US 8362006, Intervet International B.V., Boxmeer, The Netherlands, Zilpaterol, PATENT

Example 1 Preparation of 8,9-dihydro-2H,7H-2,9a-diazabenzo[cd]azulene-1,6-dione Part A. Preparation of chloro 2,3-dihydro-2-oxo-1H-benzimidazol-1-butanoate

4-(2-Oxo-2,3-dihydrobenzimidazol-1-yl)butyric acid (50 g; 0.227 mol), N,N-dimethylformamide (1.84 g; 0.025 mol; 0.11 eq), and dichloromethane (480 g; 5,652 mol; 24.89 eq) were charged to a stirred-tank reactor. Oxalyl chloride (31.12 g; 0.245 mol; 1.08 eq) was then dosed at 10-20° C. over a 1-hour period while stirring. The resulting mixture was then stirred at 10-20° C. for an additional hour. All the above steps were conducted under a N₂ atmosphere.Part B. Preparation of 8,9-dihydro-2H,7H-2,9a-diazabenzo[cd]azulene-1,6-dione.

The reaction product mixture from Part A was added to a slurry of aluminum chloride (100 g; 0.75 mol, 3.3 eq) in dichloromethane (320 g; 3.768 mol; 16.59 eq) over 2-5 hours at 60° C. and a pressure of 2.7 bar (absolute) in a stirred-tank reactor that allowed HCl gas to escape through an overpressure vent. The resulting slurry was stirred for an additional hour at that temperature, and then cooled to 12° C. In a separate stirred-tank reactor, water (800 g; 44.407 mol; 195.59 eq.) and aqueous 32.5% HCl (118 g; 1.052 mol HCl; 4.63 eq. HCl) were mixed. This mixture was cooled to 0° C., and the gas in the headspace was evacuated to 300 mbar (absolute). The slurry from the first reactor was then added portion-wise to the second reactor, whereby the temperature increased to 10-15° C. under distillation of dichloromethane. The first reactor was rinsed with additional dichloromethane (25 g; 0.294 mol; 1.3 eq), which was then added to the second reactor. Distillation of the dichloromethane was then completed at 300 mbar to atmospheric pressure (absolute) and 12-40° C. The resulting suspension was cooled to 0° C. The solid was filtered off, and washed 4 times with water (291.25 g each time; 64.668 mol total; 284.83 eq. total) and once with isopropanol (80 g; 1.331 mol; 1.331 eq) at 0° C. All the above steps were conducted under a N₂ atmosphere.Example 2 Preparation of 4,5-dihydro-imidazo[4,5,1-jk][1]benzazepin-2,6,7[1H]-trione-6-oxime.

8,9-Dihydro-2H,7H-2,9a-diazabenzo[cd]azulene-1,6-dione (50 g; 92.4% purity; 0.228 mol) prepared in accordance with the procedure in Example 1 was dried and mixed with isopropanol (7.23 g; 0.12 mol; 0.53 eq) and water (3.01 g; 0.167 mol; 0.73 eq) (in alternative experiments and in production, 8,9-dihydro-2H,7H-2,9a-diazabenzo[cd]azulene-1,6-dione prepared in accordance with the procedure in Example 1 was instead used as centrifuge-wet material without the addition of water and isopropanol). The resulting wet 8,9-dihydro-2H-7H-2,9a-diazabenzo[cd]azulene-1,6-dione was combined with sodium nitrite (19.05 g at 99.3% purity; 0.274 mol; 1.2 eq) and N,N-dimethylformamide (800 g; 10.945 mol; 47.9 eq) in a stirred-tank reactor. The mixture was heated to 50° C., and then 32% HCl (41.65 g; 0.366 mol HCl; 1.6 eq HCl) was added over a 30 minute period. Toward the end of the HCl addition (i.e., after greater than 1 eq HCl had been added), the temperature quickly increased to 60-70° C. After all the HCl was added, the mixture was stirred at 60° C. for an additional 30 minutes. The mixture then was cooled to 35° C. over a 2- hour period. Next, water (224.71 g; 12.473 mol; 54.6 eq) was added over a 2-hour period. The resulting mixture was then cooled to 0° C. over a 2-hour period, and maintained at that temperature for 2 hours. Afterward, the solid 4,5-dihydro-imidazo[4,5,1-jk][1]benzazepin-2,6,7[1H]-trione-6-oxime product was removed by filtration and washed 4 times with water (70.1 ml each time; 15.566 mol total; 68.13 eq total) and once with acetone (115.9 g; 99.9% purity; 1.994 mol; 8.73 eq). All the above steps were conducted under a N₂ atmosphere.Example 3 Scale-up Preparation of 8,9-dihydro-2H,7H-2,9a-diazabenzo[cd]azulene-1,6-dione Part A. Preparation of chloro 2,3-dihydro-2-oxo-1H-benzimidazol-1-butanoate

