PPI-668 (Company: Presidio Pharmaceuticals)
  • Setrobuvir (ANA-598) (Company: Roche)
  • VX-222 (Company: Vertex Pharmaceuticals)
  • GS-9669 (Company: Gilead Sciences)
  • GS-9190 (Tegobuvir) (Company: Gilead Sciences)
  • BMS-791325 (Company: Bristol-Myers Squibb)

Hepatitis C – Pipeline Drugs Sales Forecast (Chapter 7)

  • Simeprevir (TMC 435)
  • Faldaprevir (BI 201335) (Boerhinger Ingelheim)
  • Asunaprevir (BMS-650032)
  • Sofosbuvir (PSI-7977 or GS-7977)
  • Daclatasvir (BMS-790052)
  • ABT-450/r (Ritonavir)
  • ABT-072/333
  • Alisporivir
  • Mericitabine (RG-7128)
  • Danoprevir (RG7227)
  • GS-9256
  • Setrobuvir (ANA-598)
  • VX-222
  • GS-9190 (Tegobuvir)
  • BMS-791325

Data Sources

This report is built using data and information sourced from proprietary databases, primary and secondary research and in-house analysis by Renub Research team of industry experts.

Primary sources include industry surveys and telephone interviews with industry experts.

Secondary sources information and data has been collected from various printable and non-printable sources like search engines, News websites, Government Websites, Trade Journals, White papers, Government Agencies, Magazines, Newspapers, Trade associations, Books, Industry Portals, Industry Associations and access to more than 500 paid databases.

News From

RnR Market Research
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AmVac begins Phase III trial of Gynevac vaccine for bacterial vaginosis

 Phase 3 drug, Uncategorized, VACCINE  Comments Off on AmVac begins Phase III trial of Gynevac vaccine for bacterial vaginosis
Jun 192014
 
AmVac begins Phase III trial of Gynevac vaccine for bacterial vaginosis
AmVac has commenced a Phase III study of its Gynevac to assess the safety and efficacy of the vaccine in bacterial vaginosis (BV) treatment.

AmVac has commenced a Phase III study of its Gynevac to assess the safety and efficacy of the vaccine in bacterial vaginosis (BV) treatment.

Image

Manufactured in accordance with the current GMP standards, the therapeutic vaccine is based on a blend of inactivated lactobacilli strains.

http://www.marketwatch.com/story/amvac-initiates-phase-iii-trial-with-its-lead-vaccine-gynevac-for-the-treatment-of-bacterial-vaginosis-2014-06-17

 

Love, cast in stone: Temples in India depicting erotic art

India is dotted with many glorious temples, but erotica on the walls of some arouses curiosity and even puzzles tourists. There are various theories about the reason for such vivid depiction of erotica–mass sex education, warding off natural calamities and the devdasi system. Due to the presence of 64 Yogini temples near Khajuraho, Padawali, Konarak/Lingaraj etc., scholars also attribute the erotic art to Tantric practices, which revolve around the ultimate union of the male and the female energy and forms referred to as Maithuna. Whatever the reason be, the brazenness or ethereal beauty of temple erotica will never cease to amaze us.

Khajuraho, Madhya Pradesh

Built by the Chandela Kings who were greatly influenced by Tantric traditions, this temple is said to represent the ultimate seductress.

While the fine sandstone statues built earlier have a well rounded finish, the ones made later are more angular. In his history of the Kamasutra, Mc Connachie describes the amorous sculptures as “the apogee of erotic art”, where the twisting, broad hipped and high breasted nymphs, fleshy apsaras and extravagantly interlocked maithunas run riot along the surface of stone.

The various scenes of passionate love making, in acrobatic postures that sometimes border on the physically impossible, strike viewers. Look out for the bold panels of multiple partners engaged with each other. For an interesting perspective on Khajuraho, watch the Sound and Light show. The best time to visit is during the Khajuraho Dance Festival in the first week of February.

Markandeshwar Temple, Maharashtra

Near the naxal district of Gadchiroli, the Markandeshwar temple complex, by the River Wainganga, showcases a sprinkling of erotic art. A couple performing ‘fellacio’ will raise eyebrows. Know to be built by danavas (evil forces) in one night, the temple is made from stone, and follows Hemadpanth architecture. The annual fair during Mahashivratri attracts devotees from far and wide every year. Hiring a car from Nagpur is recommended, unless you fancy hitch-hiking with villagers past moonlit fields or changing several buses and autos. If you’re stranded, look for the dharamshala near the temple.

Padawali Temple,  Madhya Pradesh

In Morena district near the Chambal Valley, once notorious for dacoits, lies the fortress of Padawali. Two stalwart lion statues greet you at its entrance. The temple inside has earned the reputation being a ‘Mini Khajuraho’ due to the prevalence of erotic art. The difference between big brother Khajuraho and Padawali Temple, is that the erotic art here seems less acrobatic and more ‘real life’ and ‘doable’. The carvings of maithunas in various positions, ranging from simple to difficult almost brings the Kamasutra to life.

Ranakpur Jain Temples, Rajasthan

This marble temple of superlative beauty is a ‘vision in white’ with its domes, shikharas and turrets. Over 1,444 intricately carved marble pillars hold up the temple and a monolithic marble rock depicting over 100 snakes catches the eye. Look out for a panel depicting several experimental love making scenes, in a line with a central queen-like figure seated on a throne, with an amorous midget on her lap. It’s interesting to note that not only Hindus, but even Jains decorated temples with erotic art. It hints at how nudity had a religious connect due to the ‘Digambara’ ideology or the Tantric cult.

Sun Temple,  Orissa 

When I first visited the Sun Temple at Konarak in Orissa, as a giggly 16-year-old , I was  taken aback by how the panels revealed way more about the ‘birds and bees’ than our biology classes had taught us. My second visit recently, helped me appreciate the beautiful erotic art better. The brazenness of the sculptures here gives Khajuraho stiff competition; one of the most scandalous panels is of a dog licking a woman’s genital area. I overheard a guide say, “this was considered a cure for sex related infections, as the dog’s saliva has antibiotic properties.” Scenes of polygamy, polyandry and lesbian love are blissfully abundant.

An architectural genius, this temple shows the Sun God on a colossal chariot drawn by seven horses. The word Konarak is a combination of Kona (corner) and Arka (Sun).  The temple was previously located closer to the sea, but the magnetic properties of its stone caused shipwrecks. This, along with the dark colour of its stones, earned it the tile of ‘The Black Pagoda’. An interesting study in contrast is the famous Jagannath Temple at Puri, also referred to as ‘The White Pagoda’ due to its whitewashed walls. If you are an art enthusiast you must visit the Konarak Archaeological Museum nearby that contains fallen sculptures from the temple.

Sun Temple, Gujarat

It is believed to be the place where Lord Rama conducted a yagna here to purify himself of the sin of killing a Brahmana-Ravana. Like Konarak, its architecture is such that the temple catches the first rays of the rising sun. The most striking feature of the temple is a perfectly designed Kama Kunda (water tank) meant for ablutions and for a reflection of the temple in the water. It has lateral stone steps leading down to the tank, allowing both direct and diagonal descent from all sides. Carvings of men and women in various acts of sex with small midget like creatures are prominent. However, due to erosion the detailing of the stone carvings is blurred in places.

