Method of conducting hydroformylation reaction on C4 mixture to prepare aldehydes

A technology of tetrahydroformyl and mixed carbon 4, applied in the direction of carbon monoxide reaction preparation, chemical recovery, organic chemistry, etc., can solve problems such as large differences and achieve the effect of avoiding separation

Pending Publication Date: 2020-03-06
CHINA PETROLEUM & CHEM CORP +1
View PDF8 Cites 1 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] It can be seen from the boiling point of each component in the mixed carbon four that there is a large difference between 2-butene and other components, and 2-butene can be separated from the mixed carbon four by conventional rectification. However, The boiling points of isobutene and 1-butene are very close, and it is difficult to separate isobutene and 1-butene by conventional methods

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Method of conducting hydroformylation reaction on C4 mixture to prepare aldehydes
  • Method of conducting hydroformylation reaction on C4 mixture to prepare aldehydes
  • Method of conducting hydroformylation reaction on C4 mixture to prepare aldehydes

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] The reaction of embodiment 1 is in such as figure 2 and image 3 In the setup shown:

[0042] The first reaction zone consists of two stirred tanks connected in series, and the intermediate separation zone consists of a thin film evaporator and a packed tower. The first catalyst used in the first reaction zone is a rhodium-triphenylphosphine complex catalyst generated in situ by a rhodium compound and triphenylphosphine, the rhodium compound is rhodium acetylacetonate dicarbonyl, and the solvent for dissolving the first catalyst is butyl aldehyde.

[0043] from storage tank ( figure 2 Not shown) mixed butene (composition is 1-butene 36.2wt%, trans-2-butene 0.1wt%, isobutene 55.2wt%, isobutane 8.0wt%, n-butane 0.5wt%) with flow 200g / hr is sent into the pipeline 302 by the pump 503 through the pipeline 301, mixed with the discharge 323 from the bottom of the thin film evaporator 507, and then sent to the bottom of the reactor 501 through the pipeline 303 by the bott...

Embodiment 2

[0053] Embodiment 2 adopts the technique identical with embodiment 1, and the condition of the first reaction zone and intermediate separation zone is identical with embodiment 1, and the difference among embodiment 2 and embodiment 1 is:

[0054] The second catalyst used in the second reaction zone is a rhodium-phosphonite catalyst generated in situ from a rhodium compound and a phosphite, the rhodium compound is rhodium acetylacetonate dicarbonyl, and the phosphonite ligand is 6,6'- [(3,3',5,5'-tetra-tert-butyl-1-1'-biphenyl)2,2'-dioxo]-bis-bibenzo[d,f][1,3,2 ] dioxaphosphapine ring, the solvent used to dissolve the second catalyst is butyraldehyde. In the reactor 601, the rhodium concentration is 200ppm, and the phosphonite ligand concentration is 0.6wt%; in the reactor 602, the rhodium concentration is 200ppm, and the phosphonite ligand concentration is 0.6wt%. The total pressure of the reactor 601 is 1.3MPa, and the temperature is 80°C; the total pressure of the reactor ...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

Provided is a method of conducting a hydroformylation reaction on a C4 mixture to prepare aldehydes. The method includes the steps: S1, in the presence of a first catalyst, the C4 mixture and a syngasmake contact in a first reaction region to be subjected to the hydroformylation reaction, and a first reaction product containing n-valeraldehyde and 2-methylbutyraldehyde is obtained, wherein the C4mixture is composed of 1-butylene and isobutylene and obtained by removing 2-butylene and 1,3-butadiene; S2, separation is conducted on the first reaction product, and a mixture of n-valeraldehyde and 2-methylbutyraldehyde, unreacted raw materials and a material flow which contains the first catalyst are obtained; and S3, in the presence of a second catalyst, the unreacted raw materials and the syngas make contact in a second reaction region to be subjected to the hydroformylation reaction, a second reaction product containing 3-methylbutyraldehyde is obtained, and optionally, the second reaction product is purified. According to the method of conducting the hydroformylation reaction on the C4 mixture to prepare the aldehydes, in a staged reaction mode, 1-butylene and isobutylene are subjected to the hydroformylation reaction separately to obtain different products, and advance separation of 1-butylene and isobutylene is avoided.

Description

technical field [0001] The invention relates to a method for preparing aldehyde by mixed carbon tetrahydroformylation reaction. Background technique [0002] It is a well-known process that olefins and synthesis gas undergo hydroformylation reaction under the action of a catalyst to generate aldehydes with one more carbon atom than olefins. [0003] For olefins without isomers such as ethylene and propylene, the hydroformylation reaction is relatively simple, and for olefins with more than four carbon atoms, because there are different isomers, the hydroformylation of various isomers The reaction conditions are different, and the structure of the product aldehyde is also different. It is difficult to separate the hydroformylation product aldehyde of some isomers. Therefore, for olefins with more than four carbons, it is not suitable to mix olefins with more than four carbons in the same reaction zone. The reaction is carried out simultaneously in the reaction, and it needs ...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Applications(China)
IPC IPC(8): C07C45/50C07C47/02
CPCC07C45/50Y02P20/584
Inventor 陈和朱丽琴包天舒武陈
Owner CHINA PETROLEUM & CHEM CORP
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products