Dichloromethane (3772 L) and then 4-(2-oxo-2,3-dihydrobenzimidazol-1-yl)butyric acid (525 kg; 2.4 kmol) were charged to a stirred-tank reactor, followed by N,N-dimethylformamide (21 L). The resulting mixture was cooled to 10° C. Afterward, oxalyl chloride (326.8 kg)) was dosed at 10-15° C. over 2-3 hours while stirring. The resulting mixture was then stirred at 15-20° C. for an additional 1-3 hours. All the above steps were conducted under a N₂ atmosphere. Conversion was checked by in-process control (“IPC”).Part B. Preparation of 8,9-dihydro-2H,7H-2,9a-diazabenzo[cd]azulene-1,6-dione.

Aluminum chloride (1050 kg) and dichloromethane (2403 L) at 10-20° C. were charged to a stirred-tank reactor, followed by additional dichloromethane (112 L) at 10-20° C. to rinse the reactor. The reactor was then pressurized with N₂ to 2.7 bar (absolute), and heated to 58-60° C. Next, the product mixture from Part A was added over 2−5 hours. The resulting slurry was stirred for an additional 1-2 hours, and then cooled to 10-20° C. Afterward, the pressure was released. In a second stirred-tank reactor at 5° C., water (3675 L) was charged, followed by aqueous 33% HCl (452 L). This mixture was cooled to 0° C., and the gas in the headspace was evacuated to 270-470 mbar (absolute). About half the content from the first reactor was added to the second reactor at from 5-20° C. The mixture was maintained at 10-30° C. for an additional 30-90 minutes. In parallel to and following the transfer, distillation of dichloromethane occurred. The line between the two reactors was rinsed with dichloromethane (150 ml). The resulting rinse and the contents in the second reactor were transferred to a thud stirred-tank reactor. The transfer line between the second and third reactors was rinsed with water (200 L). This rinse also was charged to the third reactor. Water (3675 L) at 5° C. and 33% HCl (452 L) were then added to the second reactor. The resulting mixture was cooled to 0° C., and the pressure in the headspace was set to between 270-470 mbar (absolute). The second half of the content from the first reactor was then added to the second reactor at 5-20° C. This mixture was maintained at 10-30° C. for an additional 30-90 minutes. In parallel to and following the transfer, distillation of dichloromethane occurred. The line between the first and second reactors was rinsed with dichloromethane (150 ml). The resulting rinse and the contents in the second reactor were transferred to the third reactor. The transfer line between the second and third reactors was then rinsed with water (200 L). This rinse was charged to the third reactor. In the third reactor, the dichloromethane was further distilled at 30-40° C. under atmospheric pressure. When the distillation was complete, the suspension was cooled to 0−5° C., and then centrifuged in two parts. Each of the resulting cakes was washed with four times water (390 L for each wash) and once with isopropanol (508 L) at 0−5° C. All the above steps were conducted under a N₂ atmosphere.Example 4 Scale-up of Preparation of 4,5-dihydro-imidazo[4,5,1-jk][1]benzazepin-2,6,7[1H]-trione-6-oxime.

