NZ272053A - Process for preparing pharmaceutical grade ranitidine base - Google Patents

Description

^ / 'i. y ^ Priority Date(s): .fejb qu . AIL.C, qq.

[ Compile Specification Filed: "" i '-lass: PubHcatfon Date: I ■ ^ ^ ■ 1 ■ » M >••■>...<•• P.O. Journal No: ItkQZl PATENTS FORM NO. 5 Fee No. 1 & 4: $340.00 26 jUKIGQS "j PATENTS ACT 1953 COMPLETE SPECIFICATION PROCESS FOR THE MANUFACTURE OF PHARMACEUTICAL GRADE RANITIDINE BASE WE RANBAXY LABORATORIES LIMITED, an Indian company of A-2 Phase 1, Okhla 110020, INDIA hereby declare the invention, for which we pray that a patent may be granted to us, and the method by which it is to be performed to be particularly described in and by the following statement: PROCESS FOR THE MANUFACTURE OF PHARMACEUTICAL GRADE RANITIDINE BASE FIELD OF THE INVENTION This invention relates to a manufacturing process for the Ha-antagonist 'ranitidine', that is, N-(2-[[{5-(Dimethylamino)methyl]-2-furanyl] methyl] thio] ethyl-N' -methyl-2-nitro-1,1-ethenediamine in crystalline form having >99.Sk purity.

BACKGROUND OF THE INVENTION Ranitidine hydrochloride, as described and claimed in British Patent Specification No. 1,565,966 (Apr. 1980) shows potent histamine H2-blocking activity. A process for preparing ranitidine is known and described in U.S. Patent No. 4,128,658 (Dec. 1978) and in British Patent Specification No. 1,565,966 (Apr. 1980) . Though a method to prepare crude ranitidine base is described in U.S. Patent No. 4,128,658 (Dec. 1978), see Example 15 thereby, the ranitidine base produced by this method has not been evaluated for clinical application. In experiments following Example 15, the ranitidine base produced thereby is brownish yellow in color and has a purity of less than 97V (HPLC) , with related substances being ca. 2V. 27 2 y SUMMARY OF THE INVENTION The present invention provides a process for producing ranitidine base which is crystalline, is of pharmaceutical grade (>99.5% purity) , and .is convenient to produce on a commercial scale.

According to the invention, a process for preparing pharmaceutical grade ranitidine base comprises reacting a mixture of N-methyl-1-(methylthio) -2-nitroetheneamine and 2-[[ [5- (Dimethylamino)m'ethyl-2-furanyl]methyl]thio]ethanamine in water at 40°C to reflux temperature, removing the unreacted'starting material and other impurities at a suitable pH (4-S), preferably by washing, separating the ranitidine base at a suitable pH (9-10), removing water, if any, and precipitating ranitidine base from a "suitable organic solvent", and collecting the resulting product. The product so obtained can be crystallized from a "suitable organic solvent" to produce almost white powder of ranitidine base, having a purity of about 99.6% (HPLC), with related substances being less -nan 0.4%.

BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 shows the infra-red spectrum in KBr disc of ranitidine base prepared by the method described in Example 2 below. Ranitidine base prepared this way was also characterized by its proton magnetic resonance spectrum in CDC1,. 2 / ki \j jj Fig. 2 shows a comparative dissolution profile (dissolution © parameters as per USP) of Zantac (Glaxo) 300mg tablet vs. !300mg tablet of ranitidine base prepared in accordance with the present invention.

DETAILED DESCRIPTION OF THE INVENTION In accordance with the present invention, pharmaceutical grade (>99.5% purity) is prepared by reacting a mixture of N-methyl-rl-(methylthio)-2-nitroetheneamine and 2-[[[5-(dimethylamino)methyl-2-furanyl] methyl) thio] ethanamine in water at a temperature from about 40°C to reflux temperature, acidifying the solution to remove unreacted starting materials and other impurities, basifying the solution to separate ranitidine base from the solution, removing water if any, and precipitating the ranitidine base from a suitable organic solvent such as a lower alkanol;, and collecting the precipitated ranitidine base. Desirably, the precipitated base is dissolved in a suitable organic solvent and crystallized therefrom.

It has been found that if the ranitidine base is prepared under the above defined working conditions, the following advantages are obtained: a) the product is easily filtrable and can be readily dried; b) the solvents used are readily recoverable; c) the product can be crystallized from the same solvent system; d) the process is economical and convenient to operate on a commercial scale; e) the process provides a product which has a high degree of purity (>99.5V); and f) the product is stable.

