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A kind of method for directly preparing dimethylamine from synthesis gas

A synthesis gas and dimethylamine technology, which is applied in the preparation of amino compounds, chemical instruments and methods, and the preparation of hydroxyl compounds, can solve the problems of high proportion of trimethylamine and low selectivity of dimethylamine, and achieve low catalyst cost , Improve the selectivity of dimethylamine, the effect of simple synthesis

Active Publication Date: 2022-07-26
ZHEJIANG UNIVERSITY OF SCIENCE AND TECHNOLOGY
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  • Claims
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AI Technical Summary

Problems solved by technology

[0004] Baiker et al. adopt Cu / Al 2 o 3 Catalyst at 0.6MPa, 200-300℃, CO / H 2 / NH 3 =1 / 1 / 3 Under the reaction conditions, methylamine can be directly synthesized, wherein Cu is the catalyst for hydrogenation of synthesis gas to methanol, and acidic Al 2 o 3 As a catalytic methanol ammoniation catalyst (Journal of the Chemical Society, Chemical Communications, 1995, 1, 73-74), but due to Al 2 o 3 The disordered nature of the pores has no shape-selective catalytic effect on the product, resulting in a significantly higher proportion of trimethylamine in the product and a lower selectivity of dimethylamine

Method used

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  • A kind of method for directly preparing dimethylamine from synthesis gas
  • A kind of method for directly preparing dimethylamine from synthesis gas
  • A kind of method for directly preparing dimethylamine from synthesis gas

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preparation example Construction

[0044] And, the preparation method of described methanol catalyst, comprises the following steps:

[0045] (1) The copper salt, zinc salt and aluminum salt are adjusted according to CuO: 30-60%, ZnO: 30-60%, Al 2 O 3 : 5-10% metal molar ratio is configured into mixed salt solution, and copper salt solution and zinc salt solution are one or more of hydrochloride solution, nitrate solution and acetate solution;

[0046] (2) The mixed salt solution and the precipitating agent are reacted, the pH value of the solution is 8-10, the precipitation temperature is 40-80 °C, and the precipitating agent is Na 2 CO 3 , NaHCO 3 One or more of , NaOH and urea;

[0047] (3) After the precipitate is separated from the mother liquor, the precipitate is repeatedly washed with deionized water, the temperature of the deionized water is 40-60 ° C, and then dried and roasted in the air, the drying temperature is 90-120 ° C, and the drying time is 12- 24h, the calcination temperature is 300-500...

Embodiment 1

[0058] Methanol catalyst CuZnAl synthesis: Weigh 10.87g of copper nitrate trihydrate, 13.38g of zinc nitrate hexahydrate and 3.75g of aluminum nitrate nonahydrate, put them into a beaker containing 200mL, keep at 60°C, and take this solution as solution A. Dissolve 9.54 g of sodium carbonate solution in 100 mL of deionized water, and use this solution as solution B. The solution B was slowly added dropwise to the solution A, while vigorously stirring, the temperature was maintained at 60°C, and the pH in the system was controlled at about 8.6 by the rate of addition of the sodium carbonate solution. After the precipitation was completed, it was aged at room temperature overnight, filtered, washed with deionized water at 60 °C for 5 times until the filtrate was neutral, and finally dried at 120 °C for 6 hours, and calcined at 350 °C for 5 hours in a muffle furnace to obtain CuZnAl methanol catalyst, CuZnAl The molar ratio is 45:45:10, and the XRD pattern of the CuZnAl sample is...

Embodiment 2

[0060] Synthesis of HZSM-5 catalyst: Weigh 4.87g of silica, 0.48g of boehmite, 0.28g of sodium hydroxide, and 0.25g of tetrapropylammonium bromide, add them to an agate mortar, grind for 5-10min, and then add them to In a hydrothermal kettle, crystallize at 200°C for 16h. After crystallization, cool to room temperature in an ice-water bath, repeatedly wash with deionized water until neutral, and dry at 120°C overnight to obtain NaZSM-5 molecular sieve. The NaZSM-5 powder was added to a 1M ammonium nitrate aqueous solution with a solid-liquid mass ratio of 1:10, vigorously stirred, and ion exchanged at 80 °C. This process was repeated three times. After filtration, the powder was dried at 120 °C for 6 hours. Finally, it was calcined in air at 500 °C for 5 h to obtain HZSM-5 molecular sieve. The XRD pattern of the ZSM-5 sample is as follows image 3 shown.

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Abstract

The invention relates to a method for directly preparing dimethylamine from synthesis gas, which is characterized in that: the method comprises two series reactions of synthesis gas-to-methanol reaction and methanol ammoniation reaction, wherein the reaction catalyst is composed of methanol catalyst and methylamine catalyst , the method is carried out in a continuous fixed-bed reactor, the reaction temperature is 200-400 ° C, the pressure is 0.1-5 MPa, and the raw gas volume ratio is H 2 / CO / NH 3 =1-3:1:1-3, the mass ratio of the methanol catalyst and the methylamine catalyst is 1:0.5-5, and the present invention realizes the reaction of directly producing dimethylamine from the synthesis gas by a one-step method by coupling the methanol catalyst and the methylamine catalyst. By designing a series catalyst composed of CuZnAl and core-shell structure composite molecular sieve, it has the advantages of simple synthesis, low catalyst cost, low equipment investment, etc., and the selectivity of dimethylamine in the product is significantly improved.

Description

technical field [0001] The invention belongs to the field of chemical synthesis, and relates to a tandem catalytic synthesis reaction technology, in particular to a multifunctional composite catalyst, in particular to a method for directly preparing dimethylamine from synthesis gas. Background technique [0002] Methylamine is an important organic chemical raw material, widely used in pharmaceuticals, pesticides, solvents, templates and other industries, and has a wide range of uses. At present, methanol and ammonia gas-phase catalytic method is used to synthesize methylamine in industry. However, due to the control of thermodynamic equilibrium, the equilibrium composition of monomethylamine / dimethylamine / trimethylamine is 23 / 27 / 50 (mass ratio), of which dimethylamine It has the largest market demand, accounting for more than 80%, and it is an important raw material for generating dimethylformamide solvent. [0003] my country is rich in coal resources, and the production o...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C209/16C07C211/04C07C29/154C07C31/04B01J23/80B01J37/03B01J29/85B01J29/83
CPCC07C209/16C07C29/154B01J23/80B01J23/002B01J37/031B01J29/005B01J2523/00B01J29/85B01J29/83B01J29/40B01J29/65C07C211/04C07C31/04B01J2523/17B01J2523/27B01J2523/31Y02P20/52
Inventor 邢闯李明权张桂华童明亮王佳元吕鹏杨瑞芹
Owner ZHEJIANG UNIVERSITY OF SCIENCE AND TECHNOLOGY
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