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Hydroformylation method, reaction device and reaction system using same

A reaction device, the technology of chemical reaction, applied in the field of reaction system, hydroformylation reaction device

Pending Publication Date: 2019-08-27
SHANGHAI HUAYI GRP CO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Therefore, although the introduction of the jet gas-liquid reactor has improved the efficiency of the hydroformylation reaction, there is room for further improvement of this method

Method used

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  • Hydroformylation method, reaction device and reaction system using same
  • Hydroformylation method, reaction device and reaction system using same
  • Hydroformylation method, reaction device and reaction system using same

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0080] use figure 2 Shown two-stage jet flow reactor, selects propylene to be the olefin raw material to test, catalyst rhodium concentration 80ppm, ligand is the composition of three (o-methylphenyl) phosphorus L0 and L4, wherein the mole of Rh:L0:L4 The ratio is 1:10:4, the temperature of the reactor is maintained at 90°C, and the reaction pressure is at 1.6MPa. The effective reaction liquid volume of the reaction kettle 100 is 10L, which is divided into two cavities of equal volume, and an injector 200A and 200B are respectively arranged on the top of each cavity. The diameter of the spray expansion tube is 14mm, and the length of the spray tube is 400mm.

[0081] In this embodiment, the propylene feed 101A is 1.6kg / h, 101B is 0.4kg / h, the synthesis gas 102A is 1720NL / h, the synthesis gas 102B is 420NL / h, the volume flow rate of the circulation 203 is 150L / h, and the gas circulation The quantities are all displayed as 175L / h. The output rate of butyraldehyde is 3.40kg / h...

Embodiment 2

[0084] use figure 2 Shown two-stage jet flow reactor, selects propylene to be the olefin raw material to test, catalyst rhodium concentration 80ppm, ligand is the composition of three (o-methylphenyl) phosphorus L0 and L5, wherein the mole of Rh:L0:L5 The ratio is 1:10:4, the temperature of the reactor is maintained at 90°C, and the reaction pressure is at 1.6MPa. The effective reaction liquid volume of the reaction kettle 100 is 10L, which is divided into two cavities of equal volume, and an injector 200A and 200B are respectively arranged on the top of each cavity. The diameter of the spray expansion tube is 14mm, and the length of the spray tube is 400mm.

[0085] In this embodiment, the propylene feed 101A is 1.6kg / h, 101B is 0.4kg / h, the synthesis gas 102A is 1720NL / h, the synthesis gas 102B is 420NL / h, the volume flow rate of the circulation 203 is 150L / h, and the gas circulation The quantities are all displayed as 175L / h. The output rate of butyraldehyde is 3.41kg / h...

Embodiment 3

[0087] use figure 2 Shown two-stage jet flow reactor, select propylene to be the olefin raw material to test, catalyst rhodium concentration 80ppm, ligand is the composition of three (o-methylphenyl) phosphorus L0 and monophosphite L7, wherein Rh:L0 The molar ratio of :L7 is 1:10:4, the temperature of the reactor is maintained at 90°C, and the reaction pressure is at 1.6MPa. The effective reaction liquid volume of the reaction kettle 100 is 10L, which is divided into two cavities of equal volume, and an injector 200A and 200B are respectively arranged on the top of each cavity. The diameter of the spray expansion tube is 14mm, and the length of the spray tube is 400mm.

[0088] In this embodiment, the propylene feed 101A is 1.6kg / h, 101B is 0.4kg / h, the synthesis gas 102A is 1720NL / h, the synthesis gas 102B is 420NL / h, the volume flow rate of the circulation 203 is 150L / h, and the gas circulation The quantities are all displayed as 175L / h. The output rate of butyraldehyde ...

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Abstract

The invention discloses a hydroformylation method, a reaction device and a reaction system using the same. The reaction device comprises a horizontal reactor, chamber body outlets, distribution platesand circulating pipes, wherein the interior of the reactor is partitioned into multiple chamber bodies by one or more partition plates; the upper fluid of each chamber body is communicated with eachother; each chamber body comprises a reversed self-aspirated injector mounted at the top of each chamber body; each reversed self-aspirated injector comprises a nozzle, a gas suction section, a mixingsection and a diffusion section, wherein the gas suction section, the mixing section and the diffusion section are connected with a fluid, the nozzle is formed in the gas suction section, the gas suction section is communicated with a raw material gas source fluid and communicated with the fluid above the liquid phase line of each chamber body; the chamber body outlets are formed in the lower parts of the chamber bodies and used for discharging reaction mixtures; the distribution plates are mounted in the chamber bodies and used for changing raw material gas flowing between the reversed self-aspirated injectors and the chamber body outlets; the circulating pipes are used for recovering the reaction mixtures from the chamber body outlets and then supplying the reaction mixtures to the nozzles of the reversed self-aspirated injectors; and the reactor further comprises a liquid loop pipeline used for enabling partial solution, containing a catalyst, output by the last chamber body to becirculated into the first chamber body.

Description

technical field [0001] The present invention relates to a hydroformylation reaction device and a reaction system using the device. Specifically, it relates to a reaction device for preparing aldehyde by carbonylation of olefin and synthesis gas. By adopting the method and the reaction system of the invention, the reaction efficiency can be improved, equipment investment can be reduced, and the economic benefit is high. Background technique [0002] Olefin carbonyl reaction is an important organic synthesis reaction, which plays a pivotal role in modern industry. The product aldehyde is a very useful chemical intermediate, which can synthesize a variety of important chemical and chemical products. It is the largest homogeneous catalytic reaction process in production scale so far. [Trzeciak, A.M.; Ziólkowski, J.J. Coord. Chem. Rev. 1999, 190-192, 883-900.]. [0003] The main methods for producing aldehydes from olefin carbonyls include low-pressure rhodium-catalyzed carbon...

Claims

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Application Information

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IPC IPC(8): B01J19/26B01J4/00B01J10/00B01J19/00C07C45/50C07C47/02
CPCB01J19/26B01J19/0053B01J19/0013B01J10/00B01J4/002B01J4/008C07C45/50B01J2204/002B01J2204/005B01J2204/007C07C47/02
Inventor 马利群易明武赖春波费利江杨旭石高山林范曼曼马建学
Owner SHANGHAI HUAYI GRP CO
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