Osian, Rajasthan

Amidst the sand dunes of Thar, Osian has a cluster of Hindu and Jain temples dating back to the 11 century AD. The Sachiya Mata temple dedicated to the resident Goddess has a gorgeous carved archway leading up to the shrine and has some beautiful depiction of erotic love locked couples, complete with details like the bed on which the couples lie.

Virupaksha Temple, Karnataka
On the banks of the Tungabhadra River, this temple with beautiful pillars and towered gateways dedicated to Lord Shiva in his avatar as Virupaksha. It is one of the oldest functioning temples since the 7th century AD. A  panel  that catches the eyes depicts a nude woman being ‘admired’ by men and women around her. It is best to visit the temple, during the Hampi festival in November. While in the area, also check out the erotic art on the pillars of the Achyutaraya temple.

Several other temples in South India like Belur, Halebidu, Somanathapura and Nugguhalli, the Badami and Banashankari temples of the Chalukya times and the Vijayanagar temples of Bhatkal and Lepakshi also have a profusion of erotic art. The Meenakshi temple of Madurai and Veeraranarayan temple of Gadag have erotic sculptures on their Gopuram. (Information about other temples with erotic art in South India taken from www.kamat.com)

No one has summed up the beauty of erotica on temple walls better than Tagore while he was referring to Konarak, ‘The language of man here is defeated by the language of stone.’

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Mesocrystals as a class of multifunctional materials

 Uncategorized  Comments Off on Mesocrystals as a class of multifunctional materials
Jun 192014
 

Graphical abstract: Mesocrystals as a class of multifunctional materials

 

Mesocrystals that consist of crystallographically aligned individual building blocks and controlled level of porosity in between exhibit unique structures and multifunctional behavior. A large number of mesocrystals have been successfully developed by different growth technologies, and various growth mechanisms are discussed. In addition to various self-assembly and growth techniques, considerable attention has been paid to the formation mechanisms where the crystalline colloidal nanoparticles are assembled into mesocrystals via interparticle forces or physical fields. Owing to their high surface area, controllable level of porosity, crystallinity of subunits, oriented subunit alignment, and elegant 3D network structure, the performance of mesocrystals may be superior to their nanocrystalline, single-crystal, and polycrystalline counterparts. There has been a surge in the number of applications demonstrated for mesocrystals over the past couple of years, showing their great application potential.

 

Mesocrystals as a class of multifunctional materials

Yanqiong Liu,a   Yu Zhanga and   John Wang*a
*Corresponding authors
aDepartment of Materials Science and Engineering, Faculty of Engineering, National University of Singapore, Singapore 117574
E-mail: msewangj@nus.edu.sg;
Fax: +65 6776 3604 ;
Tel: +65 6516 1268
CrystEngComm, 2014,16, 5948-5967

DOI: 10.1039/C4CE00256C

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The crystal structure and optical properties of a pharmaceutical co-crystal – the case of the melamine–barbital addition compound

 Uncategorized  Comments Off on The crystal structure and optical properties of a pharmaceutical co-crystal – the case of the melamine–barbital addition compound
Jun 162014
 

 

Graphical abstract: The crystal structure and optical properties of a pharmaceutical co-crystal – the case of the melamine–barbital addition compound

 

The crystal structure and optical properties of a pharmaceutical co-crystal – the case of the melamine–barbital addition compound

M. Gryl, T. Seidler, K. Stadnicka, I. Matulková, I. Němec, N. Tesařová and P. Němec

CrystEngComm, 2014, 16, 5765 DOI:10.1039/C4CE00178H

The melamine barbital co-crystal is a product of crystal engineering of non-linear optical materials composed of pharmaceutically active ingredients. The resulting crystal phase shows a non-linear effect higher than that of KDP. The material was characterized by means of X-ray diffraction and optical property measurements and calculations.

Graphical abstract: The crystal structure and optical properties of a pharmaceutical co-crystal – the case of the melamine–barbital addition compound

http://pubs.rsc.org/en/Content/ArticleLanding/2014/CE/C4CE00178H?utm_medium=email&utm_campaign=pub-CE-vol-16-issue-26&utm_source=toc-alert#!divAbstract

The crystal structure and optical properties of a pharmaceutical co-crystal – the case of the melamine–barbital addition compound

*Corresponding authors
aDepartment of Crystal Chemistry and Crystal Physics, Faculty of Chemistry, Jagiellonian University, Ingardena 3, 30-060 Kraków, Poland 
bDepartment of Inorganic Chemistry, Faculty of Science, Charles University in Prague, Hlavova 2030, 128 40 Prague 2, Czech Republic
cDepartment of Chemical Physics and Optics, Faculty of Mathematics and Physics, Charles University in Prague, Ke Karlovu 3, 121 16 Prague 2, Czech Republic
CrystEngComm, 2014,16, 5765-5768

DOI: 10.1039/C4CE00178H

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Large Scale Production Of MAbs

 MONOCLONAL ANTIBODIES  Comments Off on Large Scale Production Of MAbs
Jun 132014
 

Production of MAb

Fig.1 Production of MAb

Large Scale Production Of MAbs:

Commercially, on large scale, MAbs are produced by two methods.

(a) Ascites production in mice

(b) In-vitro fermentation

The production method is summarized in Fig.no.2a & 2b.

a) Ascites Production In Mice:

The first monoclonal antibodies approved by FDA for therapeutic use OKTS, is produced by ascitic technology19.

In this method hybridoma cells are injected into peritoneal cavity of histocompatible mice. The mice are pretreated by i.p. injection of Pristane to irritate the peritoneal cavity which facilitates the growth of ascitic tumor. The fluid produced may contain the high concentration of secreted MAbs, 2 to 20 μg / ml and 2 to 6 ml or more can be harvested per mouse. Comparison of different MAb production22,23 methods is shown inTable 1.

Drawbacks of this method are:

1. It is very costly, very difficult and not reliable.

2. Product may get contaminated with mouse immunoglobulins and also with other mouse proteins.

3. Viruses can be introduced as contaminants.

4. Antibody yield is often less as compared to other methods.

b) In-Vitro Fermentation:

In this method, the cells are grown and gradually moved to larger and larger culture ensuring exponential growth. Typical antibody levels in the culture supernatant ranges from 5-50 μg/ml depending on the individual clone and on cell density. When more production of antibody is required 1-litre cultures in roller bottles are used. Required cells are removed from rest of media by centrifugation or filtration, generally followed by ultra filtration step for concentrating the filtrate by up to 20 folds.

Advantages of this method are:

(1) As serum required in culture media is reduced, it is cost effective.

(2) There will not be any contamination with mouse immunoglobulin.

But the major drawback is that of contamination of final product with serum or protein based growth factors.

Table 1: Comparison of different MAb production methods.