Generally, the reaction is carried out iri water as a medium that has been heated by standard means to a temperature of from about 400C to reflux temperature, preferably to about 45-70°C, most preferably to about 50°C. This temperature is considerably lower than the reaction temperature of the process described in Example 15 of U.S. 4,128,658. The amount of water is at least 1 part by volume per part of the starting material. Higher amounts of water and generally up to 10 parts by volume can be used . Amounts higher than 10 volumes are not useful from an economical point of view because large size apparatus would be necessary.

The reaction will typically be accomplished within about 3 to about 10 hrs, preferably, within 3-4 hours. However, the length of time required will vary depending on such factors as total volume of solution, size of batch and container, temperature of the reaction, and presence or absence of stirring.

The reaction mixture can be acidified to a pH of about 4-5 by means of mineral acids, preferably hydrochloric acid or sulfuric acid, in different concentrations, or organic acids. Unreacted starting 4 material and other impurities can be washed with any water-immiscible solvents like chlorinated hydrocarbons, aromatic hydrocarbons and ketones at different temperatures.

The reaction mixture can be basified to a pH of about 9-10 with basifying agents such as alkali metal carbonates, bicarbonates and hydroxides.

The term "suitable organic solvent" means any lower alkanol and includes those primary, secondary and tertiary alcohols having from one to six carbons atoms, ketones, esters and aliphatic or aromatic hydrocarbons having from one to ten carbon atoms. Mixtures of two or more solvents are also contemplated.

It is also desirable to filter the solution prior to crystal formation in order to remove any insoluble, particulate material. The solutions can be cooled to -10° to 50°C, preferably to about 0 -30°C, most preferably to about 10°C, before precipitation b'y standard procedures well known in the art.

Addition of a miscible solvent such as hexane, petroleum ether, toluene, ethyl acetate and n-butyl acetate to the solution can be advantageously used to complete crystallization.

Methods known in the art may be used with the process of this invention to enhance any aspect of this process. For example, the 27 O t £. V solution may be seeded with one or more crystals of ranitidine base prior to the initiation of product crystallization.

Generally, after cooling, the product can be collected by any standard method known in the art such as by filtration, filtration under vacuum, or decantation and drying.. Typically, this product will be collected by filtration when any of the solvents within the scope of this process are used.

Ranitidine base prepared as above may further be crystallized using conditions and solvents for crystallizations similar to those described above. Mixtures of two or more solvents are also contemplated.

Histamine H, antagonist activity of ranitidine base prepared as above Jhas been studied in-vitro by using guinea pig atrium and in-vivo on aspirin induced gastric lesions in conscious rats. Both ranitidine base as well as Form 2 ranitidine hydrochloride were found equi-potent in these tests.

Acute toxicity studies were conducted in mice. From the results of the acute toxicity studies it is concluded that ranitidine base prepared as above is as safe as Form 2 ranitidine hydrochloride.

Ranitidine base prepared an above has boon used in formulating the following products: 27205 i) Ranitidine base tablets in two strengths of ISOmg and 30 0mg, and ii) Ranitidine base injection containing 25mg/ml of the drug. Both strengths of the tablet formulation have been found to have comparable dissolution rates in in-vitro performance to that of Zantac (Glaxo) which contains Form 2 ranitidine hydrochloride. See Fig. 2 .

The accelerated stability of these formulations is satisfactory and long term room temperature studies are currently underway.

The following specific examples are presented to illustrate the inventive process, but they should not be construed as limiting the scope of this invention in any way.

EXAMPLE l Preparation of Ranitidine Base 2- [ [ [5- (Dimethylamino)methyl-2-furanyl] methyl] thio] ethanamine (50g) and N-methyl-1-(methylthio)-2-nitroetheneamine (40g) in water (235ml) was jstirred and heated at 4S-50°C. The solution was stirred further for 3-1 hrs. It was acidified with hydrochloric acid and extracted with chloroform. The solution was basified with potassium carbonate and ranitidine base was separated. The water, if any, w<is removed by azeotropic distillation under reduced pressure at lO-flS'C using isopropanol. The resultant solution v/as cooled to 10°C and n-hexane (500ml) was added. Ranitidine base was filtered off and dried under vacuum to give the crude product (66.2g), m.p. 68-70°C; purity = 99.4V (HPLC); IR(KBr): 3280, 3200, 2820, 2774, 1620, 1580, 1440, 1370, 1258, 1130, 1020, 990, 820, 790, 760, 630 and 600 cm"1; 6„(CDCl3) : 2. 23 [6H, s, -N(CH-,) ?1 . 2 . 75 ( 2H, t, -SCH3CHj), 2 . 8 5 ( 3H, br d, CHjNH-) , 3.3 (2H,2t, -CH?NH- ) ,3.4 (2 H,s, >NCHj) , 3.7 (2H.s.CH, bridge linking), 6.0-6.2 (2H,AB,furan) and 6.5 (1H, s, =CHN02) .

