US2007112215A1PendingUtilityA1

Method for the separation of pentenenitrile isomers

Assignee: BASF AKTIENGESELLWSCHAFTPriority: Jan 29, 2004Filed: Jan 26, 2005Published: May 17, 2007
Est. expiryJan 29, 2024(expired)· nominal 20-yr term from priority
C07C 253/34C07C 255/07
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Claims

Abstract

A process is described for separating mixtures of isomeric pentenenitriles, in which at least one isomer is removed from the mixture, wherein the separation of the substance mixtures of isomeric pentenenitriles is effected distillatively under reduced pressure.

Claims

exact text as granted — not AI-modified
1 . A process for separating mixtures of isomeric pentenenitriles, in which at least one isomer is depleted from the mixture, which comprises effecting the separation of the mixtures of isomeric pentenenitriles selected from the group consisting of 
 mixtures comprising 2-methyl-3-butenenitrile and 3-pentenenitrile,    mixtures comprising 2-methyl-3-butenenitrile and (Z)-2-methyl-2-butenenitrile,    mixtures comprising cis-2-pentenenitrile and 3-pentenenitrile and    mixtures comprising (E)-2-methyl-2-butenenitrile and 3-pentenenitrile    by distilling under a pressure of from 0.001 to 1 bar.    
   
   
       2 . The process according to  claim 1 , wherein at least two different isomers are separated.  
   
   
       3 . The process according to  claim 1 , wherein the mixture comprises 2-methyl-3-butenenitrile and 3-pentenenitrile and is produced from a reaction of 1,3-butadiene with hydrogen cyanide over a hydrocyanation catalyst.  
   
   
       4 . The process according to  claim 3 , wherein the proportion of 2-methyl-3-butenenitrile in the mixture is from 0.1 to 99.9% by weight, based on the sum of all pentenenitrile isomers in the mixture, and/or the proportion of 3-pentenenitrile in the mixture is from 0.1 to 99.9% by weight, based on the sum of the pentenenitrile isomers in the mixture.  
   
   
       5 . The process according to  claim 1 , wherein the mixture comprises 2-methyl-3-butenenitrile and (Z)-2-methyl-2-butenenitrile and is produced from an isomerization of 2-methyl-3-butenenitrile.  
   
   
       6 . The process according to  claim 5 , wherein the proportion of 2-methyl-3-butenenitrile in the mixture is from 0.1 to 99% by weight, based on the sum of the pentenenitrile isomers in the mixture, and/or the proportion of (Z)-2-methyl-2-butenenitrile in the mixture is from 0.1 to 99% by weight, based on the sum of the pentenenitrile isomers in the mixture.  
   
   
       7 . The process according to  claim 1 , wherein the mixture comprises cis-2-pentenenitrile and 3-pentenenitrile and stems is produced from a reaction of 3-pentenenitrile with hydrogen cyanide over a hydrocyanation catalyst.  
   
   
       8 . The process according to  claim 7 , wherein the proportion of cis-2-pentenenitrile in the mixture is from 0.1 to 99.9% by weight, based on the sum of pentenenitrile isomers in the mixture, and/or the proportion of 3-pentenenitrile in the mixture is from 0.1 to 99.9% by weight, based on the sum of the pentenenitrile isomers in the mixture.  
   
   
       9 . The process according to  claim 1 , wherein the mixture comprises (E)-2-methyl-2-butenenitrile and 3-pentenenitrile and is produced from a reaction of 1,3-butadiene with hydrogen cyanide over a hydrocyanation catalyst or from the isomerization of 2-methyl-3-butenenitrile or from a reaction of 3-pentenenitrile with hydrogen cyanide over a hydrocyanation catalyst.  
   
   
       10 . The process according to  claim 9 , wherein the proportion of 3-pentenenitrile in the mixture is from 0.1 to 99.9% by weight, based on the sum of the pentenenitrile isomers in the mixture, and/or the proportion of (E)-2-methyl-2-butenenitrile in the mixture is from 0.1 to 99.9% by weight, based on the sum of the pentenenitrile isomers in the mixture.  
   
   
       11 . The process according to  claim 2 , wherein the mixture comprises 2-methyl-3-butenenitrile and 3-pentenenitrile and is produced from a reaction of 1,3-butadiene with hydrogen cyanide over a hydrocyanation catalyst.  
   
   
       12 . The process according to  claim 2 , wherein the mixture comprises 2-methyl-3-butenenitrile and (Z)-2methyl-2-butenenitrile and is produced from an isomerization of 2-methyl-3-butenenitrile.  
   
   
       13 . The process according to  claim 2  wherein the mixture comprises cis-2-pentenenitrile and 3-pentenenitrile and is produced from a reaction of 3-pentenenitrile with hydrogen cyanide over a hydrocyanation catalyst.  
   
   
       14 . The process according to  claim 2 , wherein the mixture comprises (E)-2-methyl-2-butenenitrile and 3-pentenenitrile and is produced from a reaction of 1, 3-butadiene with hydrogen cyanide over a hydrocyanation catalyst or from the isomerization of 2-methyl-3-butenenitrile or from a reaction of 3-pentenenitrile with hydrogen cyanide over a hydrocyanation catalyst.

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