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提高MDEA溶液脱碳的单位脱除率
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作者 张伍 《当代化工研究》 CAS 2023年第22期110-112,共3页
本文基于提高终端脱碳单元的CO_(2)单位脱除率的目的,深入探讨了影响MDEA溶液脱碳效率的关键问题,尤其是MDEA溶液的发泡问题,并针对问题所在提出改进措施。改进方案实施后,成功将MDEA溶液发泡问题的解决率提高到98.5%,显著降低了MDEA的... 本文基于提高终端脱碳单元的CO_(2)单位脱除率的目的,深入探讨了影响MDEA溶液脱碳效率的关键问题,尤其是MDEA溶液的发泡问题,并针对问题所在提出改进措施。改进方案实施后,成功将MDEA溶液发泡问题的解决率提高到98.5%,显著降低了MDEA的损耗和维护成本,同时提高了碳捕集系统的经济效益。 展开更多
关键词 MDEA溶液 co_(2)脱除率 脱碳效率
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燃煤电厂溶剂法碳捕集中试系统分析 被引量:2
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作者 王保登 崔倩 +4 位作者 闫学良 张峰 龙银花 孙永伟 熊日华 《现代化工》 CAS CSCD 北大核心 2022年第12期242-246,共5页
通过对某电厂溶剂法CO_(2)捕集中试装置开展基础溶剂(30%乙醇胺(MEA))的测试,揭示了烟气流量、贫液流量、再生温度、再生压力等关键操作条件对CO_(2)脱除率和再生能耗的影响规律,预测了CO_(2)脱除率90%、再生能耗4.0 GJ/t时的装置操作范... 通过对某电厂溶剂法CO_(2)捕集中试装置开展基础溶剂(30%乙醇胺(MEA))的测试,揭示了烟气流量、贫液流量、再生温度、再生压力等关键操作条件对CO_(2)脱除率和再生能耗的影响规律,预测了CO_(2)脱除率90%、再生能耗4.0 GJ/t时的装置操作范围,通过选定预测操作条件的24 h连续运行验证了预测的准确性,证实了该溶剂法CO_(2)捕集装置的可靠性,为后续其他溶剂在该装置上的测试奠定了基础。该研究方法在电厂溶剂法CO_(2)捕集中试装置上的成功应用,大大提高了中试现场的工作效率,也将为更大规模的溶剂法CO_(2)捕集示范工程提供宝贵的借鉴经验。 展开更多
关键词 燃煤电厂 co_(2)吸收 乙醇胺 co_(2)脱除率 能耗
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Mass-transfer studies of solid-base catalyst-aided CO_(2) absorption and solid-acid catalyst-aided CO_(2) desorption for CO_(2) capture in a pilot plant using aqueous solutions of MEA and blends of MEA-MDEA and BEA-AMP
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作者 James Coker Daniel Boafo Afari +1 位作者 Jessica Narku-Tetteh Raphael Idem 《Clean Energy》 EI 2019年第4期263-277,共15页
Mass-transfer studies of catalyst-aided CO_(2) absorption and desorption were performed in a full-cycle,bench-scale pilot plant to improve CO_(2) absorption using 5M MEA,5M MEA-2M MDEA and 2M BEA-2M AMP.A solid-base c... Mass-transfer studies of catalyst-aided CO_(2) absorption and desorption were performed in a full-cycle,bench-scale pilot plant to improve CO_(2) absorption using 5M MEA,5M MEA-2M MDEA and 2M BEA-2M AMP.A solid-base catalyst,K/MgO,and an acid catalyst,HZSM-5,were used to facilitate absorption and desorption,respectively.Absorption and desorption mass-transfer performance was presented in terms of the overall mass-transfer coefficient of the gas side(KGav)and liquid side(K_(L)a_(v)),respectively.For non-catalytic runs,the highest K_(G)a_(V) and K_(L)a_(V) were 0.086 Kmol m^(3).kPa.hr and 0.7851 hr for 2M BEA-2M AMP solvent.The results showed 38.7% KGav and 23.6% K_(L)a_(v) increase for 2M BEA-2M AMP with only HZSM-5 catalyst in desorber and a 95% K_(G)a_(V) and 45% K_(L)a_(V) increase for both K/MgO catalyst and HZSM-5 catalyst.This was attributed to the role of K/MgO in bonding loosely with CO_(2) and making it available for the amine reaction. 展开更多
关键词 HZSM-5 K/MgO catalyst co_(2)removal efficiency co_(2)capture mass-transfer coefficients of absorber(KGaV)and desorber(K_(L)a_(V))
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