The process of Example 1 was repeated at a commercial scale, using 2 - ( [ [5 - (Dimethylamino) methyl-2 -furanyl] methyl] thio] ethanamine (35kg) and N-methyl-1- (methylthio)-2-nitroetheneamine (28kg) to give crude ranitidine base (46.5 kg), m.p. 68-70°C; purity - 99.1% (HPLC). ; The process of Example 1 was repeated at 25g scale, using a mixture of ethyl acetate and isopropanol instead oC isopropanol to give ranitidine base (34.5g), m.p. 67-69°C; purity = 98.8% (HPLC). 2 - ( [ [5- (Dimethylamino) methyl - 2- Curanyl) methyl) t liio] ethanamine ('/!5g) r EXAMPLE 2 EXAMPLE 3 EXAMPLE 4 r 8 272053 and N-methyl-1-(methylthio)-2-nitroetheneamine (18g) in water (35ml) was stirred and heated at 50°C. ' The solution was stirred further for 3-4 hrs. It was acidified with sulfuric acid and extracted with chloroform. The solution was basified with potassium carbonate and ranitidine base was separated. The water, if any, was removed by azeotropic distillation under reduced pressure at 40-45°C using isopropanol. The resultant solution was cooled to 10°C and n-hexane (250ml) was added. Ranitidine base was filtered off and dried under vacuum to give the crude product (30g), m.p. 67-69°C, purity =99.1% (HPLC) EXAMPLE 5 2- [ [ [5- (Dimethylamino) methyl-2-furanyl) methyl] thio] ethanamine (25g) and N-methyl-1-(methylthio) 2-nitroetheneamine (20g) in water (118ml) was stirred and heated at 50°C. The solution.was stirred further for 3-4 hrs. It was acidified with sulfuric acid and extracted with chloroform. The solution was basified with potassium carbonate and ranitidine base was extracted with chloroform and worked up. Isopropanol was added to the residue, cooled to 10°C, and n-hexane (250 ml) was added. Ranitidine base was filtered off and dried under vacuum to give the crude product (33 g) , m.p. 67-69-C; purity«=99% (HPLC) 27205 EXAMPLE 6 Crystallization of ranitidine base Ranitidine base (25g) prepared earlier was crystallized by dissolving in isopropanol at 35-40°C and precipitating from n-hexane. The slurry was cooled to 10°C and stirred for 1-2 hrs. The product was filtered off, washed with n-hexane, and dried to give pure ranitidine base (21g) , m.p. 71-72°C; purity =99.6% (HPLC) EXAMPLE 7 The process of Example 5 was repeated using isobutanol instead of isopropanol at 5g scale to give pure, ranitidine base (3.9g), m.p. 71-72°C; purity = 99.8% (HPLC) EXAMPLE 8 Ranitidine base (I50g) prepared earlier was crystallized by dissolving in toluene at 38-40°C. The resultant solution v/as cooled to 10°C and the slurry was stirred for 1 hour at 10-12°C. The product v/as filtered off, washed with pre-cooled toluene and dried under vacuum to give pure ranitidine base (135g) , m.p. 70-710 C; purity = 99.8% (HPLC) EXAMPLE 9 The process of Example 7 was repeated, using ethyl acetate instead of toluene to give pure ranitidine base (137g), m.p. 70-7l°C; purity = 99.8% (HPLC) EXAMPLE 10 The process of Example 7 was repeated, using 4-methylpentan-2-one instead of toluene to give pure ranitidine base (I20g) , m.p. 71-72 °C; purity = 99.7% (HPLC) It is believed that the higher purity ranitidine base produced by the process of the present invention in comparison to the method described in Example 15 of U.S. 4,128,658, may be attributed to one or more of the following combination of factors: (1) reaction under higher dilution of reaction medium, i.e., water, thereby producing fewer impurities; (2) higher molar concentration (1.157:1) of one of the starting materials, i.e., N-methyl-1-(methylthio)-2-nitroetheneamine, with respect to 2-[[(5-(Dimethylamino) methyl - 2 - furanyl) methyl) thio] ethanamine, as against a ratio of 1.036:1 in Example 15 of U.S. 4 , 128,65 8; (3) <ihortcr reaction time (ca. 3-4 hours) than in Example IS of: U.S. 4,128,6511, which reduces the quantity o£ 272 ( impurities formed, and monitoring of the completion of the reaction by TLC; (<l) removal of excess starting materials and impurities by extraction at a suitable pH; and (5) recrystallization of the crude ranitidine base to give a higher purity final product.