Production system

Scale

Volume (ml)

Concentration (mg/ml)

Production time (weeks)

Quality

Ascites (in vivo)

20-250 mg

5-10

< 20

2-3

Low
Stir growth

100-2500

0.01-0.1

2-3

High
Dialysis membrane

< 50 mg

10-25

0.1-1.5

2-5

High
Roller bottles

< 2 gm

100-2000

0.01-0.2

2-6

High
Hollow fiber

0.15-30 gm

25-1000

0.2-0.3

3-12

High
Fermentor

2-100 gm

< 2000 lit

0.05-0.5

2-12

High

 MAb Production

Fig. 2a:  MAb Production (Flowchart)

 Freeze Dried MAb Production

Fig. 2b:  Freeze Dried MAb Production (Flowchart)

i) Purification:

Contamination, during production process, such as protein, nucleic acid, endotoxins, immunoglobulin and adventitious agent can be removed by purification method. The purification methods such as precipitation with ammonium sulphate, zone electrophoresis, ion exchange chromatography, hydrophobic interaction chromatography, gel filtration and affinity chromatography are used19.

· Affinity chromatography is often used for initial purification.

· Ion exchange chromatography is used for removing endotoxins and DNA.

· Gel filtration chromatography can remove both high and low molecular form of monoclonal antibodies and it is usually used as the final polishing step.

j) Characterization:

The final determination of monoclonality requires biochemical and biophysical characterization of the immunoglobulin. It is also characterized immunochemically to define its affinity for antigen, its immunoglobulin subclass, the epitopes for which it is specific and the effective number of binding site that it possesses19.

k) Final Processing:

Depending upon the intended application, the antibody may be conjugated to specific radionuclide or toxin. Then the stabilizing agent is added, and the product is filled into final container under inert gas or other specialized conditions.  Lyophillization is frequently applied to get freeze dried product.

Antigenicity Of Murine MAb:

The main problem for mouse MAb is that, human body recognizes it as a foreign agent and produces antibodies against such mouse MAb. The induced human anti-mouse antibodies (HAMA) quickly reduce the effectiveness of mouse MAb and also their interaction may lead to allergic reactions.

To overcome the problem, Human MAbs can be used. Though difficult, this is possible by fusion of EBV (Epstein Barr Virus) transformed human B-lymphocyte with appropriate fusion partners21. EBV is a lymphotrophic DNA herpes virus which is capable of converting normal B-lymphocytes of human and/or mouse into cancer cell having proliferating capacity in vitro. But the presence of EBV as contaminant can pose a problem of producing cancer24.

Even the human-human hybridomas producing MAbs have been produced 25,26. Olsson and Kaplan in the year 1980 produced first human-human myeloma (SKO-007), against the hapten 2, 4-dinitrophenyl (DNP) 19.

The routine production of human MAbs is prevented due to following reason:-

  • Sources of antibody producing cells27.
  • Reliable methods for lymphocytes immortalization.
  • Stability28 and antibody producing capacity.
  • Administration of some antigens to humans could endanger their health29.
  • Recovery of B-lymphocytes from the spleen of human is impracticable.
  • The fusion of human lymphocytes with human lymphoblastoid cell lines is a very inefficient process.
  • Low production yield of human monoclonal antibody.

Hence, other alternatives methods come forth.

Advantages Of MAbs:

  • Pure one molecular species with high specificity for a particular antigenic target.
  • Anti-serum titer values are high.
  • Antibodies with high avaidity can be produced.
  • In vitro and in vivo production is possible.
  • Radiolabelling and fluorescent conjugation of monoclonal antibody are easy.

Disadvantages Of MAbs:

  • Initial cost involved in the technique is high. However, continuous production is somewhat economical.
  • Methods are time consuming.
  • Antigenicity of Murine MAb.
  • MAbs have comparatively less complement fixing ability than that of convectional antiserum.
  • MAbs are highly selective for a particular single antigenic determinant. This renders them incapable of distinguish between different molecules, cells bearing the chemical structure or determinants except one against which it is targeted.
  • The high antibody avidity (energy of binding to an antigen) of MAbs is advantageous for immunoassay but some property is undesirable for purification process.
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A new easy way to “clean” pharma ingredients; study

 Uncategorized  Comments Off on A new easy way to “clean” pharma ingredients; study
Jun 122014
 

 

A new easy way to “clean” pharma ingredients; study

By Natalie Morrison, 28-Jun-2012

Scientists have uncovered a new simple way to “clean” genotoxic impurities (GTIs) in drug ingredients by mixing the solution with contamination-eating scavengers.

http://www.in-pharmatechnologist.com/Ingredients/A-new-easy-way-to-clean-pharma-ingredients-study

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Exploratory Study on Active Pharmaceutical Ingredient Manufacturing for Essential Medicines

 drugs  Comments Off on Exploratory Study on Active Pharmaceutical Ingredient Manufacturing for Essential Medicines
Jun 122014
 

Exploratory Study on Active Pharmaceutical Ingredient Manufacturing for Essential Medicines

http://www.unido.org/fileadmin/user_media/Services/PSD/BEP/APIExploratoryStudy.pdf

Active Pharmaceutical Ingredients (API) of good quality are core to the
manufacturing of effective and safe essential drugs. The price of APIs is the main cost
driver for manufacturing. Only a limited number of large manufacturers of finished
pharmaceutical products have their own API manufacturing capabilities, and none of
them can make all required APIs in-house. The majority of manufacturers, including all
those located in Sub-Saharan Africa (with the exception of one company in South Africa)
have to buy all APIs in the open market.
The paper tries to make the structures of the
API market more transparent, trying to determine how difficult it is for small
manufacturers in developing countries to navigate the global API market and ensure that
they get a quality product at a fair price. It also looks into the competitiveness of the
market, trying to assess the risk that manufacturers or traders monopolize parts of the API
market for essential medicines with low commercial attractiveness. The author confirms
the initial assumption that the API market provides a challenge in particular to small
manufacturers, who have limited means to verify the quality of the APIs they are buying.
One potential way to address this problem would be to broaden the WHO
Prequalification system to include APIs for drugs that are on the WHO Model List for
Essential Medicines.
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Simple new way to clean traces of impurities from drug ingredients

 drugs  Comments Off on Simple new way to clean traces of impurities from drug ingredients
Jun 122014
 

 

Scientists are reporting development of a simple new procedure for removing almost 98 percent of an important impurity that can contaminate prescription drugs and potentially increase the risk for adverse health effects in patients.

Their report appears in ACS’ journal Organic Process Research & Development.

Ecevit Yilmaz and colleagues note that contamination of medications with so-called “genotoxic” impurities (GTIs) have resulted in several major recent drug recalls. GTIs may be ingredients used to make drugs, or they may be formed during production of drugs, and can remain in the final product in minute amounts. The presence of one GTI in the anti-viral medication Viracept distributed in the European Union forced a recall in 2007. With GTIs an ongoing serious concern for the pharmaceutical industry, the scientists sought a better way to remove an important GTI called acrolein.

read at

http://www.sciencedaily.com/releases/2012/06/120620113336.htm

 

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Continuous Processing in the Manufacture of Active Pharmaceutical Ingredients and Finished Dosage Forms: An Industry Perspective

 drugs, Uncategorized  Comments Off on Continuous Processing in the Manufacture of Active Pharmaceutical Ingredients and Finished Dosage Forms: An Industry Perspective
Jun 122014
 

