1. 昊华化工科技集团股份有限公司,四川,成都,610225
2. 西南化工研究设计院有限公司 工业排放气综合利用国家重点实验室,国家碳一化学工程技术研究中心,四川,成都,610225
3. 中国石油天然气股份有限公司广西石化分公司,广西,钦州,535000
4. 胜利油田鲁胜石油开发有限责任公司,山东,东营,257077
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任恩泽, 张巍松, 王育力, 等. 液固相变吸收剂的CO2吸收性能及相分离行为机理研究[J]. 低碳化学与化工.
REN Enze, ZHANG Weisong, WANG Yuli, et al. Research on CO2 absorption and phase separation mechanism of liquid-solid phase change absorbent[J]. Low-Carbon Chemistry and Chemical Engineering.
任恩泽, 张巍松, 王育力, 等. 液固相变吸收剂的CO2吸收性能及相分离行为机理研究[J]. 低碳化学与化工. DOI: 10.12434/j.issn.2097-2547.20230033.
REN Enze, ZHANG Weisong, WANG Yuli, et al. Research on CO2 absorption and phase separation mechanism of liquid-solid phase change absorbent[J]. Low-Carbon Chemistry and Chemical Engineering. DOI: 10.12434/j.issn.2097-2547.20230033.
以N-甲基二乙醇胺(MDEA)+哌嗪(PZ)水溶液作为复合吸收剂的化学吸收法是捕集二氧化碳(CO,2,)的重要手段之一,但该复合吸收剂再生能耗较高,限制了其在碳捕集领域的应用。为克服该缺点,在该复合吸收剂中加入某种溶剂形成相变吸收剂,可减少吸收剂进入解吸单元的总量,从而降低再生能耗。设计了一种组成为MDEA+PZ+N-甲基吡咯烷酮(NMP)+水(H,2,O)的液固相变吸收剂,并考察了其吸收CO,2,的性能,测定了NMP、PZ质量分数对液固相变吸收剂CO,2,溶解度的影响,分析了相分离行为机理。结果表明,该吸收剂的CO,2,溶解度随着NMP质量分数的增加而降低,随着PZ质量分数的增加而增加;当吸收剂中NMP、PZ的质量分数分别达到50%、3%及以上时,吸收CO,2,后生成PZ-氨基甲酸酯达到饱和析出形成固相,固相先随CO,2,溶解度增加而增加,后随着CO,2,溶解度继续增加,生成更易溶于水的PZ-二氨基甲酸酯,导致固相减少。
The chemical absorption method with N-methyldiethanolamine(MDEA) + piperazine(PZ) aqueous solution as the composite absorbent is one of the important means for CO,2, capture. However, the high regeneration energy consumption of this composite absorbent limits its application in the field of carbon capture. In order to overcome this shortcoming, some certain additive is added to form phase change absorbent to reduce the total amount of absorbent into the desorption unit, so as to reduce the energy consumption for regeneration. A liquid-solid phase change absorbent with the composition of MDEA + PZ + N-methylpyrrolidone(NMP) + water(H,2,O) was designed. The CO,2, absorption performance of the liquid-solid phase change absorbent was investigated, the effects of mass fraction of NMP and PZ on the CO,2, solubility were determined, and the mechanism of liquid-solid phase separation behavior mechanism was also analyzed. The results show that, the CO,2, solubility of the liquid-solid phase change absorbent decreases with the increase of the mass fraction of NMP and increases with the increase of the mass fraction of PZ. When the mass fraction of NMP and PZ in the absorbent reaches 50% and 3% and above, respectively, the PZ-carbamate formed by absorbing CO,2, can reach saturation and precipitate to form a solid phase. The solid phase first increases with the increase of CO,2, solubility, and then PZdicarbamate which is more soluble in water is formed with the increase of CO,2, solubility, resulting in the decrease of solid phase.
CO2捕集相变吸收剂相分离行为MDEANMP
CO2 capturephase change absorbentphase separation behaviorMDEANMP
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