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Document Number
US Patent 6723231
Issued Date
April 20, 2004
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Abstract
Process to separate propene from gaseous fluid catalytic cracking products by performing the following steps: a) separating a feed mixture comprising the gaseous products, propene and other saturated and unsaturated hydrocarbons obtained in a fluid catalytic cracking process into a hydrocarbon-rich liquid fraction and a hydrogen containing gaseous fraction, b) separating the hydrogen containing gaseous fraction into a hydrogen-rich gaseous fraction and a hydrocarbon-rich gaseous fraction by means of a membrane separation, c) supplying the hydrocarbon-rich gaseous fraction obtained in step (b) to an absorber section and obtaining in said absorber section a lower boiling fraction rich in gaseous products having a boiling point of ethane or below and supplying the hydrocarbon-rich liquid fraction obtained in step (a) to a stripper section and obtaining in said stripper section a higher boiling fraction comprising propene and hydrocarbons having a boiling point higher than ethane.
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Propene recovery - US Patent 6723231 Drawing
Drawing from US Patent 6723231
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Number of Claims:
7
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Owner
Shell Oil Company (Houston, TX)
Published
April 20, 2004
Application Number
09/980,059
Filed
November 29, 2001
US Classification
208/351   208/347 208/354 208/355 208/358
Int'l Classification
C10G   70/00   (20060101)   C10G   70/04   (20060101)  
Examiner
Assistant Examiner
Priority Data
Jun 03, 1999 [EP] 99304349
USPTO Field of Search
208/347   208/351   208/354   208/355   208/358   585/318  
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