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Catalyst, method and uses of dimethyl ether synthesis using coal based synthetic gas in a slurry reactor

A technology of coal-based synthesis gas and catalyst, which is applied in the direction of catalyst activation/preparation, physical/chemical process catalyst, ether preparation, etc. It can solve the problems of high selectivity and low selectivity of dimethyl ether, and achieve uniform particle distribution and pH The value is easy to control and the effect of reducing the occurrence of side reactions

Inactive Publication Date: 2007-05-30
SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, when used in one-step synthesis of dimethyl ether, it shows the disadvantages of relatively low selectivity of product dimethyl ether and relatively high selectivity of by-products such as hydrocarbons.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] Example 1 Weigh 441.3 grams of aluminum nitrate, 109.7 grams of zinc nitrate, and 25.2 grams of manganese nitrate to prepare 0.5M solutions, and mix them together to form a mixed solution A. 172.7 grams of precipitant ammonia water and 172.7 grams of auxiliary urea were also formulated into 0.5M solutions respectively, and mixed together to form B solution. Liquid A and liquid B are fed into the sedimentation tank to precipitate the catalyst at a speed of 12 ml / min under the condition of 60° C. and pH=8. After precipitation, continue to age for 1 hour, filter with suction, dry at 80°C, and roast at 500°C to obtain Al 2 o 3 : 60, ZnO: 30, MnO: 10 catalyst. It is crushed to below 250 mesh and physically mixed with industrial methanol catalyst C301 crushed to below 250 mesh before evaluation. Catalyst evaluation is carried out on a self-made slurry bed evaluation device, and the process conditions are: 280°C, 5.0MPa, 80000h -1 , C301 and dehydration catalyst weight rat...

Embodiment 2

[0022] Example 2 Weigh 588.4 grams of aluminum nitrate, 27.0 grams of zinc acetate, and 25.2 grams of manganese nitrate to form 0.1M solutions, and mix them together to form a mixed solution A. 198.7 grams of precipitant ammonia water and 49.7 grams of auxiliary agent ethylenediamine are also prepared into 0.1M solutions respectively, and mixed together to form B solution. Liquid A and liquid B are fed into the sedimentation tank to precipitate the catalyst at a speed of 15 ml / min under the condition of 80° C. and pH=7. After precipitation, continue to age for 2 hours, filter with suction, dry at 110°C, and roast at 700°C to obtain Al 2 o 3 : 80, ZnO: 10, MnO: 10 catalyst. It is crushed to below 250 mesh and physically mixed with industrial methanol catalyst C301 crushed to below 250 mesh before evaluation. Catalyst evaluation is carried out on a self-made slurry bed evaluation device, and the process conditions are: 260°C, 6.0MPa, 40000h -1 , C301 and dehydration catalyst...

Embodiment 3

[0023] Example 3 272.0 grams of aluminum acetate, 36.6 grams of zinc nitrate, and 50.5 grams of manganese nitrate were weighed to make 1M solutions, and mixed together to form a mixed solution A. 187.1 grams of ammonia water as a precipitant, 31.2 grams of urea as an auxiliary agent, and 31.2 grams of n-butylamine were also prepared into 1M solutions respectively, and mixed together to form liquid B. Liquid A and liquid B are fed into the sedimentation tank to precipitate the catalyst at a speed of 14 ml / min under the condition of 70° C. and pH=9. After precipitation, continue to age for 1.5 hours, filter with suction, dry at 100°C, and roast at 600°C to obtain Al 2 o 3 : 70, ZnO: 10, MnO: 20 catalyst. It is crushed to below 250 mesh and physically mixed with industrial methanol catalyst C301 crushed to below 250 mesh before evaluation. Catalyst evaluation was carried out on a self-made slurry bed evaluation device, and the process conditions were: 320°C, 5.0MPa, 80000h -1...

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PUM

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Abstract

The invention provides a catalyst for synthesizing dimethyl ether from coal-based synthesis gas on slurry bed, which comprises synthetic methanol catalyst C301 and dehydration catalyst by the weight ratio of 1-5:1. The dehydration catalyst comprises Al2O3 60-80%, ZnO 10-30%, MnO 10-30%, and is prepared through precipitation method. The prepared dehydration catalyst has homogeneous particle size distribution and large specific surface area.

Description

technical field [0001] The invention relates to a catalyst for synthesizing dimethyl ether, in particular to a catalyst for synthesizing dimethyl ether from coal-based synthesis gas in a slurry bed, a preparation method and an application. Background technique [0002] Dimethyl ether (DME) is a colorless, non-toxic product with little corrosion, no damage to the atmospheric ozone layer, and is easily degraded in the atmospheric troposphere, so it is called an environmentally friendly compound. [0003] Dimethyl ether is a traditional chemical industrial product with small output and demand. With the development of science, many new uses of dimethyl ether have been discovered, so its demand is also increasing. It can be used as a methylation reagent for the synthesis of medicine, pesticides and dyes; carbonylation to produce methyl acetate and acetic anhydride; it can replace chlorofluorocarbons as aerosol propellants to reduce the damage to the atmospheric ozone layer; it h...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C43/04C07C41/01B01J27/25B01J37/00
Inventor 谭猗生解红娟韩怡卓崔海涛杨彩虹
Owner SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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