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Economic Analysis of CO_2 Separation from Coal-fired Flue Gas by Chemical Absorption and Membrane absorption Technologies in China

机译:中国化学吸收与膜吸收技术与燃煤烟气分离的CO_2分离经济分析

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Two typical CO_2 chemical absorption processes using MEA and aqueous ammonia (AA) solutions to act as absorbents and one novel process using hollow fiber membrane contactors (HFMCs) to act as absorber and MEA as absorbent were analyzed in this study to find out what CO_2 capture process may be more suitable for China. An ultra supercritical PC power plant with 840-MWe-gross-output was selected as the reference case without CO_2 capture. Economic results show that when membrane price is set at RMB 50/m~2 and lifetime is 5 years, CAPEX of MEA, HFMC and AA cases are increased by about 90.12%, 85.4% and 68%, respectively, compared to reference case. And the corresponding cost of avoided is RMB 305.1/tCO_2, RMB 266.45/tCO_2 and RMB 206.02/tCO_2, respectively. The seemingly positive results imply that AA-based chemical absorption process should be the best for China nowadays. In addition, prospect of HFMC process in the future was also considered based on the increasing anxiety of NH_3 slip for AA process. If membrane price can be reduced to less than RMB 20/m~2 and new solvents with ~3 GJ/tCO_2 total regeneration heat requirement can be adopted in the future, HFMC may replace the AA-based method to capture CO_2. Additionally, economic results also show that the development of new solvents only considering the reduction of heat of CO_2 absorption may be not sufficient in terms of the reduction of CO_2 avoided cost. That is because CO_2 avoided cost can only be reduced by about 8% even the heat of CO_2 absorption can be reduced by about 60%. Finally, effects of coal price, improvements of reference case and CO_2 capture system on the cost of CO_2 avoided were also investigated.
机译:使用MEA和氨水(AA)溶液的两个典型的CO_2化学吸收过程作为使用中空纤维膜接触器(HFMC)的吸收剂和一种新方法,以充当吸收剂和MEA作为吸收剂作为吸收剂,以找出CO_2捕获的捕获过程可能更适合中国。选择具有840 MWE-GROS-OUTPUT的超超临界PC电厂作为没有CO_2捕获的参考情况。经济结果表明,当膜价格设定为50 / m〜2,寿命为5年,与参考案例相比,MEA,HFMC和AA病例的CAPEX分别增加了约90.12%,85.4%和68%。避免的相应成本分别为人民币305.1 / TCO_2,266.45 / TCO_2和人民币206.02 / TCO_2。看似积极的结果意味着现在,AA的化学吸收过程现在应该是最适合中国的。此外,还将根据AA流程的越来越多的NH_3滑块焦虑越来越多地考虑未来HFMC过程的前景。如果未来可以采用薄膜价格低于20 / m〜2,新的溶剂〜3 GJ / TCO_2总再生热需求,HFMC可以取代基于AA的方法来捕获CO_2。此外,经济结果还表明,在避免成本的减少方面,仅考虑减少CO_2吸收的热量的新溶剂的开发可能是不够的。这是因为避免成本只能降低8%,即使CO_2吸收的热量也可以减少约60%。最后,还研究了煤炭价格,参考案例的改进和CO_2捕获系统的影响,避免了CO_2成本。

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