Abstract Image

Continuous Processing in the Manufacture of Active Pharmaceutical Ingredients and Finished Dosage Forms: An Industry Perspective

http://pubs.acs.org/doi/full/10.1021/op300159y

DSM Innovative Synthesis B.V., P.O. Box 18, 6160 MD Geleen, The Netherlands
ACS Green Chemistry Institute, 1155 Sixteenth Street, NW, Washington, DC 20036, United States
§ AstraZeneca R&D Södertälje, S-151 85 Södertälje, Sweden
Org. Process Res. Dev., 2012, 16 (10), pp 1586–1590
DOI: 10.1021/op300159y
Continuous manufacturing as a way of producing fine chemicals, active pharmaceutical ingredients, and finished dosage forms is gaining widespread attention. Although potential benefits over traditional batch-wise production have been discussed at many occasions and appear evident, continuous processes are only slowly being implemented. The American Chemical Society Green Chemistry Institute Pharmaceutical Roundtable has defined “continuous processing” as one of its research priorities(1) and performed a survey of its members’ opinions, the status of implementation, and perceived hurdles blocking implementation of continuous manufacturing processes. Here we discuss the most important results of this survey and their relation to present trends in this industry to “go green”.
UPDATED FROM OTHER SOURCES

Traditional drug manufacturing is a time-consuming process. Active pharmaceutical ingredients are synthesized in a chemical manufacturing plant and then shipped to another site, where they are converted into giant batches of pills. Including transport time between manufacturing plants, each batch can take weeks or months to produce.

Five years ago, MIT and pharmaceutical company Novartis launched a research effort to transform those procedures. Instead of manufacturing drugs using this conventional batch-based system, they envision a continuous manufacturing process, all done in one location, which would cut down on time and cost.

Novartis machine
Researchers at the Novartis-MIT Center for Continuous Manufacturing built this drug-manufacturing prototype in an MIT chemical engineering lab. The system, which consists of six connected units, can transform raw ingredients into finished drug tablets.
Photo: Dominick Reuter

Such a system would allow greater flexibility in supply and could reduce the environmental impact of manufacturing. Continuous manufacturing could also improve quality-assurance testing, says Bernhardt Trout, director of the Novartis-MIT Center for Continuous Manufacturing.

“We see the future of pharmaceutical manufacturing as continuous,” says Trout, who is also a professor of chemical engineering at MIT. “That includes continuous flow together with a systems approach, integration and advanced control.”

Trout and other MIT researchers have now developed and demonstrated a prototype continuous-manufacturing system — the first that can transform raw materials into tablets in a nonstop process. The research team described the new prototype at last October’s annual meeting of the American Institute of Chemical Engineers.

Going with the flow

The original grant supporting the MIT-Novartis Center for Continuous Manufacturing was $40 million over the first five years, with the possibility of renewal for another five years. Researchers at the center, which includes about a dozen MIT faculty members, have been working on different components of the prototype, including reactions between drug precursors, purification, crystallization, tablet formation and monitoring of the overall process.

To demonstrate the system, the researchers built a prototype that produces tablets of a specific drug manufactured by Novartis. However, the system is designed so that components can be swapped in and out to create different drugs.

Key to the continuous system is the development of chemical reactions that can take place as the reactants flow through tubes, as opposed to the huge vats in which most pharmaceutical reactions now take place. Traditional “batch processing” is limited by the difficulty of cooling large vats, but the flow system allows reactions that produce a great deal of heat to be run safely.

For drugs that require multiple steps, new ingredients can be added to the flow at specific points. Also integrated into the system are points where the drug solution is purified. Once the final active product is achieved, it is crystallized into a solid. Any necessary inert ingredients — such as preservatives or flavorings — are added, and the drug is then molded into the traditional tablet shape.

Novartis machine
Tablets produced by a prototype drug-manufacturing system built at MIT.
Photo: Dominick Reuter

In the new prototype, all of these steps take place within an enclosure 24 feet long, 8 feet wide and 8 feet tall in an MIT chemical engineering lab. In addition to Trout, MIT faculty members involved in the project include Klavs Jensen, Stephen Buchwald, Tim Jamison, Gregory Rutledge, Allan Myerson, Paul Barton and Richard Braatz.

Several of those researchers — Jensen, Jamison and Myerson — are now also working on an even smaller, tabletop version of the technology, funded by DARPA.

Many benefits

With continuous-flow manufacturing, drug companies could manufacture drugs in small plants scattered around the globe, offering greater supply flexibility. Eliminating the need to transport drug components during the manufacturing process would also cut costs significantly: Estimates for the total cost savings of switching to continuous manufacturing range from 15 to 50 percent.

Another advantage is improved quality control, according to the center’s researchers. “Once you go to continuous, you begin to have continuous monitoring, so it’s much easier to control the quality,” says Jensen, the Warren K. Lewis Professor and head of the Department of Chemical Engineering, who developed much of the flow chemistry for the prototype system.

Continuous manufacturing also allows chemists to explore new ways to make drugs, by using reactions that would require too much heat or dangerous chemicals if performed in a huge vat. “We can use a lot of chemistry in continuous that we couldn’t use in batch,” Trout says.

Novartis recently renewed its grant to MIT for a second five-year term, during which the MIT research teams will work on new ways to form tablets, recycle catalysts and design more complex multistep syntheses, among other projects.

In the meantime, Novartis is setting up a pilot plant at its headquarters in Basel, Switzerland, to create a larger-scale version of the flow technology developed at MIT. It will likely take another four years to begin commercial rollout, and another five to 10 years to convert all of Novartis’ production facilities, says Tom Van Laar, head of global technical operations for Novartis. He expects that many other pharmaceutical companies will head in the same direction.

“It’s kind of like what happened with the first iPad. When it became successful, everybody else started making tablet computers,” Van Laar says. “I think the benefits are so huge, companies are almost going to have to try to do it.”

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Jun 102014
 

2D chemical structure of 1393477-72-9

Selinexor (KPT-330)

1393477-72-9

Karyopharm Therapeutics, Inc.

WO2011109799A1

WO2013019548A1

  • 443.3099

Synonyms

Karyopharm Announces Initiation of Phase 2 Study of Selinexor (KPT-330) in Patients with

MarketWatch

“These patients were treated in our Phase 1 clinical trial of Selinexor in … Additional Phase 1 and Phase 2 studies are ongoing or currently planned and … the discovery and development of novel first-in-class drugs directed against …

Selinexor, a Exportin-1 (CRM1/XPO1) agonist, is in phase II clinical trials at Karyopharm for the treatment of advanced or metastatic gynecological malignancies (cervical, ovarian and uterine carcinomas) and recurrent glioblastomas. The company is also evaluating the compound in early clinical trials for the treatment of advanced solid tumors, hematological cancer (non-Hodgkin’s lymphoma, multiple myeloma and Waldenstrom’s macroglobulinemia), soft tissue or bone sarcoma, relapsed or refractory acute myeloid leukemia (AML) and relapsed or refractory acute lymphoblastic leukemia (ALL).

