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Synthesis method of multi-element tertiary amine

A synthesis method and technology for polyvalent tertiary amines, which are applied in chemical instruments and methods, preparation of amino compounds, preparation of organic compounds, etc., can solve the problems affecting reaction yield and long reaction time, and achieve high yield and short reaction time. , the effect of less by-products

Active Publication Date: 2021-02-19
JIANGSU FEYMER TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] CN101735068 discloses a kind of with 1,3-propanediol and dimethylamine as raw material, with Cu-Co-Ni / Al 2 o 3 As a catalyst, the method for preparing tetramethylpropylenediamine by mixing and heating with hydrogen produces by-product 3-dimethylaminopropanol, and the conversion rate of tetramethylpropylenediamine is only about 70%; CN110317138 discloses a method based on Paraformaldehyde solution and ethylenediamine are used as raw materials to prepare tetramethylethylenediamine by catalytic hydrogenation. The imine generated by this reaction contains C=N bonds, which are easy to form polymers during the reaction and affect the reaction yield. ; CN109206319 discloses a method for preparing tertiary amines under the action of a catalyst with primary or secondary amines or nitro derivatives and alcohols as raw materials. The reaction of raw materials with low boiling point, the reaction time reaches 24h, and the yield is only about 70%; CN 105481698A discloses a method for the co-production of tetramethylpropylenediamine, which uses protonic acid, Lewis acid or organic carboxylic acid as catalyst , some of the mentioned acids can form salts with amines to affect the catalytic performance, and at the same time obtain difficult high-boilers. At the same time, the reaction time of this method is 3~15h, and the reaction time is long

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] Catalyst preparation: take nano-powders of aluminum silicate, tin oxide, and antimony oxide with a mass ratio of 2:1:1, and disperse nano-powders of calcium silicate, tin oxide, and antimony oxide in a solution with a mass concentration of 1% sodium benzoate. Dispersion liquid, the quality of the dispersion liquid is 5~100 times of the total mass of zinc silicate, tin oxide, and antimony oxide nanopowder; adding molecular sieve to the dispersion liquid, the particle size of the molecular sieve is 100±50 μm, and the dispersion liquid added with molecular sieve is Stir to make the molecular sieve microspheres evenly distributed in the dispersion liquid, and then use an ultrasonic instrument to ultrasonicate the dispersion liquid for 2 hours; filter the ultrasonic dispersion liquid, and place the filtered molecular sieve in a muffle furnace for roasting. The temperature was 750°C, and the calcination time was 2 hours; the loading amount of active components on the loaded ca...

Embodiment 2

[0030] Catalyst preparation: take calcium silicate, tin oxide, and antimony oxide nano-powders with a mass ratio of 3:1:1, and disperse aluminum silicate, tin oxide, and antimony oxide nano-powders in a mass concentration of 1% sodium benzoate solution. Dispersion liquid, the quality of the dispersion liquid is 5~100 times of the total mass of zinc silicate, tin oxide, and antimony oxide nanopowders; add activated alumina microspheres to the dispersion liquid, the particle size of the activated alumina microspheres is 100±50 μm, Stir the dispersion liquid with alumina microspheres, so that the microspheres are evenly distributed in the dispersion liquid, and then use an ultrasonic instrument to ultrasonicate the dispersion liquid for 2 hours, and filter the ultrasonic dispersion liquid, and obtain The microspheres were calcined in a muffle furnace at a temperature of 600°C and a calcining time of 4 hours. The loading rate of the active components of the catalyst after loading w...

Embodiment 3

[0035] The catalyzer that embodiment 2 obtains is filled in the stainless steel 316L microreactor, and wherein the single module liquid holding capacity of microreactor is 300ml, and flow channel cross-section is 8mm 2 .

[0036] The by-product raw materials N,N-dimethyl-1,3-propanediamine, N,N,N'-trimethyl-1,3-propanediamine, N,N,N',N'-tetra Methyl-1,3-propylenediamine and methanol are passed into the reactor, and methanol is added to N,N-dimethyl-1,3-propylenediamine, N,N,N'-trimethyl- The molar ratio of 1,3-propanediamine to methanol is [2n(N,N-dimethyl-1,3-propanediamine)+n(N,N,N'-trimethyl-1,3- Propylenediamine)]: n methanol = 1:1.2, the reaction temperature was controlled at 150°C, the reaction pressure was 3.0MPa, the residence time was 35min, and the reaction conversion rate was tested by gas chromatography to be 92.26%.

[0037] Pass the reacted reaction liquid into the azeotropic rectification system for rectification. The tail gas (dimethyl ether) in the distillat...

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Abstract

The invention discloses a synthesis method of multi-element tertiary amine, wherein the synthesis method comprises the steps: under the action of a catalyst, carrying out methylation reaction on N,N-dimethyl-1,3-propane diamine, N,N,N'-trimethyl-1,3-propane diamine and methanol which serve as reaction raw materials in a microreactor to obtain N,N,N',N'-tetramethyl-1,3-propane diamine, wherein thecatalyst comprises a carrier and an active component loaded on the carrier, the active component is a combination of one or more of aluminum silicate, zinc silicate and calcium silicate and one or twoof tin oxide and antimony oxide. According to the method, N,N-dimethyl-1,3-propane diamine, N,N,N'-trimethyl-1,3-propane diamine and methanol serve as raw materials, the tertiary amine is produced through direct methylation under the catalyst and the microreactor, the reaction route is short, few byproducts are produced, the product is easy to recycle, the reaction time is short, and the conversion rate is high.

Description

technical field [0001] The invention belongs to the technical field of organic synthesis, and specifically relates to a synthesis method of N,N,N',N'-tetramethyl-1,3-propanediamine. Background technique [0002] N,N,N',N'-Tetramethyl-1,3-propylenediamine, referred to as tetramethylpropylenediamine, is used as catalyst for polyurethane foam, microporous elastomer, curing catalyst for epoxy resin, Intermediates for the preparation of quaternary ammonium compounds, etc., have a large market demand. [0003] CN101735068 discloses a kind of with 1,3-propanediol and dimethylamine as raw material, with Cu-Co-Ni / Al 2 o 3 As a catalyst, the method for preparing tetramethylpropylenediamine by mixing and heating with hydrogen produces by-product 3-dimethylaminopropanol, and the conversion rate of tetramethylpropylenediamine is only about 70%; CN110317138 discloses a method based on Paraformaldehyde solution and ethylenediamine are used as raw materials to prepare tetramethylethylene...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C209/16C07C209/84C07C211/11B01J29/00B01J23/18B01J35/08B01J37/34B01J37/08
CPCC07C209/16C07C209/84B01J29/00B01J23/18B01J23/002B01J37/343B01J37/08B01J2523/00B01J35/23B01J35/51C07C211/11B01J2523/23B01J2523/31B01J2523/41B01J2523/43B01J2523/53
Inventor 段立明刘强何国锋李胜兵魏星光王勤秦宝雨
Owner JIANGSU FEYMER TECH