US2013006014A1PendingUtilityA1

Preparation of Methionine or Selenomethionine from Homoserine via a Lactone Intermediate

Assignee: NOVUS INT INCPriority: Mar 9, 2010Filed: Aug 30, 2012Published: Jan 3, 2013
Est. expiryMar 9, 2030(~3.6 yrs left)· nominal 20-yr term from priority
C07D 265/10C07C 319/14C07C 321/08C07C 391/00
56
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Claims

Abstract

Provided herein are processes for the production of methionine or selenomethionine from homoserine. In particular, the processes proceed via the production of lactone intermediates.

Claims

exact text as granted — not AI-modified
1 . A process for preparing a compound comprising Formula (III) or a pharmaceutically acceptable salt thereof, the process comprising:
 a. contacting a compound comprising Formula (I) with an acyl donor comprising R to form a compound comprising Formula (IIb):   b. contacting the compound comprising Formula (IIb) with a compound comprising MeZ to form a compound comprising Formula (IIIb): and   c. contacting the compound comprising Formula (IIIb) with a deacylating agent to form the compound comprising Formula (III) or pharmaceutically acceptable salt thereof:   
       
         
           
           
               
               
           
         
         wherein:
 the compound comprising MeZ is an alkali metal methaneselenoate or methyl selenol; 
 Me is methyl; 
 R is chosen hydrogen, hydrocarbyl, and substituted hydrocarbyl; and 
 Z is selenium. 
 
       
     
     
         2 . The process of  claim 1 , wherein R is chosen from hydrogen, alkyl, alkene, alkoxy, aryl, substituted alkyl, substituted alkene, substituted alkoxy, and substituted aryl. 
     
     
         3 . The process of  claim 1 , wherein the acyl donor is chosen form an acyl halide, an acid anhydride, and a carbamate; and the molar ratio of the compound comprising Formula (I) to the acyl donor is from about 1:0.5 to about 1:10. 
     
     
         4 . The process of  claim 1 , wherein the reaction of step (a) further comprises a proton donor chosen from HCl, HBr, HI, HClO 3 , HClO 4 , HBrO 4 , HIO 3 , HIO 4 , HNO 3 , H 3 PO 4 , poly H 3 PO 4 , H 2 SO 4 , MeSO 3 H, CF 3 SO 3 H, and p-toluene sulfonic acid; and, optionally, further comprises a catalyst 
     
     
         5 . The process of  claim 1 , wherein the molar ratio of the compound comprising Formula (IIb) to the alkali metal methaneselenoate or methyl selenol is from about 1:0.5 to about 1:5. 
     
     
         6 . The process of  claim 1 , wherein the deacylating agent is a proton acceptor chosen from an alkali metal hydroxide, an alkaline earth metal hydroxide, a alkali metal carbonate, an amide, and a hydride; or the deacylating agent is a proton donor chosen from HCl, HBr, HI, HClO 3 , HClO 4 , HBrO 4 , HIO 3 , HIO 4 , HNO 3 , H 2 SO 4 , MeSO 3 H, CF 3 SO 3 H, and p-toluene sulfonic acid. 
     
     
         7 . The process of  claim 1 , wherein steps (a)-(c) are conducted in the presence of a solvent at a temperature of about 20° C. to about 100° C. and at ambient pressure; the solvent being chosen from an aprotic solvent, a protic solvent, and combinations thereof; and the molar ratio of the solvent to the compound comprising Formula (I) is from about 1:1 to about 50:1. 
     
     
         8 . The process of  claim 1 , wherein the compound comprising Formula (III) has an L configuration, a D configuration, or mixture thereof. 
     
     
         9 . The process of  claim 1 , wherein R is ethoxy; the acyl donor is chloroformate; the proton donor is hydrochloric acid; the compound comprising MeZ is lithium methyl selenide, and the deacylating agent is sodium hydroxide. 
     
     
         10 . A process for preparing a compound comprising Formula (III) or a pharmaceutically acceptable salt thereof, the process comprising:
 a. contacting a compound comprising Formula (I) with a proton donor (HX) to form a compound comprising Formula (II); and   b. contacting the compound comprising Formula (II) with a compound comprising MeZ to form the compound comprising Formula (III) or pharmaceutically acceptable salt thereof:   
       
         
           
           
               
               
           
         
         wherein:
 the compound comprising MeZ is chosen from an alkali metal methaneselenoate and methyl selenol; 
 Me is methyl; 
 X is an anion; and 
 Z is selenium. 
 
       
     
     
         11 . The process of  claim 10 , wherein the proton donor is chosen from HCl, HBr, HI, HClO 3 , HClO 4 , HBrO 4 , HIO 3 , HIO 4 , HNO 3 , H 2 SO 4 , MeSO 3 H, CF 3 SO 3 H, and p-toluene sulfonic acid; and the molar ratio of the compound comprising Formula (I) to the proton donor is from about 1:0.1 to about 1:10. 
     
     
         12 . The process of  claim 10 , wherein the step (a) is conducted in the presence of a protic solvent chosen from water, a C 104  alcohol, and combinations thereof; the molar ratio of the solvent to the compound comprising Formula (I) is from about 1:1 to about 50:1; and the reaction is conducted at a temperature from about 50° C. to about 150° C. 
     