In 2014, orphan drug designation was assigned in U.S. for the treatment of acute myeloid leukemia and diffuse large B-cell lymphoma

 

Cells from most major human solid and hematologic malignancies exhibit abnormal cellular localization of a variety of oncogenic proteins, tumor suppressor proteins, and cell cycle regulators (Cronshaw et al. 2004, Falini et al 2006). For example, certain p53 mutations lead to localization in the cytoplasm rather than in the nucleus. This results in the loss of normal growth regulation, despite intact tumor suppressor function. In other tumors, wild-type p53 is sequestered in the cytoplasm or rapidly degraded, again leading to loss of its suppressor function. Restoration of appropriate nuclear localization of functional p53 protein can normalize some properties of neoplastic cells (Cai et al. 2008; Hoshino et al. 2008; Lain et al. 1999a; Lain et al. 1999b; Smart et al. 1999), can restore sensitivity of cancer cells to DNA damaging agents (Cai et al. 2008), and can lead to regression of established tumors (Sharpless & DePinho 2007, Xue et al. 2007). Similar data have been obtained for other tumor suppressor proteins such as forkhead (Turner and Sullivan 2008) and c-Abl (Vignari and Wang 2001). In addition, abnormal localization of several tumor suppressor and growth regulatory proteins may be involved in the pathogenesis of autoimmune diseases (Davis 2007, Nakahara 2009). CRMl inhibition may provide particularly interesting utility in familial cancer syndromes (e.g. , Li-Fraumeni Syndrome due to loss of one p53 allele,

BRCA1 or 2 cancer syndromes), where specific tumor suppressor proteins (TSP) are deleted or dysfunctional and where increasing TSP levels by systemic (or local) administration of CRMl inhibitors could help restore normal tumor suppressor function. Specific proteins and R As are carried into and out of the nucleus by specialized transport molecules, which are classified as importins if they transport molecules into the nucleus, and exportins if they transport molecules out of the nucleus (Terry et al. 2007;

Sorokin et al. 2007). Proteins that are transported into or out of the nucleus contain nuclear import/localization (NLS) or export (NES) sequences that allow them to interact with the relevant transporters. Chromosomal Region Maintenance 1 (Crml or CRM1), which is also called exportin-1 or Xpol, is a major exportin.

Overexpression of Crml has been reported in several tumors, including human ovarian cancer (Noske et al. 2008), cervical cancer (van der Watt et al. 2009), pancreatic cancer (Huang et al. 2009), hepatocellular carcinoma (Pascale et al. 2005) and osteosarcoma (Yao et al. 2009) and is independently correlated with poor clinical outcomes in these tumor types.

Inhibition of Crml blocks the exodus of tumor suppressor proteins and/or growth regulators such as p53, c-Abl, p21, p27, pRB, BRCA1, IkB, ICp27, E2F4, KLF5, YAP1, ZAP, KLF5, HDAC4, HDAC5 or forkhead proteins (e.g., FOX03a) from the nucleus that are associated with gene expression, cell proliferation, angiogenesis and epigenetics. Crml inhibitors have been shown to induce apoptosis in cancer cells even in the presence of activating oncogenic or growth stimulating signals, while sparing normal (untransformed) cells. Most studies of Crml inhibition have utilized the natural product Crml inhibitor Leptomycin B (LMB). LMB itself is highly toxic to neoplastic cells, but poorly tolerated with marked gastrointestinal toxicity in animals (Roberts et al. 1986) and humans (Newlands et al. 1996). Derivatization of LMB to improve drug-like properties leads to compounds that retain antitumor activity and are better tolerated in animal tumor models (Yang et al. 2007, Yang et al. 2008, Mutka et al. 2009). Therefore, nuclear export inhibitors could have beneficial effects in neoplastic and other proliferative disorders.

In addition to tumor suppressor proteins, Crml also exports several key proteins that are involved in many inflammatory processes. These include IkB, NF-kB, Cox-2, RXRa, Commdl, HIFl, HMGBl, FOXO, FOXP and others. The nuclear factor kappa B (NF-kB/rel) family of transcriptional activators, named for the discovery that it drives immunoglobulin kappa gene expression, regulate the mRNA expression of variety of genes involved in inflammation, proliferation, immunity and cell survival. Under basal conditions, a protein inhibitor of NF-kB, called IkB, binds to NF-kB in the nucleus and the complex IkB-NF-kB renders the NF-kB transcriptional function inactive. In response to inflammatory stimuli, IkB dissociates from the IkB-NF-kB complex, which releases NF-kB and unmasks its potent transcriptional activity. Many signals that activate NF-kB do so by targeting IkB for proteolysis (phosphorylation of IkB renders it “marked” for ubiquitination and then proteolysis). The nuclear IkBa-NF-kB complex can be exported to the cytoplasm by Crml where it dissociates and NF-kB can be reactivated. Ubiquitinated IkB may also dissociate from the NF-kB complex, restoring NF-kB transcriptional activity. Inhibition of Crml induced export in human neutrophils and macrophage like cells (U937) by LMB not only results in accumulation of transcriptionally inactive, nuclear IkBa-NF-kB complex but also prevents the initial activation of NF-kB even upon cell stimulation (Ghosh 2008, Huang 2000). In a different study, treatment with LMB inhibited IL-Ιβ induced NF-kB DNA binding (the first step in NF-kB transcriptional activation), IL-8 expression and intercellular adhesion molecule expression in pulmonary microvascular endothelial cells (Walsh 2008). COMMDl is another nuclear inhibitor of both NF-kB and hypoxia-inducible factor 1 (HIFl) transcriptional activity. Blocking the nuclear export of COMMDl by inhibiting Crml results in increased inhibition of NF-kB and HIFl transcriptional activity (Muller 2009).

Crml also mediates retinoid X receptor a (RXRa) transport. RXRa is highly expressed in the liver and plays a central role in regulating bile acid, cholesterol, fatty acid, steroid and xenobiotic metabolism and homeostasis. During liver inflammation, nuclear RXRa levels are significantly reduced, mainly due to inflammation-mediated nuclear export of RXRa by Crml . LMB is able to prevent IL-Ιβ induced cytoplasmic increase in RXRa levels in human liver derived cells (Zimmerman 2006).

The role of Crml -mediated nuclear export in NF-kB, HIF-1 and RXRa signalling suggests that blocking nuclear export can be potentially beneficial in many inflammatory processes across multiple tissues and organs including the vasculature (vasculitis, arteritis, polymyalgia rheumatic, atherosclerosis), dermatologic (see below), rheumatologic

(rheumatoid and related arthritis, psoriatic arthritis, spondyloarthropathies, crystal arthropathies, systemic lupus erythematosus, mixed connective tissue disease, myositis syndromes, dermatomyositis, inclusion body myositis, undifferentiated connective tissue disease, Sjogren’s syndrome, scleroderma and overlap syndromes, etc.).

CRM1 inhibition affects gene expression by inhibiting/activating a series of transcription factors like ICp27, E2F4, KLF5, YAP1, and ZAP.

Crml inhibition has potential therapeutic effects across many dermatologic syndromes including inflammatory dermatoses (atopy, allergic dermatitis, chemical dermatitis, psoriasis), sun-damage (ultraviolet (UV) damage), and infections. CRMl inhibition, best studied with LMB, showed minimal effects on normal keratinocytes, and exerted anti-inflammatory activity on keratinocytes subjected to UV, TNFa, or other inflammatory stimuli (Kobayashi & Shinkai 2005, Kannan & Jaiswal 2006). Crml inhibition also upregulates NRF2 (nuclear factor erythroid-related factor 2) activity, which protects keratinocytes (Schafer et al. 2010, Kannan & Jaiswal 2006) and other cell types (Wang et al. 2009) from oxidative damage. LMB induces apoptosis in keratinocytes infected with oncogenic human papillomavirus (HPV) strains such as HPV 16, but not in uninfected keratinocytes (Jolly et al. 2009).

