Al2O3 and CeO2-promoted MgO sorbents for CO2 capture at moderate temperatures

被引:0
作者
Huimei Yu
Xiaoxing Wang
Zhu Shu
Mamoru Fujii
Chunshan Song
机构
[1] Pennsylvania State University,EMS Energy Institute, PSU
[2] Chinese Academy of Sciences,DUT Joint Center for Energy Research, and Department of Energy & Mineral Engineering
[3] East China University of Science and Technology,Shanghai Institute of Ceramics
来源
Frontiers of Chemical Science and Engineering | 2018年 / 12卷
关键词
CO; capture; MgO sorbents; Al; O; CeO; flue gas;
D O I
暂无
中图分类号
学科分类号
摘要
A series of Al2O3 and CeO2 modified MgO sorbents was prepared and studied for CO2 sorption at moderate temperatures. The CO2 sorption capacity of MgO was enhanced with the addition of either Al2O3 or CeO2. Over Al2O3-MgO sorbents, the best capacity of 24.6 mg- CO2/g-sorbent was attained at 100 °C, which was 61% higher than that of MgO (15.3 mg-CO2/g-sorbent). The highest capacity of 35.3 mg-CO2/g-sorbent was obtained over the CeO2-MgO sorbents at the optimal temperature of 200 °C. Combining with the characterization results, we conclude that the promotion effect on CO2 sorption with the addition of Al2O3 and CeO2 can be attributed to the increased surface area with reduced MgO crystallite size. Moreover, the addition of CeO2 increased the basicity of MgO phase, resulting in more increase in the CO2 capacity than Al2O3 promoter. Both the Al2O3-MgO and CeO2-MgO sorbents exhibited better cyclic stability than MgO over the course of fifteen CO2 sorption-desorption cycles. Compared to Al2O3, CeO2 is more effective for promoting the CO2 capacity of MgO. To enhance the CO2 capacity of MgO sorbent, increasing the basicity is more effective than the increase in the surface area.
引用
收藏
页码:83 / 93
页数:10
相关论文
共 229 条
  • [1] Williams J H D(2012)The technology path to deep greenhouse gas emissions cuts by 2050: The pivotal role of electricity Science 335 53-59
  • [2] Benedictis A(2009)“Molecular basket” sorbents for separation of CO Journal of the American Chemical Society 131 5777-5783
  • [3] Ghanadan R(2006) and H2S from various gas streams Catalysis Today 115 2-32
  • [4] Mahone A(2012)Global challenges and strategies for control, conversion and utilization of CO Carbon Management 3 201-220
  • [5] Moore J(2004) for sustainable development involving energy, catalysis, adsorption and chemical processing Energy 29 1259-1267
  • [6] Morrow W R(2008)Part 5b: Solvent chemistry: Reaction kinetics of CO Journal of Membrane Science 325 509-519
  • [7] Price S(2005) absorption into reactive amine solutions Separation Science and Technology 40 321-348
  • [8] Torn M S(1997)Test results from a CO Energy Conversion and Management 38 S147-S152
  • [9] Ma X L(2010) extraction pilot plant at boundary dam coal-fired power station Angewandte Chemie International Edition 49 6058-6082
  • [10] Wang X X(2012)Liquid membranes for gas/vapor separation Journal of Colloid and Interface Science 366 147-154