US2011135544A1PendingUtilityA1

Apparatus For The Hydroformylation Of Olefins

Assignee: LG CHEMICAL LTDPriority: May 29, 2007Filed: Jan 17, 2011Published: Jun 9, 2011
Est. expiryMay 29, 2027(~0.8 yrs left)· nominal 20-yr term from priority
C07C 45/50B01J 10/00B01J 2219/0011B01J 19/2465Y02P20/582B01J 4/002C07C 45/78C07B 61/00
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Claims

Abstract

The present invention relates to a method for preparing aldehydes by reacting olefins with a synthesis gas including carbon monoxide and hydrogen, and to an apparatus therefore. More particularly, the present invention relates to a method for preparing aldehydes, characterized by spraying and supplying olefins, synthesis gas including carbon monoxide and hydrogen, and a catalyst composition into an oxo reactor through a nozzle, and to an apparatus therefore. According to the present invention, the hydroformylation efficiency can be improved, thereby obtaining desirable aldehydes with a high yield.

Claims

exact text as granted — not AI-modified
1 .- 12 . (canceled) 
     
     
         13 . An apparatus for the hydroformylation of olefins, comprising an oxo reactor provided with a nozzle which is connected with a venturi; an olefin feed line and a synthesis gas feed line for feeding a synthesis gas including hydrogen and carbon monoxide, which are connected to the nozzle, respectively; a recycling line for supplying the reaction mixture Which is recovered from the oxo reactor, into the nozzle provided in the oxo reactor; a separation line branching off from any position in the recycling line; a catalyst/aldehyde separator connected to the separation line; a catalyst solution feed line connected to any position in the catalyst/aldehyde separator and recycling line; and an aldehyde recovery line which is connected to the catalyst/aldehyde separator. 
     
     
         14 . The apparatus for the hydroformylation of olefins according to  claim 13 , wherein the nozzle is provided at the top portion inside the oxo reactor. 
     
     
         15 . The apparatus for the hydroformylation of olefins according to  claim 13 , wherein the oxo reactor is a venturi-loop reactor. 
     
     
         16 . The apparatus for the hydroformylation of olefins according to  claim 13 , wherein the nozzle has a diameter of 0.1 mm to 100 cm. 
     
     
         17 . The apparatus for the hydroformylation of olefins according to  claim 13 , wherein a circulating pump is provided at any position of the recycling line. 
     
     
         18 . The apparatus for the hydroformylation of olefins according to  claim 13 , wherein a heat exchanger is provided at any position of the recycling line.

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