Crml also mediates the transport of key neuroprotectant proteins that may be useful in neurodegenerative diseases including Parkinson’s disease (PD), Alzheimer’s disease, and amyotrophic lateral sclerosis (ALS). For example, by (1) forcing nuclear retention of key neuroprotective regulators such as NRF2 (Wang 2009), FOXA2 (Kittappa et al. 2007), parking in neuronal cells, and/or (2) inhibiting NFKB transcriptional activity by sequestering IKB to the nucleus in glial cells, Crml inhibition could slow or prevent neuronal cell death found in these disorders. There is also evidence linking abnormal glial cell proliferation to abnormalities in CRMl levels or CRMl function (Shen 2008).

Intact nuclear export, primarily mediated through CRMl, is also required for the intact maturation of many viruses. Viruses where nuclear export, and/or CRMl itself, has been implicated in their lifecycle include human immunodeficiency virus (HIV), adenovirus, simian retrovirus type 1, Borna disease virus, influenza (usual strains as well as H1N1 and avian H5N1 strains), hepatitis B (HBV) and C (HCV) viruses, human papillomavirus (HPV), respiratory syncytial virus (RSV), Dungee, Severe Acute Respiratory Syndrome coronavirus, yellow fever virus, West Nile virus, herpes simplex virus (HSV), cytomegalovirus (CMV), and Merkel cell polyomavirus (MCV). (Bhuvanakantham 2010, Cohen 2010, Whittaker 1998). It is anticipated that additional viral infections reliant on intact nuclear export will be uncovered in the future.

The HIV-1 Rev protein, which traffics through nucleolus and shuttles between the nucleus and cytoplasm, facilitates export of unspliced and singly spliced HIV transcripts containing Rev Response Elements (RRE) RNA by the CRMl export pathway. Inhibition of Rev-mediated RNA transport using CRMl inhibitors such as LMBor PKF050-638 can arrest the HIV-1 transcriptional process, inhibit the production of new HIV-1 virions, and thereby reduce HIV-1 levels (Pollard 1998, Daelemans 2002). Dengue virus (DENV) is the causative agent of the common arthropod-borne viral disease, Dengue fever (DF), and its more severe and potentially deadly Dengue hemorrhagic fever (DHF). DHF appears to be the result of an over exuberant inflammatory response to DENV. NS5 is the largest and most conserved protein of DENV. CRMl regulates the transport of NS5 from the nucleus to the cytoplasm, where most of the NS5 functions are mediated. Inhibition of CRMl -mediated export of NS5 results in altered kinetics of virus production and reduces induction of the inflammatory chemokine interleukin-8 (IL-8), presenting a new avenue for the treatment of diseases caused by DENV and other medically important flaviviruses including hepatitis C virus (Rawlinson 2009).

Other virus-encoded RNA-binding proteins that use CRMl to exit the nucleus include the HSV type 1 tegument protein (VP 13/14, or hUL47), human CMV protein pp65, the SARS Coronavirus ORF 3b Protein, and the RSV matrix (M) protein (Williams 2008, Sanchez 2007, Freundt 2009, Ghildyal 2009).

Interestingly, many of these viruses are associated with specific types of human cancer including hepatocellular carcinoma (HCC) due to chronic HBV or HCV infection, cervical cancer due to HPV, and Merkel cell carcinoma associated with MCV. CRMl inhibitors could therefore have beneficial effects on both the viral infectious process as well as on the process of neoplastic transformation due to these viruses.

CRMl controls the nuclear localization and therefore activity of multiple DNA metabolizing enzymes including histone deacetylases (HDAC), histone acetyltransferases (HAT), and histone methyltransferases (HMT). Suppression of cardiomyocyte hypertrophy with irreversible CRMl inhibitors has been demonstrated and is believed to be linked to nuclear retention (and activation) of HDAC 5, an enzyme known to suppress a hypertrophic genetic program (Monovich et al. 2009). Thus, CRMl inhibition may have beneficial effects in hypertrophic syndromes, including certain forms of congestive heart failure and hypertrophic cardiomyopathies.

CRMl has also been linked to other disorders. Leber’s disorder, a hereditary disorder characterized by degeneration of retinal ganglion cells and visual loss, is associated with inaction of the CRMl switch (Gupta N 2008). There is also evidence linking

neurodegenerative disorders to abnormalities in nuclear transport.

…………………………………………

PATENT

 

http://www.google.com/patents/WO2013019548A1?cl=en

 

To date, however, small-molecule, drug-like Crml inhibitors for use in vitro and in vivo are uncommon. SUMMARY OF THE INVENTION

The present invention relates to compounds, or pharmaceutically acceptable salts thereof, useful as nuclear transport modulators. The invention also provides

pharmaceutically acceptable compositions comprising compounds of the present invention and methods of using said compounds and compositions in the treatment of various disorders, such as those associated with abnormal cellular responses triggered by improper nuclear transport..

In one embodiment of the invention, the compounds are represented by formula I:

 

Figure imgf000013_0001

 http://www.google.com/patents/WO2013019548A1?cl=en

HERE IT REFERS AS 1-16  READER PLEASE CHECKABOVE AND BELOW FOR ERROR

 

Figure imgf000101_0001

HERE IT REFERS AS 1-18  READER PLEASE CHECK

http://www.google.com/patents/WO2013019548A1?cl=en

 

Example 1 : Synthesis of Intermediate (Z)-3-(3-(3,5-bis(trifluoromethyl)phenyl)-lH-l,2,4- triazol-l-yl)acrylic acid.

 

Synthesis of 3,5-bis(trifluoromethyl)benzothioamid

 

A 2-L, 3-necked, round-bottomed flask was charged with a solution of 3,5- bis(trifluoromethyl)benzonitrile (200 g) in DMF (1 L). The solution was then treated with NaSH (123.7 g, 2.0 eq.) and MgCl2 (186.7 g, 1.0 eq.) and the reaction mixture was stirred at RT for 3 hours. The mixture was poured into an ice-water slurry (10 L) and the compound was extracted with EtOAc (3 x 1 L). The combined organic layers were washed with aqueous saturated brine (3 x 100 mL), dried over anhydrous Na2S04, filtered, and concentrated under reduced pressure to afford 205 g of desired crude 3,5- bis(trifluoromethyl)benzothioamide (yield: 90 %), which wasused without purification in the following step.

