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作 者:臧吴琪 孙莹[1] 杨林军[1] ZANG Wu-qi;SUN Ying;YANG Lin-jun(Key Laboratory of Energy Thermal Conversion and Control of Ministry of Education,Southeast University,Nanjing 210096,China)
机构地区:[1]东南大学能源热转换及其过程测控教育部重点实验室,江苏南京210096
出 处:《应用化工》2022年第6期1633-1636,1641,共5页Applied Chemical Industry
基 金:江苏省煤基CO 2捕集与地质储存重点实验室(2016年)开放基金(2016A05)。
摘 要:分别以3种醇胺溶液:MEA、DEA和MDEA为吸收液,PP中空纤维吸收膜作为膜组件搭建膜法吸收捕集CO_(2)装置,考察不同操作条件对CO_(2)吸收性能的影响。结果表明,当吸收液浓度由0.25 mol/L增至1.5 mol/L、流速150 mL/min增至400 mL/min过程中,CO_(2)脱除效率逐渐增加,增速渐缓;而气相流速及CO_(2)浓度的升高大幅度抑制CO_(2)的脱除,CO_(2)脱除效率减少20%以上。传质速率与吸收液浓度、气液相流速及CO_(2)体积分数均成正相关。各种工况下CO_(2)脱除效率和传质速率由高到低均为MEA>DEA>MDEA;CO_(2)脱除效率和传质效率主要受CO_(2)浓度的影响。The research constructed membrane absorption CO_(2)device with PP hollow fiber membrane as membrane contactor,and three alkolamine solutions:monoethanolamine(MEA),diethanolamine(DEA)and methyldiethanolamine(MDEA)as absorption liquid,respectively.The effects of operating conditions on CO_(2)removal were investigated.The results revealed that when the absorption fluid concentration increased from 0.25 mol/L to 1.5 mol/L,flow rate 150 mL/min to 400 mL/min,the CO_(2)removal efficiency gradually increased and the rate of increase slowed down;while the increase of gas flow rate,fluid flow rate and CO_(2)volume fraction inhibited the removal efficiency of CO_(2),which was reduced by more than 20%.The mass transfer rate was positively correlated with the concentration of absorption solution,gas phase flow rate,fluid flow rate and CO_(2)volume fraction.Under the same operating conditions,the removal efficiency and mass transfer rate was:MEA>DEA>MDEA;CO_(2)removal efficiency and mass transfer efficiency were mainly affected by CO_(2)concentration.
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