Technological method for preparing methanol by combining coke oven gas with water gas

A technique for synthesizing methanol from coke oven gas, applied in chemical instruments and methods, preparation of hydroxyl compounds, preparation of organic compounds, etc., can solve problems such as unbalanced hydrogen-carbon ratios, achieve an increase in primary conversion rate, reduce production costs, and effectively The effect of improving the utilization rate of ingredients

Inactive Publication Date: 2010-05-12
山西焦化股份有限公司
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AI Technical Summary

Problems solved by technology

[0005] The purpose of the present invention is to make up for the serious unbalanced hydrogen-to-carbon ratio in the existing technology of coke oven gas conversion to methanol, and to provide a process for coke oven gas with water gas and low-pressure synthesis of methanol

Method used

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Examples

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Embodiment Construction

[0030] Coke oven gas from coke oven gas outer pipe, pressure 500mmH 2 O column, with a temperature of 35°C, passes through the coke oven gas tank and dry-type electric tar catcher, enters the Roots blower, pressurizes and enters the desulfurization tower, and contacts with the desulfurization liquid sprayed from the tower top in the desulfurization tower countercurrently to absorb the gas H in 2 S and part of the organic sulfur, after the liquid is separated by the swirl plate on the upper part of the desulfurization tower, the dust and tar are further removed by the dry electric tar catcher, and sent to the coke oven gas compression process.

[0031] The pressure of the coke oven gas from the compression process is 2.5MPa, and the temperature is 40°C. First, the tar and dust are removed through the filter, and then it is preheated to 300-350°C in the conversion section.

[0032] The preheated coke oven gas passes through the iron-molybdenum pre-reformer and iron-molybdenum c...

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PUM

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Abstract

The invention discloses a technological method for preparing methanol by combining coke oven gas with water gas. The method comprises the following steps: purifying coke oven gas; performing direct fine desulfurization and purification to water gas at a low temperature; mixing the cleaned and qualified coke oven gas and water gas to ensure the mixed gas to reach a hydrogen carbon ratio that (H2 - CO) / (CO2 + CO) = 2.05-2.10, pressurizing the mixed gas, and sending the mixed gas into a methanol synthesis tower for synthesizing methanol at low pressure. The method of the invention avoids the problem of serious imbalance of hydrogen carbon ratio in the process of preparing methanol by only using coke oven gas, the methanol one-step conversion is increased, the utilization rate of effective ingredients is increased, the production cost is reduced; the problem of low sulfur capacity of the existing catalyst to the organic sulfur such as CS2 and COS is solved, the technological process has no cold-hot fatigue, finally the total sulfur content of water gas can reach 0.1ppm or more; and the technological method of the invention designs a difunctional ventilation gas-recycling device so that one device can be used to realize two purposes.

Description

technical field [0001] The present invention relates to a method for synthesizing methanol with coke oven gas, in particular to a method for synthesizing methanol at low pressure with coke oven gas and water gas. . Background technique [0002] At present, the scale of my country's methanol plants is generally small, and the coal-head route using coal as raw material accounts for 78%. The disadvantage is that the unit capacity investment is high, and the production cost is 1,700-2,100 yuan / ton, which is about the investment of foreign large-scale methanol plants. 2 times. The scale of foreign methanol plants represented by the Middle East and Central and South America is generally large. Currently, the production capacity of the largest methanol plant in the world has reached 1.7 million tons per year. At the end of April 2008, the Saudi Methanol Company's 1.7 million tons / year giant methanol plant was put into operation in Al Jubail, bringing the total production capacity ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C31/04C07C29/151
CPCY02P20/52
Inventor 卫正义杨清明马万进翟越广张文案李金喜宋红慧张国军樊生才张权应
Owner 山西焦化股份有限公司
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