Synthesi -(3,5-bis(trifluoromethyl)phenyl)-lH-l 2,4-triazole:

 

A 5-L, 3-necked, round-bottomed flask was charged with a solution of 3,5- bis(trifluoromethyl)benzothioamide (205.65 g) in DMF (1.03 L). Hydrazine hydrate (73.2 mL, 2.0 eq.) was added dropwise and the reaction mixture was stirred at RT for 1 h. HCOOH (1.03 L) was added dropwise and the reaction mixture was refluxed at 90 °C for 3 hours. After being allowed to cool to RT, the reaction mixture was poured into saturated aqueous sodium bicarbonate solution (7 L) and extracted with EtOAc (3 x 1 L). The combined organic layers were washed with aqueous saturated brine (3 x 500 mL), dried over anhydrous Na2S04, filtered, and concentrated under reduced pressure (35 °C, 20 mmHg) to afford 180 g of crude compound. This crude material was stirred with petroleum ether (3 x 500 mL) , filtered and dried to obtain 160 g. of 3-(3,5-bis(trifluoromethyl)phenyl)-lH- 1,2,4-triazole obtained as a pale yellow solid (yield: 75%).

Synthesis of (Z)-isopropyl 3-(3-(3,5-bis(trifluoromethyl)phenyl)-lH-l,2,4-triazol-l- yl)acrylate:

 

A 2-L, 3-necked, round-bottomed flask was charged with a solution of 3-(3,5- bis(trifluoromethyl)phenyl)-lH-l ,2,4-triazole (160 g) in DMF (960 mL). The solution was treated with DABCO (127.74 g, 2 eq.) and stirred for 30 min before adding (Z)-isopropyl 3- iodoacrylate (150.32 g, 1.1 eq.) dropwise. After ca. 1 hour, the reaction mixture was poured into an ice-water slurry (5 L) and extracted with EtOAc (3 x 1 L). The combined organic layers were washed with aqueous saturated brine (3 x 100 mL), dried over anhydrous Na2S04, filtered, and concentrated under reduced pressure (35 °C, 20 mmHg) to afford 250 g of crude compound that was purified by column chromatography (60/120 silica gel) using a ethyl acetate/n-hexane gradient (the column was packed in hexane and the desired compound started eluting from 2% EtOAC/n-hexane). Fractions containing the desired compounds were combined to afford 138 g the pure desired compound (yield: 61%).

Synthesis of (Z)-3 -(3 -(3 ,5-bis(trifluoromethyl)phenyl)- 1 H- 1 ,2,4-triazol- 1 -yl)acrylic acid:

 

In a 5-L, 3-necked, round-bottomed flask, (Z)-isopropyl 3-(3-(3,5- bis(trifluoromethyl)phenyl)-lH-l,2,4-triazol-l-yl)acrylate (130 g, 1.0 eq.) was dissolved in THF (1.3 L). A solution of LiOH (69.3 g, 5.0 eq.) in water (1.3 L) was added dropwise to the solution and the reaction mixture was stirred at room temperature for 4 h before being quenched with 400 mL ice-water slurry and made acidic (pH = 2-3) with dilute aqueous HC1. The mixture was extracted with EtOAc (3 x 1 L) and the combined organic layers were washed with brine, dried over anhydrous Na2S04 and concentrated under reduced pressure to afford 110 g of desired carboxylic acid (yield: 94 %) (cis content = 90.0%, trans content = 8.2% by LCMS).

Example 17: Synthesis of (E)-3-(3-(3,5-bis(trifluoromethyl)phenyl)-lH-l,2,4-triazol-l-yl)- ‘-(pyrazin-2-yl)acrylohydrazide

 

Synthesis of 3,5-bis(trifluoromethyl)benzothioamide:

 

A 2-L, 3 -necked, round-bottomed flask, charged with a solution of 3,5- bis(trifluoromethyl)benzonitrile (200 g) in DMF (1 L), was treated with NaSH (123.7 g, 2.0 eq.) and MgCl2 (186.7 g, 1 eq.). The reaction mixture was stirred at RT for 3 h before being poured into an ice-water slurry (10 L) and was extracted with EtOAc (3 x 1 L). The combined organic extracts were washed with brine (3 x 100 niL), dried over anhydrous Na2S04, filtered, and concentrated under reduced pressure (25 °C, 20 mmHg) to afford 205 g of crude compound (yield: 90 %), which was used in the following step without further purification.

Synthesis of 3-(3,5-bis(trifluoromethyl)phenyl)-lH-l,2,4-triazole:

 

A 5-L, 3-necked, round-bottomed flask, charged with a solution of 3,5- bis(trifluoromethyl)benzothioamide (205.65 g) in DMF (1.03 L) was treated with hydrazine hydrate (73.16 mL, 2.0 eq.) added dropwise. The reaction mixture was stirred at room temperature for 1 h before being treated with HCOOH (1.028 L) added dropwise. The reaction mixture was refluxed at 90°C for 3 h then cooled to room temperature and poured into saturated aqueous NaHC03 solution (7 L) and extracted with EtOAc (3 x 1L). The combined organic layers were washed with brine (3 x 500 mL), dried over anhydrous Na2S04, filtered, and concentrated under reduced pressure (35°C, 20 mmHg) to afford 180 g of a solid. The solid was suspended in petroleum ether and the suspension was stirred, filtered and dried to afford the desired triazole as a pale yellow solid (160 g, yield: 75%).

Synthesis of (Z)-isopropyl 3-(3-(3,5-bis(trifluoromethyl)phenyl)-lH-l,2,4-triazol-l- yl)acrylate and (E)-isopropyl 3-(3-(3,5-bis(trifluoromethyl)phenyl)-lH-l,2,4-triazol-l- yl)acrylate:

 

A 2-L, 3-necked, round-bottomed flask, charged with a solution of 3-(3,5- bis(trifluoromethyl)phenyl)-lH-l,2,4-triazole (160 g,) in DMF (0.96 L, 6V), was treated with DAB CO (127.74 g, 2 eq.) and stirred for 30 min. (Z)-isopropyl 3-iodoacrylate (150.32 g, 1.1 eq.) was added dropwise to the above reaction mixture and stirred for 1 h before being poured into an ice-water slurry (5 L) and extracted with EtOAc (3 x 1 L). The combined organic extracts were washed with brine (3 x 100 mL), dried over anhydrous Na2S04, filtered, and concentrated under reduced pressure (35°C, 20 mmHg) to afford 250 g of crude compound. Purification by column chromatography (Si02, 60/120 mesh, elution with EtOAc:hexanes gradient; the desired compounds started eluting in 2-2.5 % EtOAc in hexanes) afforded pure cis ester (138 g, yield: 61.6%) and pure trans ester (11.6 g, yield: 5.2%). Synthesis of (E)-3-(3-(3,5-bis(trifluoromethyl)phenyl)-lH-l ,2,4-triazol-l-yl);

acid:

 

A 500-mL, 3 -necked, round-bottomed flask was charged with a solution of (E)- isopropyl 3-(3-(3,5-bis(trifluoromethyl)phenyl)-lH-l ,2,4-triazol-l-yl)acrylate (5.0 g) in THF (50 mL). The solution was treated with a solution of LiOH (2.66 g, 5.0 eq.) in water (50 mL) and the reaction mixture was stirred at room temperature for 4 h. before being diluted with 40 mL water, acidified (pH = 2-3) with dilute aqueous HC1 and extracted with EtOAc (3 x 100 mL). The organic extract was washed with brine, dried over anhydrous Na2S04, filtered and concentrated under reduced pressure to afford 2.75 g of the desired unsaturated carboxylic acid (yield: 61.6 %, purity: 99.0 % by LCMS).