     
         13 . The process of  claim 10 , wherein the molar ratio the compound comprising Formula (II) to the alkali metal methaneselenoate is from about 1:0.5 to about 1:10; the reaction is conducted in the presence a solvent chosen from an aprotic solvent, a protic solvent, and combinations thereof; the molar ratio of the solvent to the compound comprising Formula (II) is from about 1:1 to about 50:1; and the reaction is conducted at a temperature from about 20° C. to about 200° C., at ambient pressure, and under an inert gas chosen from nitrogen and argon. 
     
     
         14 . The process of  claim 10 , wherein the molar ratio the compound comprising Formula (II) to methyl selenol is from about 1:10 to about 1:150; the reaction is conducted in the presence of a solvent chosen from a protic solvent, an aprotic solvent, an organic solvent, and combinations thereof; the molar ratio of the solvent to the compound comprising Formula (IIa) is from about 1:1 to about 50:1; and the reaction is conducted at a temperature from about 20° C. to about 200° C., at ambient pressure, and under an inert gas chosen from nitrogen and argon. 
     
     
         15 . A process for preparing a compound comprising Formula (III) or a pharmaceutically acceptable salt thereof, the process comprising:
 a. contacting a compound comprising Formula (I) with a first proton donor (HX) to form a compound comprising Formula (II);   b. contacting the compound comprising Formula (II) with RC(O)R′ to form a compound comprising Formula (IIa);   c. contacting the compound comprising Formula (IIa) with a compound comprising MeZ to form a compound comprising Formula (IIIa) or a pharmaceutically acceptable salt thereof; and   d. contacting the compound comprising Formula (IIIa) or pharmaceutically acceptable salt thereof with a second proton donor to form the compound comprising Formula (III) or a pharmaceutically acceptable salt thereof:   
       
         
           
           
               
               
           
         
         wherein:
 Me is methyl; 
 R is hydrocarbyl or substituted hydrocarbyl; 
 R′ is hydrogen, hydrocarbyl, or substituted hydrocarbyl; 
 X is an anion; and 
 Z is sulfur or selenium. 
 
       
     
     
         16 . The process of  claim 15 , wherein R is chosen from alkyl, alkene, aryl, substituted alkyl, substituted alkene, and substituted aryl; and R′ is chosen from hydrogen, alkyl, alkene, aryl, substituted alkyl, substituted alkene, and substituted aryl. 
     
     
         17 . The process of  claim 15 , wherein the first proton donor is chosen from HCl, HBr, HI, HClO 3 , HClO 4 , HBrO 4 , HIO 3 , HIO 4 , HNO 3 , H 2 SO 4 , MeSO 3 H, CF 3 SO 3 H, and p-toluene sulfonic acid; and the molar ratio of the compound comprising Formula (I) to the first proton donor is from about 1:0.5 to about 1:5. 
     
     
         18 . The process of  claim 15 , wherein RC(O)R′ is chosen from acetaldehyde, propionaldehyde, benzaldehyde, propionaldehyde, acetophenone, and benzophenone; and the molar ratio of the compound comprising Formula (I) to RC(O)R′ is from about 1:0.1 to about 1:10. 
     
     
         19 . The process of  claim 15 , wherein steps (a) and (b) are conducted in the presence a solvent chosen from an aprotic solvent, a protic solvent, an organic solvent, and combinations thereof; the molar ratio of the solvent to the compound comprising Formula (I) is from about 1:1 to about 50:1; and steps (a) and (b) are conducted at a temperature from about 50° C. to about 150° C. 
     
     
         20 . The process of  claim 15 , wherein the compound comprising MeZ is chosen from an alkali metal methanethiolate, an alkali metal methaneselenoate, methyl mercaptan, and methyl selenol. 
     
     
         21 . The process of  claim 20 , wherein the molar ratio of the compound comprising Formula (IIa) to the alkali metal methanethiolate or the alkali metal methaneselenoate is from about 1:0.25 to about 1:5; the reaction is performed in the presence of a solvent chosen from an aprotic solvent, a protic solvent, and combinations thereof; the molar ratio of the solvent to the compound comprising Formula (IIa) is from about 1:1 to about 50:1; and the reaction is conducted at a temperature of about 20° C. to about 200° C., at ambient pressure, and under an inert gas chosen from nitrogen and argon. 
     
     
         22 . The process of  claim 20 , wherein the molar ratio the compound comprising Formula (IIa) to methyl mercaptan or methyl selenol is from about 1:10 to about 1:150; the reaction is performed in the presence of a solvent chosen from an aprotic solvent, a protic solvent, an organic solvent, and combinations thereof; the molar ratio of the solvent to the compound comprising Formula (IIa) is from about 1:1 to about 50:1; and the reaction is conducted at a temperature of about 20° C. to about 200° C., at ambient pressure, and under an inert gas chosen from nitrogen and argon. 
     
     
         23 . The process of  claim 15 , wherein the second proton donor is chosen from HCl, HBr, HI, HClO 3 , HClO 4 , HBrO 4 , HIO 3 , HIO 4 , HNO 3 , H 3 PO 4 , poly H 3 PO 4 , H 2 SO 4 , MeSO 3 H, CF 3 SO 3 H, and p-toluene sulfonic acid; and the molar ratio of the compound comprising Formula (IIIa) to the second proton donor is from about 1:0.5 to about 1:10. 
     
     
         24 . The process of  claim 15 , wherein step (d) is conducted in the presence of a protic solvent; the molar ratio of the solvent to the compound comprising Formula (IIIa) is from about 1:1 to about 50:1; and the reaction is conducted at a temperature of about 20° C. to about 100° C.

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