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Method for production of low carbon alcohol and combined production of natural gas and urea from synthetic gas and coke oven gas

A technology of coke oven gas and low-carbon alcohol, which is applied in chemical instruments and methods, preparation of organic compounds, gas fuel, etc., can solve problems such as hydrogen replenishment, adjust excess production capacity, facilitate product diversification, and promote energy saving and reduction row effect

Active Publication Date: 2015-11-18
SEDIN ENG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The present invention is based on the composition of coke oven gas with more hydrogen and less carbon, while the synthesis gas has more carbon and less hydrogen and contains a large amount of CH 4 The characteristics of the two complement each other to meet the hydrogen-to-carbon ratio for the synthesis of low-carbon alcohols, so as to solve the shortcomings of carbon supplementation in the production of low-carbon alcohols using coke oven gas alone or the need for hydrogen supplementation in the production of low-carbon alcohols from syngas alone, and Can by-produce LNG (liquefied natural gas) or CNG (compressed natural gas)

Method used

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  • Method for production of low carbon alcohol and combined production of natural gas and urea from synthetic gas and coke oven gas

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0039] Feed raw coal, water vapor and oxygen from the air separation unit into the gasifier to obtain crude synthesis gas, then pass the crude synthesis gas and coke oven gas into the gas cabinet to fully mix to form a hydrogen-carbon molar ratio that satisfies the low-carbon alcohol synthesis. 2 Raw material gas with / CO=3.6.

[0040] The raw material gas is compressed to 3.5MPa and enters the low-temperature methanol washing and purification device to remove impurities such as hydrogen sulfide and carbon dioxide. 2 S off to less than 0.1ppm, CO 2 Less than 20ppm, the hydrogen sulfide H removed 2 S desulfurization recovery, the removed carbon dioxide through CO 2 Purification by steam stripping.

[0041] The raw material gas washed and purified by low-temperature methanol enters the methane separation, and the methane in the crude gas is separated to obtain LNG at a temperature of -162°C and a pressure of 3.5Mpa by using the cryogenic separation technology of American Chem...

Embodiment 2

[0046] Feed raw coal, water vapor and oxygen from the air separation unit into the gasifier to obtain crude synthesis gas, then pass the crude synthesis gas and coke oven gas into the gas cabinet to fully mix to form a hydrogen-carbon molar ratio that satisfies the low-carbon alcohol synthesis. 2 Raw material gas with / CO=2.9.

[0047] The raw material gas is compressed to 5.0MPa and enters the low-temperature methanol washing and purification device to remove impurities such as hydrogen sulfide and carbon dioxide. 2 S off to less than 0.1ppm, CO 2 Less than 20ppm, the hydrogen sulfide H removed 2 S desulfurization recovery, the removed carbon dioxide through CO 2 Purification by steam stripping.

[0048] The raw material gas washed and purified by low-temperature methanol enters the methane separation, and the methane in the crude gas is separated to obtain LNG at a temperature of -165°C and a pressure of 5.0Mpa by using the cryogenic separation technology of American Chem...

Embodiment 3

[0053] Feed raw coal, water vapor and oxygen from the air separation unit into the gasifier to obtain crude synthesis gas, then pass the crude synthesis gas and coke oven gas into the gas cabinet to fully mix to form a hydrogen-carbon molar ratio that satisfies the low-carbon alcohol synthesis. 2 Raw material gas with / CO=4.1.

[0054] The raw material gas is compressed to 4.5MPa and enters the low-temperature methanol washing and purification device to remove impurities such as hydrogen sulfide and carbon dioxide. 2 S off to less than 0.1ppm, CO 2 Less than 20ppm, the hydrogen sulfide H removed 2 S desulfurization recovery, the removed carbon dioxide through CO 2 Purification by steam stripping.

[0055] The raw material gas washed and purified by low-temperature methanol enters methane separation, and the methane in the gas is separated by supercritical gas extraction and separation technology at a pressure of 4.5MPa and a temperature of -77°C to obtain CNG (compressed na...

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Abstract

A method for production of low carbon alcohol and combined production of natural gas and urea from synthetic gas and coke oven gas comprises the following steps: mixing crude synthetic gas with coke oven gas to form raw gas with a hydrogen / carbon ratio meeting low carbon alcohol synthesis; carrying out low temperature methanol washing on the raw gas, carrying out desulfurizing recovery on removed hydrogen sulfide, and carrying out CO2 stripping on removed carbon dioxide to realize purification; carrying out methane separation on the low temperature methanol washed raw gas, preparing LNG or CNG by using the removed methane, carrying out a low carbon alcohol synthesis reaction on methane separated purified gas, carrying out PSA separation on the obtained gas as a purge gas, returning separated gases mainly comprising CO, CO2 and CH4 to the low temperature methanol washing, and carrying out an ammonia synthesis reaction on separated H2 and N2 obtained after air separation to prepare synthetic ammonia; carrying out a urea synthesis reaction on purified CO2 and the synthetic ammonia to prepare a urea product; and carrying out low carbon alcohol separation on obtain liquid phase products to obtain a low carbon alcohol product. The method improves the utilization rate of the raw gas.

Description

technical field [0001] The invention belongs to a method for synthesizing low-carbon alcohol, in particular to a method for producing low-carbon alcohol from synthesis gas and coke oven gas and co-producing natural gas and urea. Background technique [0002] Low carbon alcohol usually refers to the mixture of C1~C5 alcohols. The application prospect is very wide: low-carbon alcohol can be used as an alternative fuel, although its calorific value is low, it is fully combusted and emits less CO, NOx, hydrocarbons, etc. during combustion, which is an environmentally friendly fuel; low-carbon alcohol It can also be used as a fuel additive. The currently used gasoline additive methyl tert-butyl ether will eventually be banned with the advancement of technology due to problems such as storage and transportation, which provides an opportunity for the development of low-carbon alcohols. Moreover, the low-carbon alcohol has a high octane number, and has good explosion-proof and sho...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C273/04C07C31/04C07C31/08C07C31/10C07C31/12C07C29/151C10L3/08
Inventor 曹会博马英民李晓王贵王军亭
Owner SEDIN ENG
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