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首页> 外文期刊>Journal of Cleaner Production >Design and simulation of a methanol production plant from CO_2 hydrogenation
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Design and simulation of a methanol production plant from CO_2 hydrogenation

机译:CO_2加氢制甲醇装置的设计与仿真

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摘要

There has been a large increase in anthropogenic emissions of CO_2 over the past century. The use of captured CO_2 can become a profitable business, in addition to controlling CO_2 concentration in the atmosphere. A process for producing fuel grade methanol from captured CO_2 is proposed in this paper. The process is designed and simulated with Aspen Plus. The CO_2 is captured by chemical absorption from the flue gases of a thermal power plant. The hydrogen is produced by water electrolysis using carbon-free electricity. The methanol plant provides 36% of the thermal energy required for CO_2 capture, reducing considerably the costs of the capture. The CO_2 balance of the process showed that it is possible to abate 1.6 t of CO_2 per tonne of methanol produced if oxygen by-product is sold, or 1.2 t if it is not.
机译:在过去的一个世纪中,人为排放的CO_2大量增加。除了控制大气中的CO_2浓度以外,使用捕获的CO_2还可成为一项有利可图的业务。本文提出了一种由捕获的CO_2生产燃料级甲醇的方法。该过程是使用Aspen Plus设计和模拟的。通过从火力发电厂的烟道气中吸收化学药品来捕获CO_2。氢气是使用无碳电力通过水电解产生的。甲醇工厂提供了CO_2捕集所需热能的36%,大大降低了捕集成本。该过程的CO_2平衡表明,如果出售氧气副产品,则每吨生产的甲醇可减少1.6吨CO_2,否则则减少1.2吨。

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