Claims
- 1. A method for preparing a crystalline 3-cyano-2-morpholino-5-(pyrid-4-yl)-pyridine having a high bulk density of from about 220 to about 360 g/l, which comprises precipitating said high bulk density crystaline 3-cyano-2-morpholino-5-(pyrid-4-yl)-pyridine from a crude or purified 3-cyano-2-morpholino-5-(pyrid-4-yl)-pyridine starting material that is
- (a) a solution of said starting material in an inorganic or organic acid, and precipitating with a base, or
- (b) a solution of said starting material in a chlorinated hydrocarbon, and precipitating with an aliphatic hydrocarbon, or
- (c) from an aliphatic ester of an aliphatic carboxylic acid of said starting material, and an aliphatic alcohol.
- 2. The method of claim 1, wherein the starting material is a crude 3-cyano-2-morpholino-5-(pyrid-4-yl)-pyridine.
- 3. The method of claim 1, wherein, after dissolving the starting material, the solution is treated with an adsorbent.
- 4. The method of claim 3, wherein said adsorbent is activated charcoal, or silica gel.
- 5. The method of claim 1, wherein a crystalline, high bulk density 3-cyano-2-morpholino-5-(pyrid-4-yl)-pyridine is precipitated by a base from its acidic solution, at a temperature of from about 15.degree. C. to about 40.degree. C.
- 6. The method of claim 5, wherein the temperature is about 30.degree. C.
- 7. The method of claim 1, wherein the base is a solution of an alkali hydroxide, ammonia, or an alkali carbonate.
- 8. The method of claim 1, wherein the solvent acid is an aqueous solution of a mineral acid, further comprising adding a further amount of the mineral acid to the solution, and precipitating a crystalline 3-cyano-2-morpholino-5-(pyrid-4-yl)-pyridine as the salt of said mineral acid, and separating the precipitate from the aqueous solution.
- 9. The process of claim 8, further comprising redissolving the separated salt of 3-cyano-2-morpholino-5-(pyrid-4-yl)-pyridine in water, and precipitating it with a base.
- 10. The process of claim 9, wherein the redissolved solution in water is treated with an adsorbent prior to precipitation with a base.
- 11. The method of claim 1, wherein a C.sub.5-10 aliphatic hydrocarbon, or a mixture of such hydrocarbons, is used as the precipitating agent.
- 12. The method of claim 1, wherein the chlorinated hydrocarbon is chlorinated aliphatic hydrocarbon.
- 13. The method of claim 11, wherein the chlorinated hydrocarbon is dichloromethane, or chloroform.
- 14. The method of claim 1, wherein the precipitation takes place from an ester of a C.sub.1-3 aliphatic carboxylic acid and a C.sub.1-4 aliphatic alcohol.
- 15. The method of claim 14, wherein said ester is butyl acetate.
- 16. The method of claim 14, wherein the recrystallization is carried out while stirring and cooling rapidly and intensively.
Priority Claims (1)
Number |
Date |
Country |
Kind |
338544 |
Mar 1990 |
DDX |
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Parent Case Info
This is a divisional application of U.S. Ser. No. 665,681, filed on Mar. 7, 1991, now U.S. Pat. No. 5,204,464.
Non-Patent Literature Citations (1)
Entry |
Hagen et al., Chemical Abstracts, vol. 107 (1987) No. 7074p. |
Divisions (1)
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Number |
Date |
Country |
Parent |
665681 |
Mar 1991 |
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