Method for preparing nonanal by adopting loop reactor and venturi ejector for preparing nonanal

A technology of loop reactor and injector, which is applied in the direction of carbon monoxide reaction preparation, chemical instruments and methods, catalytic reaction, etc., can solve the problems of poor industrial application prospects, stay in the research stage, catalyst loss, etc., and reduce the loss of precious metal rhodium content efficiency, reduce catalyst cost, and increase the effect of interfacial contact

Active Publication Date: 2020-05-19
JIANGSU NUOMENG CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

For practical industrial production, high-cost solvents should be reduced or not used as much as possible, catalysts should be recycled to reduce production costs, and the amplification effect of the process method should be fully considered. Therefore, the industrial application prospects of the above improved methods are poor, and they are still in the research stage. stage
[0006] And due to methods such as "fluorine two-phase", "organic liquid / liquid two-phase", "temperature-controlled phase separation" or ionic liquids, the ultimate goal is to achieve "homogeneous "Phase reaction" will cause the catalyst rhodium to transfer from the catalyst solution during the reaction, so that a certain degree of catalyst loss will occur during "two-phase separation".

Method used

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  • Method for preparing nonanal by adopting loop reactor and venturi ejector for preparing nonanal
  • Method for preparing nonanal by adopting loop reactor and venturi ejector for preparing nonanal
  • Method for preparing nonanal by adopting loop reactor and venturi ejector for preparing nonanal

Examples

Experimental program
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Effect test

Embodiment 1

[0036] In the loop reactor of 5L (reactor volume 5L), add TPPTS and RhCl 3 ·3H 2 The catalyst solution (water phase) formed by dissolving O in water and the reaction raw material 1-octene (organic phase), the volume ratio of the catalyst water phase and the reactant organic phase is controlled to be 1.3:1, and the molar ratio of TPPTS to Rh element is 50 :1, the molar ratio of reactant 1-octene to Rh element is 2000:1. The total volume of materials in the reactor is 4025ml, and the liquid level in the reactor of the loop reactor is 75±2% of the height of the entire reactor.

[0037] Feed synthesis gas (hydrogen to carbon monoxide volume ratio 1:1) into the reactor to a system pressure of 1 MPa, turn on the circulation pump 4 to allow the liquid in the kettle to flow slowly, vent, repeat 6 times to replace the air in the loop reactor, and heat up (heating time About 15 minutes) to the preset reaction temperature of 110°C, immediately fill the synthesis gas to the reaction pre...

Embodiment 2

[0041] In the loop reactor of 5L (reactor volume 5L), add TPPTS and RhCl 3 ·3H 2 The catalyst solution (water phase) formed by dissolving O in water and the reaction raw material 1-octene (organic phase), the volume ratio of the catalyst water phase and the reactant organic phase is 2.1:1, and the molar ratio of TPPTS to Rh element is 70: 1. The molar ratio of reactant 1-octene to Rh element is 1450:1. The total volume of materials in the reactor is 4025ml, and the liquid level in the reactor of the loop reactor is 75±2% of the height of the entire reactor.

[0042] Feed synthesis gas (hydrogen to carbon monoxide volume ratio 1:1) into the reactor to a system pressure of 1 MPa, turn on the circulation pump 4 to allow the liquid in the kettle to flow slowly, vent, repeat 6 times to replace the air in the loop reactor, and heat up (heating time About 15 minutes) to the preset reaction temperature of 90°C, immediately fill the synthesis gas to the reaction pressure of 2.3MPa, a...

Embodiment 3

[0046] In the loop reactor of 5L (reactor volume 5L), add TPPTS and RhCl 3 ·3H 2 The catalyst solution (water phase) formed by dissolving O in water and the reaction raw material 1-octene (organic phase), the volume ratio of the catalyst water phase and the reactant organic phase is 0.7:1, and the molar ratio of TPPTS to Rh element is 28: 1. The molar ratio of reactant 1-octene to Rh element is 2230:1. The total volume of materials in the reactor is 4025ml, and the liquid level in the reactor of the loop reactor is 75±2% of the height of the entire reactor.

[0047] Feed synthesis gas (hydrogen to carbon monoxide volume ratio 1:1) into the reactor to a system pressure of 1 MPa, turn on the circulation pump 4 to allow the liquid in the kettle to flow slowly, vent, repeat 6 times to replace the air in the loop reactor, and heat up (heating time About 15 minutes) to the preset reaction temperature of 90°C, immediately fill the synthesis gas to the reaction pressure of 1.6MPa, a...

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Abstract

The invention discloses a method for preparing nonanal by adopting a loop reactor. According to the method, n-nonanal is prepared through an octene hydroformylation reaction;1-octene, hydrogen and carbon monoxide are used as raw materials, triphenylphosphine tri-m-sulfonic acid sodium salt and rhodium chloride are used as catalysts, and octene hydroformylation reaction is carried out. A water / oil / gas three-phase reaction interface is increased through the loop reactor; the mass transfer rate among reaction raw materials 1-octene, synthesis gas (hydrogen and carbon monoxide) and a catalyst aqueous solution is increased; the conversion rate of the hydroformylation reaction is improved, the design parameters and related process parameters of the core part venturi ejector of the loop reactor are optimized, the conversion rate of octene is further improved, and the selectivity of n-nonanal in the product is improved.

Description

technical field [0001] The invention belongs to the technical field of chemical production, and in particular relates to a method for preparing nonanal by hydroformylation using a new type of reactor equipment—a loop reactor. Background technique [0002] Nonanal is widely used in flavor formulations, often as the top fragrance of aldehyde bases, used to prepare roses, orange blossoms, lily of the valley, peonies, iris, sunflower leaves, sweet oranges, lemons, jasmine, tuberose, parsnips, etc. Fragrance type, nonanal is mainly prepared industrially by dehydrogenation of nonanol. This process has problems such as high production cost, complex process, low product yield, and serious environmental pollution. [0003] Olefin molecules and synthesis gas (CO+H 2 ) Under certain temperature, pressure and catalytic action, aldehydes with one more carbon can be obtained through hydroformylation. The rhodium-based complex homogeneous catalyst can carry out propylene hydroformylatio...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C45/50C07C47/02B05B7/04B01J31/24
CPCC07C45/50B05B7/0425B01J31/2404B01J2231/321B01J2531/822B01J2540/32C07C47/02Y02P20/584
Inventor 梅华蒋流强汪国辉
Owner JIANGSU NUOMENG CHEM
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