At 20° C., N,N-dimethylformamide (7068 L) was charged to a stirred-tank reactor, followed by 8,9-dihydro-2H,7H-2,9a-diazabenzo[cd]azulene-1,6-dione (450 kg total wet material, approximately 405 kg pure) prepared in accordance with the procedure in Example 3. The addition funnel was rinsed with N,N-dimethylformamide (105 L), and the rinse was charged to the reactor. The resulting mixture was heated at 45° C. until all the 8,9-dihydro-2H,7H-2,9a-diazabenzo[cd]azulene-1,6-dione was in solution. IPC was used to check the amount of pure 8,9-dihydro-2H,7H-2,9a-diazabenzo[cd]azulene-1,6-dione in the mixture, and, from that measurement (together with the mass of wet 8,9-dihydro-2H,7H-2,9a-diazabenzo[cd]azulene-1,6-dione and N,N-dimethylformamide), the exact amount of 8,9-dihydro-2H,7H-2,9a-diazabenzo[cd]azulene-1,6-dione was calculated, which, in turn, was used to calculate the amounts of N,N-dimethylformamide (17.3 kg/kg), sodium nitrite (0.412 kg/kg) and HCl 33% (0.873 kg/kg). For the duration of the IPC, the mixture was cooled to 20° C. Next, sodium nitrite (167 kg, based on 405 kg 8,9-dihydro-2H,7H-2,9a-diazabenzo[cd]azulene-1,6-dione) was added. The addition funnel was rinsed with N,N-dimethylformamide (105 L), and the rinse was charged to the reactor. The temperature was then increased to 45° C. Subsequently, additional N,N-dimethylformamide was charged in the amount calculated earlier (97 L, based on having a total of 7375 L DMF for 405 kg of 8,9-dihydro-2H,7H-2,9a-diazabenzo[cd]azulene-1,6-dione). Next, the resulting mixture was warmed to 48° C., and then 33% HCl (353 kg, based on the batch size) was added over 1 hour, causing the temperature to increase to 60-65° C. by the end of the addition. The mixture was then stirred at 60° C. for another 30 minutes. Next, the mixture was cooled to 45° C. over 1-2 hours. The resulting mixture was transferred into a second reactor. The first reactor was subsequently rinsed with N,N-dimethylformamide (105 L), and the rinse was charged to the second reactor. Water (2000 L) was then added over a 2-hour period at 38° C. The resulting mixture was cooled to 0° C. over 2-3 hours, and then stirred at that temperature for another 2-8 hours. Afterward, the mixture was centrifuged at 0° C., and the resulting cake was washed with three times with water (810 L each time), washed with acetone (1010 L), and dried at 65° C. under vacuum. All the above steps, except for the IPC, were conducted under a N₂ atmosphere.Example 5 Preparation of Zilpaterol Part A. Formation of Aminoalcohol Potassium Salt from Ketooxime

A stirred-tank reactor was purged 3 times with N₂ between high pressure (3 bar, absolute) and low pressure (1 bar, absolute) for 10 minutes each. Then a pressure of 0.9 bar (absolute) was established. Water (790 kg) was then charged to the reactor, followed by 4,5-dihydro-imidazo[4,5,1-jk][1]benzazepin-2,6,7[1H]-trione-6-oxime (255 kg) prepared in accordance with Example 4. The reactor contents were then heated to 40° C. Next, 45% KOH (214 kg) was continuously charged to the reactor, causing 4,5-dihydro-imidazo[4,5,1-jk][1]benzazepin-2,6,7[1H]-trione-6-oxime to form the corresponding potassium salt, which, in turn, dissolved (this could be visually verified). The reactor was then charged with active charcoal (13 kg). The resulting mixture was then stirred for 30 minutes at 40° C. The resulting mixture was filtered through a filter loop for one hour to remove the active charcoal. The mixture was then cooled to 15° C. A 5% palladium-on-carbon catalyst (25.5 kg, Johnson-Matthey) was then charged to the reactor. The reactor was then rinsed with water (50 kg). The resulting mixture in the reactor was stirred for 2-6 hours at 40° C. and a H₂ pressure of 5-10 bar (absolute). Afterward, the reactor was vented over 30 minutes, and the reaction was analyzed using HPLC. The contents were then filtered in a filter loop for 90 minutes. The filter cake was washed with water (50 L), and removed to recover palladium. The filtered solution was analyzed via HPLC to confirm complete conversion, and then used in the next step.Part B. Formation of zilpaterol-HOAc.