Synthesis of (E)-3-(3-(3,5-bis(trifluoromethyl)phenyl)-lH-l,2,4-triazol-l-yl)-N’- (pyrazin-2-yl)acrylohydrazide :

 

To a solution of (E)-3-(3-(3,5-bis(trifluoromethyl)phenyl)-lH-l,2,4-triazol-l- yl)acrylic acid (0.75 g,) in EtOAc (25 mL) and THF (12.5 mL) was added a solution of 2- hydrazinopyrazine (0.23 g) in 12 mL THF at room temperature. T3P (50% in ethyl acetate, 1.52 mL) and DIPEA (1.46 mL) were added dropwise and simultaneously and the reaction mixture was stirred for 30 min at room temperature before being quenched with ice-cold water and extracted with EtOAc (3 x 25 mL). The combined organic layers were washed with brine, dried over anhydrous Na2S04 and concentrated under reduced pressure (35°C, 20 mmHg), affording 0.698 g of a crude solid. Trituration first with petroleum ether then with Et20 afforded 275 mg (yield: 29%) (E)-3-(3-(3,5-bis(trifiuoromethyl) phenyl)- 1H- 1,2,4- triazol-l-yl)-N’-(pyrazin-2-yl)acrylohydrazide. 1H NMR (400 MHz, DMSO-d6) δ ,10.3 (s, 1H), 9.15 (s, 2H), 8.59 (s, 2H), 8.30-8.26 (d, J= 14.8 Hz, 1H), 8.13 (s, 1H), 8.06-8.07 (m, 1H), 6.98-6.95 (d, J= 13.4 Hz, 1H); LCMS for Ci7H12F6N70 [M+H]+ 443.31 ; found 444.19 (RT 2.625 min, purity: 99.06%).

MY SUGESTION TO U

 http://www.google.com/patents/WO2013019548A1?cl=en

(Z)-isopropyl 3-(3-(3,5-bis(trifluoromethyl)phenyl)-lH-l,2,4-triazol-l- yl)acrylate  IS THE INTERMEDIATE

any discussion   mail  amcrasto@gmail.com

NOTE IF U USE Z OR CIS STARTING  INTERMEDIATE U WILL GET Z ISOMER

…………………………………………………………

int 75 in

http://www.google.com/patents/WO2011109799A1?cl=en

Figure imgf000307_0001

Exam le 75

 

Molecular Weight: 239.12 Molecular Weight: 273.2 Molecular Weight: 281 .2

 

Molecular Weight: 393.3

[00715] Synthesis of Intermediate 1)

 

Molecular Weight: 239.12 Molecular Weight: 273.2

[00716] In a 100-mL, 3N round-bottomed flask equipped with nitrogen inlet, and a rubber septum, 3,5-bis(trifluoromethyl)benzonitrile (5.0 g,1.0 eq) dissolved in DMF (50 mL,10V),Added NaSH(3.09 g,2.0eq) and MgC12 (4.24 g,l eq).Reaction mixture was stirred at RT for 2-3h. The progress of reaction was followed by TLC analysis on silica gel with 40%EtOAc- hexane as mobile phase. SM Rf=0.5 and Product Rf=0.3. Reaction mixture was poured in to ice water (250mL) and extracted with EtOAc ( 3x 100 mL). The combined organic layers were washed with brine solution (3xl00mL), dried over MgS04, filtered, and concentrated by rotary evaporation (25°C, 20mmHg) to afford 5.0g of Crude compound which was used for next step without any purification, Yield (87.5%). Mass [M+l]+: 273.8

[00717] Synthesis of Intermediate-2

 

Molecular Weight: 273.20 Molecular Weight: 281 .16

[00718] In a 250-mL, 3N round-bottomed flask equipped with nitrogen inlet, and a rubber septum, Intermediate- 1(5.0 g, 1.0 eq.) was dissolved in DMF (50 mL,10V),added NH2NH2.H20 (25.0 mL,5V). The reaction mixture was stirred at RT for 1 h. To this reaction mixture HCOOH (25.0 mL, 5V) was added and reaction mixture was refluxed at 90 0 for 2-3 h. The progress of reaction was followed by TLC analysis on silica gel with 50% Ethyl acetate-n-Hexane as mobile phase. SM Rf=0.50 and Product Rf=0.3. Reaction mixture was poured into ice water (500 mL) and neutralized with saturated sodium bicarbonate solution. The reaction mixture was extracted with EtOAc (3×100 mL). The combined organic layers were washed with brine solution,(3xl00mL), dried over MgS04, filtered, and concentrated by rotary evaporation (25°C, 20mmHg) to afford 4.6g of crude compound, yield (89.49%). Mass: 279.6(-ve mode).

 

Molecular Weight: 281.2 Molecular Weight: 393.3

[00719] In a 100-mL, 3N round-bottomed flask equipped with nitrogen inlet, and a rubber septum, Intermediate-2(4.5 g, 1.0 eq.) was dissolved in DCM(45 mL,10V),added TEA (2.10 g, 1.3 eq) and isopropyl propiolate (2.33 g, 1.3 eq). The Reaction mixture was stirred at RT for 30 min. The progress of reaction was followed by TLC analysis on silica gel with 50% Ethyl acetate-Hexane as mobile phase, SM f=0.30 and Product Rf=0.5. Reaction mixture was concentrated by rotary evaporation (25°C, 20mmHg) to afford 5.8 g of Crude compound. The crude reaction mixture was purified by column chromatography using silica 60/120 using Ethyl acetate: Hexane as mobile phase. The column (5x10cm) was packed in Hexane and started eluting in Ethyl acetate in gradient manner starting with fraction collection(50-mL fractions) from 5 % to 20 % Ethyl acetate in hexane. Compound started eluting with 20% Ethyl acetate in Hexane. Fraction containing such TLC profile was collected together to obtain pure compound (1.4 g), Yield (22.26%).1H NMR: CDC13, 400 MHz) δ 9.74(s,lH),5 8.63(s,2H),5 7.95(s,lH),5 7.28-7.3 l(d,J: 12.0 Hz,lH),55.75-5.78(d,J: 11.2 Ηζ,ΙΗ) δ 5.14-5.17 (m,lH),5 1.27-1.35(m,6H). LCMS of Ci6Hi3F6N302(M+l)+:393.28 found 393.77 at 4.707 min (LCMS 99.25%).

[00720] General method for Example 76, Example 77, Example 78, Example 79, Example 83: A mixture of 5-(3-Chlorophenyl)-l,2,4-triazole (0.50 g, 3.4 mmol), respective propiolate (0.52 ml, 5.1 mmol) and some drops of triethylamine in acetonitrile under nitrogen was stirred at room temperature for 12-16 h. Acetonitrile was removed under reduced pressure to give a residual oil, which was purified by flash chromatography (3-5%> EtOAc/hexanes) to afford the both cis and trans isomers. Cis isomer was isolated 10-30%) and trans was isolated in 30-50%) with overall yield of 50-80%.

 

 

WO2011109799A1 * Mar 5, 2011 Sep 9, 2011 Karyopharm Therapeutics, Inc. Nuclear transport modulatiors and uses thereof
US20110275607 Mar 5, 2011 Nov 10, 2011 Karyopharm Therapeutics, Inc. Nuclear transport modulators and uses thereof
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