While the invention has been described by reference to specific embodiments, this v/as for purposes of illustration only. Numerous alternative embodiments will be apparent to those skilled in the art and are considered to be within the scope of the invention. 27 2 0 5 3

Claims (26)

WHAT WE CLAIM IS:
1. A process for preparing pharmaceutical grade ranitidine base comprising reacting a mixture of N-methyl-l-(methylthio)-2-nitroetheneamine and 2-[[[5-(dimethylamino) methyl-2-furanyl]methyl]thio]ethanamine in a water solution at a temperature from about 40°C to reflux temperature, adjusting the pH of said solution a first time to remove unreacted starting materials and impurities, adjusting the pH of said solution a second time to separate ranitidine base from said solution, removing water if any and precipitating ranitidine base from an organic solvent, and collecting said precipitated ranitidine base.
2. The process of claim 1 wherein said first pH adjustment to remove unreacted starting materials and impurities form said solution comprises adding an acid to said solution.
3. The process of claim 1 or claim 2 in which said first pH adjustment is to within a range of pH 4-5 inclusive.
4. The process of claim 2 or claim 3 wherein said acid is a mineral acid or an organic acid.
5. The process of claim 4 wherein said acid is hydrochloric acid or sulfuric acid.
6. The process of any one of claims 1 through 5 further comprising washing said unreacted starting material and other impurities with a water-immiscible solvent. V sst r * 13 27 2 0 5
7. The process of claim 6 wherein said water immiscible solvent is a chlorinated hydrocarbon, aromatic hydrocarbon, or ketone.
8. The process of claims 6 wherein said water-immiscible solvent is dichloromethane, chloroform, or 1,2-dichloroethane.
9. The process of any one of the preceding claims wherein said second pH adjustment to separate ranitidine base from said solution comprises adding a basifying agent to said solution.
10. The process of claim 9 in which said second pH adjustment is to within a range of pH 9-10 inclusive.
11. The process of either claim 9 or claim 10 wherein said basifying agent is an alkali metal carbonate, alkali metal bicarbonate, or alkali metal hydroxide.
12. The process of claim 11 wherein said alkali metal is sodium or potassium.
13. The process of claim 9 or claim 10 wherein said basifying agent is ammonium carbonate, ammonium bicarbonate, or ammonium hydroxide.
14. The process of any one of the preceding claims wherein said organic solvent is a lower alkanol.
15. The process of any one of the preceding claims wherein said organic solvent is a primary alcohol, a secondary alcohol, a tertiary alcohol, a ketone, an ester, a saturated aromatic hydrocarbon, or an unsaturated aromatic hydrocarbon. // * - 14 27 2 0 5 J
16. 16. The process of any one of the preceding claims wherein said solvent is n-propanol, isopropanol, isobutanol, n-butanol, ethylmethyl ketone, 4-methylpentan-2-one, ethyl acetate, n-butyl acetate, toluene, or cyclohexane.
17. 17. The process of any one of the preceding claims further comprising adding an additional organic solvent to complete crystallization of said ranitidine base product.
18. 18. The process of any one of the preceding claims wherein said additional organic solvent is hexane, petroleum ether, toluene, ethyl acetate, or n-butyl acetate.
19. 19. The process of claim 18 wherein said additional organic solvent is hexane or petroleum ether.
20. 20. The process of any one of the preceding claims further comprising dissolving said collected ranitidine base in an additional organic solvent and crystallizing ranitidine base from said additional organic solvent.
21. 21. The process of claim 20 wherein said additional organic solvent is an alkanol.
22. 22. The process of claim 20 wherein said additional organic solvent is a primary alcohol, a secondary alcohol, a tertiary alcohol, a ketone, an ester, a saturated hydrocarbon, or an unsaturated hydrocarbon.
23. 23. The process of any one of claims 20 through 22 further comprising adding a further organic solvent to complete crystallization of said ranitidine base from said additional organic solvent. v . * \ ~9 AUG 19sg f * a 15 272 0 5 3
24. 24. The process of claim 23 wherein said further organic solvent is hexane or petroleum ether.
25. 25. A process substantially as herein described by reference to the accompanying drawings and examples.
26. 26. Pharmaceutical grade ranitidine base prepared by a process as claimed in any one of claims 1 through 24. RANBAXY LABORATORIES LIMITED By its Attorneys 16 t c V £ • -\\ "3 AUG 19 91