提高再生气中H_2S浓度的方案研究  被引量:2

Solution method for increasing the concentration of H_2S in regeneration gas

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作  者:朱维强 吴慧雄[1] 金孟笛 李复[1] ZHU WeiQiang;WU HuiXiong;JIN MengDi;LI Fu(College of Chemical Engineering,Beijing University of Chemical Technology,Beijing 100029;Inlernational College,Beijing University of Posts and Telecommunications,Beijing 100876,China)

机构地区:[1]北京化工大学化学工程学院,北京100029 [2]北京邮电大学国际学院,北京100876

出  处:《北京化工大学学报(自然科学版)》2018年第4期25-29,共5页Journal of Beijing University of Chemical Technology(Natural Science Edition)

摘  要:对以生物质热解气为原料的低温甲醇洗工艺进行模拟和研究,热解气主要成分为CO_2、H_2、CO、H_2S、COS和水等。采用Aspen plus对低温甲醇洗工艺进行全流程模拟,通过对比分析可知,模拟结果与实际值基本吻合。针对原工艺H_2S浓度低的问题,提出两个改进方案以提高H_2S的浓度:(1)提高气提塔的N_2流量;(2)在气提塔后添加一个闪蒸罐,气提塔塔底的甲醇溶液经过加热和闪蒸后再进入甲醇再生塔。结果表明改进方案可以大大提高再生气中H_2S的浓度。Production of biomass pyrolysis gas as a raw material in a plant has been simulated and studied and the main components found to be CO2,H2,CO,H2S,COS and water. Aspen plus was utilized to simulate the rectisol process. Comparative analysis shows that the simulation results are consistent with actual values. In consideration of the low concentration of H2S in conventional processes,two methods are proposed to increase the concentration of H2S:( 1) Improving the N2 flow of the gas tower;( 2) Adding a heat exchanger and flash tank to the stripper,so that the methanol solution at the bottom of the stripper tower is heated and flashed before entering the methanol regeneration tower. The results show that the concentration of H2S can be significantly increased by using these two steps.

关 键 词:低温甲醇洗 稳态模拟 CPA热力学方程 H2S浓度提高 

分 类 号:N945[自然科学总论—系统科学]

 

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