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1.国电电力发展股份有限公司,北京 100101
2.国能三河发电有限责任公司,河北 廊坊 065201
3.华中科技大学 能源与动力工程学院 煤燃烧与低碳利用全国重点实验室,湖北 武汉 430074
顾永正(1991—),博士,高级工程师,研究方向为清洁低碳发电技术及工程,E-mail:yongzheng.gu@chnenergy.com.cn。
李小姗(1990—),博士,副教授,研究方向为CO2捕集和污染物脱除技术,E-mail:lxs0721@hust.edu.cn。
收稿日期:2024-08-23,
修回日期:2024-10-12,
纸质出版日期:2025-04-25
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顾永正,李晓辉,高歌等.高效低能耗氨基酸盐水溶液固-液相变吸收剂捕集CO2性能探究[J].低碳化学与化工,2025,50(04):122-130.
GU Yongzheng,LI Xiaohui,GAO Ge,et al.Study on amino acid salt aqueous solid-liquid phase change absorbent for energy-efficient CO2 capture[J].Low-Carbon Chemistry and Chemical Engineering,2025,50(04):122-130.
顾永正,李晓辉,高歌等.高效低能耗氨基酸盐水溶液固-液相变吸收剂捕集CO2性能探究[J].低碳化学与化工,2025,50(04):122-130. DOI: 10.12434/j.issn.2097-2547.20240348.
GU Yongzheng,LI Xiaohui,GAO Ge,et al.Study on amino acid salt aqueous solid-liquid phase change absorbent for energy-efficient CO2 capture[J].Low-Carbon Chemistry and Chemical Engineering,2025,50(04):122-130. DOI: 10.12434/j.issn.2097-2547.20240348.
利用传统有机胺水溶液捕集CO
2
的再生能耗较高,制约了其在CO
2
捕集领域的广泛应用。为降低吸收
剂的再生能耗,提出了一种高效低能耗氨基酸盐水溶液固-液相变吸收剂。制备了不同浓度的L-苏氨酸钾溶液(PL-T)作为固-液相变吸收剂,研究了其CO
2
吸收、解吸过程,并对吸收、解吸速率,以及反应热、显热等进行了评价。结果表明,在吸收、解吸温度分别为313 K、363 K下,当PL-T浓度为4 mol/L时,吸收、解吸速率均达到最大值,分别为2.20 × 10
-5
mol/s、1.43 × 10
-4
mol/s。在313 K下,5 mol/L PL-T与CO
2
的反应热为-80.94 kJ/mol,其绝对值小于5 mol/L单乙醇胺溶液对应值(-88.22 kJ/mol),因此解吸能耗更低;当只解吸5 mol/L PL-T的固相沉淀物时,其显热可较5 mol/L MEA降低51.4%。
High regeneration energy consumption for CO
2
capture by traditional aqueous amine solution is still one of the bottlenecks restricting its wide application in CO
2
capture field. In order to reduce the regenerative energy consumption of the absorbent
an energy-efficient amino acid solution solid-liquid phase change absorbent was proposed. Potassium L-threonine solutions (PL-T) with different concentrations were prepared as the solid-liquid phase change absorbent. The CO
2
absorption and desorption processes of PL-T were investigated
and the absorption and desorption rates
reaction heat and sensible heat were evaluated. The results show that under absorption and desorption temperatures of 313K and 363 K
respectively
the absorption and desorption rates both reach the maximum values with PL-T concentration of 4 mol/L
which are 2.20 × 10
-5
mol/s and 1.43 × 10
-4
mol/s
respectively. Under 313 K
the reaction heat of 5 mol/L PL-T with CO
2
is -80.94 kJ/mol
and its absolute value is less than the corresponding value (-88.22 kJ/mol) of 5 mol/L monoethanolamine solution
leading to a lower desorption energy consumption. When only solid precipitate of 5 mol/L PL-T is desorbed
its sensible heat can be reduced by 51.4%
compared to 5 mol/L MEA.
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