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Method for preparing m-phenylenediamine based on continuous catalytic hydrogenation of fixed bed microreactor

A micro-reactor, catalytic hydrogenation technology, applied in the preparation of amino compounds, chemical instruments and methods, preparation of organic compounds, etc., can solve the problems of product purity, increase production cost, long reaction time, etc., and achieve high reaction efficiency. and product yield, reducing the production of azo compounds, the effect of high reaction efficiency

Active Publication Date: 2021-09-24
ZHEJIANG DIBANG CHEM +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, there are following defects in the preparation of m-phenylenediamine by hydrogenation of dinitrochlorobenzene in a hydrogenation kettle: the catalytic hydrogenation reaction of dinitrochlorobenzene is a typical gas-liquid-solid three-phase reaction, and when reacting in a batch kettle, In order to ensure the full contact between the three phases and the full progress of the hydrogenation reaction, high pressure and long reaction time are usually required, and the reaction efficiency is low. At the same time, the low mass transfer and reaction efficiency will lead to azo compounds and non-dechlorination The generation of by-products will have a great impact on the purity of the product. The post-treatment process is complicated, and 5% to 10% of the catalyst needs to be added after each reaction, which greatly increases the production cost.

Method used

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  • Method for preparing m-phenylenediamine based on continuous catalytic hydrogenation of fixed bed microreactor

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0047] Carry out experiment according to the method of the present invention, configure the ethanol solution of 2,4-dinitrochlorobenzene, concentration is 10wt%, the mol ratio of control hydrogen and 2,4-dinitrochlorobenzene is 10:1; Solution and hydrogen are in Mix in the entrance T-type micro-mixer, the gas-liquid mixture that forms passes through the micro-reactor that is packed with palladium-carbon catalyst (catalyst size 50 microns), setting reaction temperature is 90 ℃, reaction pressure 2.5MPa, residence time is 80s, in micro-reactor The reaction product was collected at the outlet of the reactor, and the obtained product was analyzed. The conversion rate of the obtained 2,4-dinitrochlorobenzene was 100%, the yield of m-phenylenediamine was 98.3%, and the azo species was 1.2%. Chlorine substances are 0.4%.

Embodiment 2

[0049] Carry out experiment according to the method of the present invention, configure the methanol solution of 2,6-dinitrochlorobenzene, concentration is 5wt%, add triethylamine according to molar ratio 1:1.2, control hydrogen and 2,6-dinitrochlorobenzene The molar ratio is 8:1; the solution and hydrogen are mixed in the inlet membrane dispersion micro-mixer, and the formed gas-liquid mixture passes through the micro-reactor filled with platinum-carbon catalyst (catalyst size 200 microns), and the reaction temperature is set at 70°C, and the reaction The pressure is 2.0MPa, the residence time is 70s, the reaction product is collected at the outlet of the microreactor, and the resulting product is analyzed. The conversion rate of the obtained 2,6-dinitrochlorobenzene is 100%, and the yield of m-phenylenediamine is 98.7%. , 0.84% ​​for azo substances, and 0.23% for non-dechlorinated substances.

Embodiment 3

[0051] Carry out experiment according to the method of the present invention, configure the tetrahydrofuran solution of 3,5-dinitrochlorobenzene, concentration is 15wt%, add sodium bicarbonate according to molar ratio 1:1.5, control hydrogen and 3,5-dinitrochlorobenzene The molar ratio is 11:1; the solution and hydrogen are mixed in the inlet micro-mesh micro-mixer, and the gas-liquid mixture formed passes through the micro-reactor filled with palladium-carbon catalyst (catalyst size 800 microns), and the reaction temperature is set to 120 ° C. The reaction pressure is 3.0MPa, the residence time is 50s, the reaction product is collected at the outlet of the microreactor, and the resulting product is analyzed. The conversion rate of the obtained 3,5-dinitrochlorobenzene is 100%, and the yield of m-phenylenediamine is 99.4 %, azo substances are 0.14%, and non-dechlorinated substances are 0.33%.

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Abstract

The invention discloses a method for preparing m-phenylenediamine based on continuous catalytic hydrogenation of a fixed bed microreactor, which comprises the following steps: (1) taking dinitrochlorobenzene as a raw material, and dissolving the dinitrochlorobenzene in a solvent to serve as a to-be-hydrogenated substrate solution, wherein the dinitrochlorobenzene is at least one of 2, 4-dinitrochlorobenzene, 2, 6-dinitrochlorobenzene and 3, 5-dinitrochlorobenzene; (2) mixing a to-be-hydrogenated substrate solution and hydrogen in a micro-mixer to form a gas-liquid mixture with a good gas-liquid micro-dispersion state, and then enabling the gas-liquid mixture to enter a micro-packed bed reactor filled with a solid particle catalyst to react, wherein the reaction temperature is 40-160 DEG C, and the pressure is 1-5 MPa, and the retention time of the gas-liquid mixture in the micro-packed bed reactor is 10-120 s; and (3) carrying out gas-liquid separation on a gas-liquid mixture obtained after the reaction is finished, and feeding a liquid product into a subsequent separation and purification system.

Description

technical field [0001] The invention relates to the technical field of preparing m-phenylenediamine, in particular to a method for preparing m-phenylenediamine based on continuous catalytic hydrogenation of a fixed-bed microreactor. Background technique [0002] M-phenylenediamine is an important organic chemical raw material and intermediate, which is widely used in the dye industry in the synthesis of azo dyes, fur dyes, reactive dyes and sulfur dye intermediates, and can also be used to prepare hair dyes, Color developer, petroleum additives and cement coagulant and other materials. M-phenylenediamine can also be synthesized with phthaloyl chloride to prepare high-temperature-resistant aromatic polyamide resin and flame-retardant fiber, which are used in special fields such as national defense and aerospace. At present, the synthesis methods of m-phenylenediamine mainly include iron powder reduction method, electrolytic reduction method and catalytic hydrogenation method...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C209/36C07C209/84C07C211/51
CPCC07C209/36C07C209/84C07C211/51
Inventor 张吉松段笑楠茹恒陈晓栋陈华祥丁亚刚黄振夫徐万福傅伟松
Owner ZHEJIANG DIBANG CHEM
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