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Reaction system and method for preparing ethanol from coal

A reaction system and ethanol production technology, applied in the field of coal to ethanol, can solve the problems of low production capacity, high temperature, high reaction pressure, etc.

Inactive Publication Date: 2020-10-23
NANJING YANCHANG REACTION TECH RES INST CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, this method has a series of problems such as high reaction pressure, high temperature, high energy consumption, low raw material utilization rate, and low production capacity.

Method used

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  • Reaction system and method for preparing ethanol from coal

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Embodiment

[0070] refer to figure 1 Shown is a specific structural schematic diagram of the coal-to-ethanol reaction system according to the embodiment of the present invention. The reaction system includes two units: a methanol-to-dimethyl ether reaction unit and a dimethyl ether-to-ethanol reaction unit.

[0071] Wherein, the dimethyl ether reaction unit includes: a dimethyl ether reactor 10, a first rectification tower 40, a washing tower 140, and a stripping tower 150, and a part of the raw material methanol is transported by a methanol pump 130 to the dimethyl ether reactor 10, and in addition A part is sent into the scrubber 140 to form a scrubbing solvent in the form of methanol or methanol-water solution in the scrubber 140 to absorb dimethyl ether in the gas phase. After the methanol enters the dimethyl ether reactor 10 for gas phase catalytic dehydration reaction, the reaction product enters the first rectification tower 40 for dimethyl ether purification, and the gas phase at ...

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Abstract

The invention provides a reaction system and method for preparing ethanol from coal. The reaction system comprises a methanol-to-dimethyl ether reaction unit and a dimethyl ether-to-ethanol reaction unit which are connected in order, wherein the methanol is prepared by coal gasification; the methanol-to-dimethyl ether reaction unit comprises a dimethyl ether reactor; methanol is introduced into the dimethyl ether reactor for a gas-phase catalytic dehydration reaction; and the dimethyl ether-to-ethanol reaction unit comprises a carbonylation reactor, a first micro-interface generator is arranged on the outer side of the carbonylation reactor, dimethyl ether separated from the stripping tower and carbon monoxide are introduced into the first micro-interface generator, and the dimethyl etherand the carbon monoxide are dispersed and crushed by the first micro-interface generator and then enter the carbonylation reactor for reaction. According to the reaction system provided by the invention, the energy consumption is reduced, the reaction temperature is reduced, the utilization rate of raw materials is improved, and meanwhile, the productivity is effectively improved.

Description

technical field [0001] The invention relates to the field of coal-based ethanol, in particular to a reaction system and method for coal-based ethanol. Background technique [0002] Worldwide, ethanol production routes include grain fermentation routes, petrochemical routes, and carbon-chemical routes such as coal and natural gas. The grain fermentation route is widely used in the world, and large-scale ethanol production enterprises mostly use the grain fermentation process. Affected by the "food crisis", the country has now stopped approving new corn fuel ethanol projects. The cellulose fuel ethanol project fermented with cassava and corn stalks has poor economic benefits due to factors such as high production costs, over-reliance on state subsidies, and imperfect production technology. The petrochemical route uses ethylene as raw material and produces fuel ethanol through ethylene hydration. my country relies heavily on imports of oil, and the price of ethylene is often...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C29/149C07C29/80C07C31/08C07C67/37C07C69/14C07C41/09C07C41/42C07C43/04
CPCC07C29/149C07C29/80C07C67/37C07C41/09C07C41/42C07C43/043C07C69/14C07C31/08C07C41/58Y02E50/10
Inventor 张志炳周政张锋李磊孟为民王宝荣杨高东罗华勋杨国强田洪舟曹宇
Owner NANJING YANCHANG REACTION TECH RES INST CO LTD