US2005033078A1PendingUtilityA1

Method and apparatus for preparing a dialkyl carbonate, and its use in the preparation of diaryl carbonates and polycarbonates

Assignee: POLIMERI EUROPA SPAPriority: Aug 14, 2001Filed: Dec 22, 2003Published: Feb 10, 2005
Est. expiryAug 14, 2021(expired)· nominal 20-yr term from priority
C07C 68/01B01J 19/002B01J 2219/00247B01J 2219/00272B01J 2219/00006C07C 68/00
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Claims

Abstract

Unexpected corrosion of downstream sections of a dialkyl carbonate manufacturing apparatus has been traced to alkyl chloroformate impurities, which slowly decompose to yield hydrochloric acid. An improved process and apparatus for dialkyl carbonate synthesis reduce corrosion by physically removing or chemically decomposing the alkyl chloroformate impurities within the corrosion-resistant upstream sections of the apparatus. The alkyl chloroformate may be decomposed by passing it through a passageway at a temperature of about 30 C to about 130° C. for a time of about 0.5 hour to about 10 hours. The passageway may include one or more holding vessels or a tubular section that promotes plug flow.

Claims

exact text as granted — not AI-modified
1 . A method of preparing a dialkyl carbonate, comprising: reacting an alkanol, oxygen, carbon monoxide, and a catalyst to form a mixture comprising a dialkyl carbonate, an alkyl chloroformate, hydrochloric acid, water, carbon dioxide, and carbon monoxide; separating from the reaction mixture a liquid fraction comprising alkyl chloroformate; and passing said liquid fraction through a fluid passageway at a temperature of about 30° C. to about 130° C. and for a time of about 0.5 hour to about 10 hours; wherein said fluid passageway has a length to diameter ratio of at least about 0.2.  
     
     
         2 . The method of  claim 1 , wherein said alkanol comprises methanol.  
     
     
         3 . The method of  claim 1 , wherein said reacting said alkanol, said oxygen, and said carbon monoxide comprises feeding said alkanol, said oxygen, and said carbon monoxide to a reactor in a molar ratio of (about 0.5 to about 0.7 alkanol):(about 0.04 to about 0.06 oxygen):(about 0.8 to about 1.2 carbon monoxide).  
     
     
         4 . The method of  claim 1 , wherein said catalyst comprises a metal selected from the group consisting of iron, copper, nickel, cobalt, zinc, ruthenium, rhodium, palladium, silver, cadmium, rhenium, osmium, iridium, platinum, gold, mercury, and combinations comprising at least one of the foregoing metals.  
     
     
         5 . The method of  claim 1 , wherein said catalyst comprises copper.  
     
     
         6 . The method of  claim 1 , wherein said catalyst comprises hydrochloric acid.  
     
     
         7 . The method of  claim 1 , wherein said catalyst comprises hydrochloric acid and copper in a molar ratio of about 0.5 to about 1.5.  
     
     
         8 . The method of  claim 1 , wherein said fluid passageway comprises a holding vessel having a length to diameter ratio less than 5.  
     
     
         9 . The method of  claim 1 , wherein said fluid passageway comprises a plurality of holding vessels having a length to diameter ratio less than 5.  
     
     
         10 . The method of  claim 1 , wherein said fluid passageway comprises a section having a length to diameter ratio of at least 5.  
     
     
         11 . The method of  claim 1 , wherein passing said liquid fraction through a fluid passageway comprises passing said liquid fraction through at least one section having a length to diameter ratio of at least about 5 for at least about 50% of the total time spent in said fluid passageway.  
     
     
         12 . The method of  claim 1 , further comprising at least partially condensing said mixture prior to separating said liquid fraction.  
     
     
         13 . The method of  claim 1 , further comprising removing hydrochloric acid from said liquid fraction.  
     
     
         14 . The method of  claim 13 , wherein said removing hydrochloric acid comprises reducing the concentration of said hydrochloric acid to less than about 1×10 −3  moles per liter.  
     
     
         15 . The method of  claim 13 , further comprising vaporizing said liquid fraction before said removing hydrochloric acid.  
     
     
         16 . An apparatus for preparing a dialkyl carbonate, comprising: a reactor for reacting an alkanol, oxygen, carbon monoxide, and a catalyst to produce a mixture comprising a dialkyl carbonate, an alkyl chloroformate, hydrochloric acid, water, carbon dioxide, and carbon monoxide; a gas-liquid separator; and a fluid passageway for removing alkyl chloroformate, wherein said fluid passageway has a length to diameter ratio of at least about 0.2.  
     
     
         17 . The apparatus of  claim 16 , wherein said fluid passageway comprises a holding vessel having a length to diameter ratio less than 5.  
     
     
         18 . The apparatus of  claim 16 , wherein said fluid passageway comprises a plurality of holding vessels having a length to diameter ratio less than 5.  
     
     
         19 . The apparatus of  claim 16 , wherein said fluid passageway comprises a section having a length to diameter ratio of at least about 10.

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