The solution from Part A was cooled to 30° C. Acetone (625 L) was then charged to the reactor. Acetic acid was added to adjust the pH to 7.5 (a pH of from about 7 to about 8 is preferred). The resulting mixture was then cooled to 15° C. Next, a 5% platinum-on-carbon catalyst (21.3 kg, Degussa) was charged to the reactor, followed by water (50 kg) to rinse the reactor. The head space was purged 3 times with H₂ between a high pressure of 5 bar (absolute) and a low pressure of 1 bar (absolute) for 15 minutes each. Then a hydrogen pressure of 9.0 bar (absolute, for hydrogenation) was established. The mixture was heated to 70° C. over 1 hour while being stirred, and then maintained at that temperature for an additional hour while being stirred. The reactor was then vented, and the headspace was purged with N₂. The reaction was analyzed using HPLC. Acetic acid (8 kg) was then charged to the reactor, and the resulting mixture was cooled to 30° C. More acetic acid was added to adjust the pH to 6.8. The mixture was then transferred through a filter loop for 1 hour while being maintained at 30° C. The resulting cake was washed with 7% aqueous acetic acid (75 L). The filtered solution was transferred to another stirred-tank reactor to be used in the next step.Part C. Formation of Zilpaterol Free Base

The stirred-tank reactor containing the product from Part B was purged 3 times with N₂ between high pressure (2 bar, absolute) and low pressure (1 bar, absolute) for 10 minutes each. Then a pressure of 0.9 bar (absolute) was established. Next, the mixture was concentrated by distillation to 30-70%. The concentrated mixture was cooled to 65° C. Ethanol (331 L) was charged to the reactor, and the resulting mixture was cooled to 50° C. The pH was adjusted to 10 using 25% NaOH. This caused zilpaterol free base to precipitate. The temperature was decreased to 0° C. to facilitate the precipitation, and maintained at that temperature for an additional hour. The solids were filtered off, and washed with water (700 L).Example 6 Synthesis of an HCl Salt of the ZilpaterolThe free base of zilpaterol is dissolved in ethanol. Subsequently, ethyl acetate saturated with HCl is added. The resulting mixture is vacuum-filtered to obtain a crude product containing the HCl salt of the zilpaterol. The crude product is dissolved in hot methanol. Ethyl acetate is then added, and the mixture is filtered to obtain the final HCl salt product.

Example 7 First Illustration of a Contemplated Suitable Dosage FormA tablet is prepared containing 2.5 or 5 mg of the HCl salt of Example 6, and sufficient excipient of lactose, wheat starch, treated starch, rice starch, talc, and magnesium stearate for a final weight of 100 mg.

Example 8 Second Illustration of a Contemplated Suitable Dosage FormGranules are prepared containing 12.5 or 25 of the HCl salt of Example 6 in each daily dose of granules.

Example 9 Third Illustration of a Contemplated Suitable Dosage FormThe HCl salt of Example 6 is crystallized using the methodology discussed U.S. Pat. No. 5,731,028 for making crystalline racemic trans zilpaterol. Less than 5% of the crystals have a size of less than 15 μm, and at least 95% of the crystals have a size of less than 250 μm. A premix of the crystalline HCl salt secured to a 300-800 μm corn cob support is then obtained using the methodology discussed in European Patent 0197188 (incorporated by reference into this patent). The concentration of the HCl salt in the premix is 3% (by weight).