化工学报 ›› 2018, Vol. 69 ›› Issue (6): 2526-2532.DOI: 10.11949/j.issn.0438-1157.20171364

• 分离工程 • 上一篇    下一篇

分子筛SBA-15负载离子液体[P66614][Triz]脱除氢烷气中CO2

李艳南, 程军, 刘建忠, 周俊虎, 岑可法   

  1. 浙江大学能源清洁利用国家重点实验室, 浙江 杭州 310027
  • 收稿日期:2017-10-12 修回日期:2018-01-07 出版日期:2018-06-05 发布日期:2018-06-05
  • 通讯作者: 程军
  • 基金资助:

    国家重点研发计划项目(2016YFE0117900);浙江省重点研发计划项目(2017C04001)。

CO2removal from biohythane by absorption in ionic liquid[P66614][Triz]loaded on molecular sieve SBA-15

LI Yannan, CHENG Jun, LIU Jianzhong, ZHOU Junhu, CEN Kefa   

  1. State Key Laboratory of Clean Energy Utilization, Zhejiang University, Hangzhou 310027, Zhejiang, China
  • Received:2017-10-12 Revised:2018-01-07 Online:2018-06-05 Published:2018-06-05
  • Supported by:

    supported by the National Key Research and Development Program of China (2016YFE0117900) and the Key Research and Development Program of Zhejiang Province (2017C04001).

摘要:

以高效吸收CO2的离子液体(IL)[P66614][Triz]作为吸收剂,通过浸渍法负载到两种不同孔径的介孔分子筛SBA-15上,用于脱除生物氢烷气中CO2,并利用N2吸附仪、扫描电子显微镜(SEM)和高倍透射电子显微镜(HRTEM)对负载材料进行了表征分析。混合吸收剂SBA-15(4.3 nm)-50%[Triz]的吸收容量和吸收速率比SBA-15(6.6 nm)-50%[Triz]的分别提高了12.4%和95.1%,这是由于SBA-15(4.3 nm)的孔道长度更短,避免了填充在孔道内的[P66614][Triz]在反应过程中接触不到CO2,从而比SBA-15(6.6 nm)-50%[Triz]有更多IL反应活性点参与反应。还研究了不同氢烷气速率下SBA-15(4.3 nm)-50%[Triz]对CO2的吸收并与2种吸附动力学模型相拟合,结果表明SBA-15(4.3 nm)-50%[Triz]对CO2的吸收更符合准二级吸附动力学模型,表明吸附过程受化学吸附机理的控制,验证了[P66614][Triz]是通过化学反应脱除CO2

关键词: 离子液体, 分子筛, CO2, 动力学模型, 生物氢烷气

Abstract:

A highly efficient CO2 absorbent, ionic liquid (IL)[P66614] [Triz], was impregnated on molecular sieves SBA-15 with two different pore diameters for removing CO2 in biohythane. The hybrid absorbents were characterized by N2 adsorption analyzer, scanning electron microscopy (SEM), high-resolution transmission electron microscopy (HRTEM). Compared to SBA-15 (6.6 nm) -50%[Triz], SBA-15 (4.3 nm) -50%[Triz] had higher CO2 absorption capacity and absorbing rate by an increase of 12.4% and 95.1%, respectively. The shorter pore length of SBA-15 (4.3 nm) allowed[P66614][Triz] inner pores to contact CO2 during adsorption process, hence SBA-15 (4.3 nm) -50%[Triz] had more IL reactive sites than SBA-15 (6.6 nm) -50%[Triz]. CO2 absorption in SBA-15 (4.3 nm) -50%[Triz] under different hythane gas flowrate was further studied and fitted with two adsorption kinetic models. The results show that CO2 adsorption bySBA-15 (4.3 nm) -50%[Triz] follows better with pseudo-second order adsorption dynamic model, indicating that the adsorption process is controlled by chemical adsorption mechanism and CO2 removal by[P66614] [Triz] is a chemical reaction process.

Key words: ionic liquid, molecular sieve, CO2, kinetic modeling, biohythane

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