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Method for producing methanol with coke oven gas

A technology for coke oven gas and methanol production, which is applied to chemical instruments and methods, gas fuels, and preparation of hydroxyl compounds. It can solve the problems of large water vapor consumption, pure oxygen, low calorific value of fuel, and huge energy consumption, and achieve economical Benefit improvement, investment reduction, good operating conditions

Active Publication Date: 2015-08-12
ZHONGRONG TECH CORP LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, as a fuel, the calorific value is very low, and the value of the heat used for burning is less than 0.3 yuan / Nm 3 , the waste caused by burning is huge
Second, methane conversion needs to consume a large amount of water vapor and pure oxygen, and an air separation unit needs to be installed, which requires huge investment and huge energy consumption

Method used

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  • Method for producing methanol with coke oven gas
  • Method for producing methanol with coke oven gas
  • Method for producing methanol with coke oven gas

Examples

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Embodiment 1

[0027] Take coke oven gas produced by coke ovens with an annual output of 2 million tons as an example:

[0028] The coke oven gas produced by the coke oven and initially purified by chemical production is 103,400 cubic meters per hour, and the composition is: H 2 58%; CO 6.2%; CO 2 2.2%; CH 4 26%; CnHm2.5%; N 2 4.5%; H 2 S 50mg / Nm 3 ; Organic sulfur 400 mg / Nm 3 ;Calorific value 4288 kcal / Nm 3 (Different coking plants have slightly different changes in coke oven gas composition due to different coal blending), go to the compressor to increase the pressure to 0.8-2.5MPa(g) and send it to the refining device for refining (after refining, H 2 The content of S and total sulfur is less than 0.1PPm, other impurities are 0), the refined high-purity coke oven gas enters the pressure swing adsorption hydrogen extraction device, and 99.99% purity of hydrogen can be extracted according to the extraction rate of 90% 50000Nm 3 / h, for the synthesis of methanol. Tail gas after ...

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Abstract

The invention relates to a production method for preparing methanol from coke oven gas. The device used by the method comprises a coke oven gas refiner, a pressure swing adsorption hydrogen extractor, a pressure swing adsorption methane extractor, a wet-process decarbonizer, a hydrogen / carbon dioxide gas mixture compressor and a methanol synthesis and rectifying unit. The method comprises the following steps: extracting hydrogen, extracting methane, using exhaust after extracting methane as fuel of a coke furnace and chemical production, extracting CO2 from combustion gas obtained by combusting the exhaust in the coke furnace by using the wet-process decarbonizer, mixing the CO2 and H2, pressurizing by the compressor, and producing the methanol through the methanol synthesis and rectifying unit. The method fully utilizes the characteristics of different components in the coke oven gas, and establishes the new production process for producing methanol from coke oven gas; and the process is scientific, simple and reasonable and can satisfy the heat requirements of coke furnace and chemical production, and the unit heat value of the exhaust is 30% higher than the original coke oven gas used as the fuel, so that the operating conditions of the coke furnace are better than those in the prior art.

Description

technical field [0001] The invention relates to the production field of coal chemical products, in particular to a method of using coke oven gas as a raw material, separating different components in the coke oven gas, and rationally configuring coke oven gas to produce methanol. Background technique [0002] The traditional coke oven gas to methanol process (see figure 2 ), there is a huge waste of resources. Taking 2 million tons of coking to produce 200,000 tons of methanol as an example, the coke oven and chemical industry itself burned nearly half of the coke oven gas, of which only 28,000 Nm of hydrogen was burned 3 / h (excluding methane and carbon monoxide burned off), another 17800 Nm of hydrogen was burned off in the reformer 3 / h, 16600 Nm of hydrogen is burned when the purge gas is used as fuel 3 / h, a total of 60000 Nm of hydrogen was burned 3 / h, but actually only 50,000 Nm of hydrogen is used to synthesize methanol 3 / h. If hydrogen is synthesized into met...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C31/04C07C29/154C10L3/08
CPCC07C29/154C10L3/08C07C31/04
Inventor 王天双
Owner ZHONGRONG TECH CORP LTD
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