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不同合成工艺的二氧化碳催化加氢制甲醇装置经济性分析

吴子波 蹇守华 吴路平

低碳化学与化工2023,Vol.48Issue(6):60-66,7.
低碳化学与化工2023,Vol.48Issue(6):60-66,7.DOI:10.12434/j.issn.2097-2547.20220344

不同合成工艺的二氧化碳催化加氢制甲醇装置经济性分析

Plants economic analysis of catalytic hydrogenation of CO2 to methanol with different synthesis processes

吴子波 1蹇守华 1吴路平1

作者信息

  • 1. 西南化工研究设计院有限公司 工业排放气综合利用国家重点实验室,四川 成都 610225
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摘要

Abstract

In order to study the economy of carbon dioxide catalytic hydrogenation large-scale methanol production plants,three representative processes(one methanol tower with circulation process,two methanol towers with circulation process and two methanol towers with circulation and small synthesis process)were taken as the research object,and 10×104 t/a methanol production capacity was taken as an example from three aspects:fixed asset investment,public engineering consumption and total cost.The economic efficiency of the three processes was analyzed and compared.The results show that the total cost of two methanol towers with circulation process is reduced by 5.3%compared to one methanol tower with circulation process and the total cost of two methanol towers with circulation and small synthesis process is reduced by 9.0%compared to one methanol tower with circulation process.In the total cost,hydrogen accounts from 46%to 52%,so hydrogen is the decisive factor affecting the total cost.When the price of methanol is 2696.9 CNY/t,the price of carbon dioxide is less than or equal to 0.4 CNY/m3 and the price of hydrogen is less than or equal to 0.7 CNY/m3,two methanol towers with circulation and small synthesis process is economically feasible.

关键词

二氧化碳/催化加氢/甲醇/固定资产投资/公用工程消耗/总成本费用

Key words

carbon dioxide/catalytic hydrogenation/methanol/fixed assets investment/utility consumption/total cost

分类

化学化工

引用本文复制引用

吴子波,蹇守华,吴路平..不同合成工艺的二氧化碳催化加氢制甲醇装置经济性分析[J].低碳化学与化工,2023,48(6):60-66,7.

低碳化学与化工

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