US2002082439A1PendingUtilityA1

Process and catalyst for making dialkyl carbonates

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Assignee: CATALYTIC DISTILLATION TECHPriority: Jun 12, 2000Filed: Dec 10, 2001Published: Jun 27, 2002
Est. expiryJun 12, 2020(expired)· nominal 20-yr term from priority
Inventors:J. Yong RyuAbraham P. Gelbein
Y02P20/10C07C 68/00
45
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Claims

Abstract

A process for producing dialkyl carbonates, such as dimethyl carbonate, from the reaction of a primary alcohol with urea in the presence of a catalyst which is a complex compound represented by R 2 Sn(OCH 3 ) 2 ·χL, wherein R=C n H 2n+1 , n=1 to 12, χ=1 or 2, and L is oxygen atom containing organic complexing agent which is carried out by conducting the reaction continuously under reactive distillation conditions wherein the product DMC is stripped from the reaction mixture with methanol and further including the recovery of product dimethyl carbonate (DMC) made in the process by contacting a stream containing the DMC, such as a azeotropic mixture with methanol, with diethyl oxylate under conditions of extractive distillation to selectively separate the DMC from methanol.

Claims

exact text as granted — not AI-modified
The invention claimed is:  
     
         1 . A process for the production of dialkyl carbonates comprising the steps of: 
 (a) feeding urea and a primary alcohol to a reaction zone;    (b) feeding a complex compound represented by R 2 Sn(OCH 3 ) 2 ·χL, wherein R=C n H 2n+1 , n=1 to 12, χ=1 or 2, and L is oxygen atom containing organic complexing agent; and    (c) concurrently in said reaction zone 
 (i) reacting a portion of the primary alcohol and urea in the presence of said organotin compound and said high boiling electron donor atom containing solvent to produce dialkyl carbonate;  
 (ii) removing the dialkyl carbonate and ammonia from said reaction zone as vapor and  
 (iii) contacting said vapor from step (c)(ii) with DEOX under conditions of extractive distillation to selectively extract dialkyl carbonate.  
   
     
     
         2 . The process according to  claim 1  wherein ammonia and a portion of said alcohol are removed from said reaction zone as vapor and withdrawn along with said dialkyl carbonate as overheads.  
     
     
         3 . The process according to  claim 2  wherein said overheads are partially condensed to separate said ammonia as a vapor from said dialkyl carbonate and said alcohol as a liquid.  
     
     
         4 . The process according to  claim 1  wherein said R 2 Sn(OCH 3 ) 2  is dibutyltin dimethoxide.  
     
     
         5 . The process according to  claim 1  wherein said R 2 Sn(OCH 3 ) 2  compound comprises dibutyltin dimethoxide.  
     
     
         6 . The process according to  claim 1  wherein L comprises triethylene glycol dimethyl ether.  
     
     
         7 . The process according to  claim 1  wherein said R 2 Sn(OCH 3 ) 2  comprises dibutyltin dimethoxide and L comprises triethylene glycol dimethyl ether.  
     
     
         8 . The process according to  claim 1  wherein said R 2 Sn(OCH 3 ) 2  comprises dibutyltin dimethoxide and L comprises diethylene glycol dimethyl ether.  
     
     
         9 . The process according to  claim 1  wherein said primary alcohol comprises methanol and said dialkyl carbonate comprises dimethyl carbonate.  
     
     
         10 . A process for recovering DMC from mixtures comprising contacting a DMC containing stream with DEOX under conditions of extractive distillation to selectively extract DMC into said DEOX.  
     
     
         11 . The process according to  claim 10  wherein said DMC containing stream contains methanol.  
     
     
         12 . The process according to  claim 10  wherein said DMC containing stream has previously been treated to remove NH 3  by fractionation.  
     
     
         13 . The process according to  claim 10  wherein said DMC containing stream is vapor phase.  
     
     
         14 . A homogeneous catalyst useful for reacting urea and primary alcohols to produce dialkyl carbonates comprising a complex represented by R 2 Sn(OCH 3 ) 2 ·χL, wherein R=C n H 2n+1 , n=4 to 12, χ=1 or 2, and L is oxygen atom containing organic complexing agent.  
     
     
         15 . The catalyst according to  claim 14  wherein said R 2 Sn(OCH 3 ) 2  comprises dibutyltin dimethoxide.  
     
     
         16 . The catalyst according to  claim 15  wherein said L comprises triethylene glycol dimethyl ether.  
     
     
         17 . The catalyst according to  claim 15  wherein L comprises triethylene glycol dimethyl ether

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