US2005070725A1PendingUtilityA1

Process for the preparation of alkylene oxide

Priority: Aug 19, 2003Filed: Aug 19, 2004Published: Mar 31, 2005
Est. expiryAug 19, 2023(expired)· nominal 20-yr term from priority
C07D 301/19C07D 303/04
44
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Claims

Abstract

A process for the preparation of alkylene oxide, which process involves mixing fresh feed containing organic hydroperoxide and alkene with a recycle stream to obtain a reaction mixture containing of from 5 to 80% wt of alcohol, based on total amount of reaction mixture, contacting the reaction mixture with a heterogeneous epoxidation catalyst to obtain a stream containing alkylene oxide and alcohol, and recycling of from 30 to 95% wt of the stream obtained in step (ii) to step (i).

Claims

exact text as granted — not AI-modified
1 . A process for the preparation of alkylene oxide, which process comprises: 
 (i) mixing fresh feed containing organic hydroperoxide and alkene with a recycle stream to obtain a reaction mixture containing from 5% wt to 80% wt of alcohol, based on total amount of reaction mixture;    (ii) contacting the reaction mixture with a heterogeneous epoxidation catalyst to obtain a stream containing alkylene oxide and alcohol; and,    (iii) recycling from 30% wt to 95% wt of the stream obtained in step (ii) to step (i), resulting in a remainder stream and a recycle stream from step (ii).    
     
     
         2 . The process of  claim 1 , which process further comprises 
 (iv) contacting the remainder of the stream obtained in step (ii) with further epoxidation catalyst to obtain a product stream substantially free of organic hydroperoxide.    
     
     
         3 . The process of  claim 1 , in which process the reaction mixture subjected to step (ii) comprises from 3% wt to 25% wt of organic hydroperoxide, from 20% wt to 50% wt of alkene, from 5% wt to 50% wt of alcohol and from 0% wt to 60% wt of further compounds, to a total of 100% wt.  
     
     
         4 . The process of  claim 1 , in which the product stream which is recycled comprises at most 10% wt of organic hydroperoxide.  
     
     
         5 . The process of  claim 1 , in which the reaction mixture subjected to step (ii) contains from 10% wt to 40% wt of alcohol.  
     
     
         6 . The process of  claim 1 , which comprises contacting the reaction mixture with epoxidation catalyst in at least 2 parallel reactors in step (ii).  
     
     
         7 . The process of  claim 1  in which the weight ratio of recycled stream obtained in step (ii) to fresh feed is from 0.5 to 4.  
     
     
         8 . The process of  claim 1 , in which process the alkene is propene.  
     
     
         9 . The process of  claim 1 , in which process the organic hydroperoxide is ethylbenzene hydroperoxide and the alcohol is 1-phenyl ethanol and which process further comprises separating the 1-phenyl ethanol from the product stream and dehydrating the 1-phenyl ethanol using a dehydration catalyst to obtain styrene.  
     
     
         10 . A process for the preparation of propylene oxide which process comprises contacting a mixture containing from 5% wt to 25% wt of organic hydroperoxide, from 30% wt to 50% wt of propene, from 5% wt to 70% wt of alcohol and from 30% wt to 60% wt of further compounds, based on total amount of reaction mixture, to a total of 100% wt, with a heterogeneous epoxidation catalyst to obtain propylene oxide and alcohol.  
     
     
         11 . The process of  claim 10 , in which process the organic hydroperoxide is ethylbenzene hydroperoxide and the alcohol is 1-phenyl ethanol and which process further comprises separating the 1-phenyl ethanol from the product stream and dehydrating the 1-phenyl ethanol using a dehydration catalyst to obtain styrene.

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