Evaluating the Feasibility of a TSA Process Based on Steam Stripping in Combination with Structured Carbon Adsorbents To Capture CO2 from a Coal Power Plant

被引:47
作者
Plaza, Marta G. [1 ]
Rubiera, Fernando [1 ]
Pevida, Covadonga [1 ]
机构
[1] CSIC, Inst Nacl Carbon, INCAR, C Francisco Pintado Fe 26, Oviedo 33011, Spain
基金
欧盟第七框架计划;
关键词
SWING ADSORPTION; ACTIVATED CARBON; FLUE-GAS; WATER-ADSORPTION; ZEOLITE; 13X; POSTCOMBUSTION CAPTURE; SOLID SORBENTS; BED SYSTEM; N-2; DIOXIDE;
D O I
10.1021/acs.energyfuels.7b01508
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The present work evaluates the feasibility to capture at least 85% of the CO2 emitted by an advanced supercritical pulverized coal power plant of 800 MWe, delivering a CO2 product with a purity of 95% (dry basis) or higher, using an adsorption-based postcombustion capture process based on carbon honeycomb monoliths regenerated by steam stripping. Process performance has been evaluated through the dynamic simulation of the cyclic adsorption process. The fixed bed adsorption model, which was validated against experimental results, is based on the mass, momentum, and energy conservation equations, and it accounts for competitive adsorption between the three main flue gas components: N-2, CO2, and H2O. The evaluated TSA process meets the targets for the capture rate and product purity, with a heat duty of 3.59 MJ kg(-1) CO2, which is close to the specific reboiler duty of the benchmark amine-based absorption process. Materials and process development will lead to lower duties. A sensitivity analysis was carried out, and it has shown that slightly faster adsorption kinetics for CO2 could drop the specific heat duty of the process to 2.89 MJ kg(-1) CO2, which is lower than that of the benchmark technology. From the process point of view, the use of waste heat from the power plant could further reduce the energy penalty of the integrated CO2 capture process.
引用
收藏
页码:9760 / 9775
页数:16
相关论文
共 57 条
  • [1] [Anonymous], 2002, PROP CHAR GRAPH
  • [2] ON THE DISPERSION OF A SOLUTE IN A FLUID FLOWING THROUGH A TUBE
    ARIS, R
    [J]. PROCEEDINGS OF THE ROYAL SOCIETY OF LONDON SERIES A-MATHEMATICAL AND PHYSICAL SCIENCES, 1956, 235 (1200): : 67 - 77
  • [3] Carbon capture by physical adsorption: Materials, experimental investigations and numerical modeling and simulations - A review
    Ben-Mansour, R.
    Habib, M. A.
    Bamidele, O. E.
    Basha, M.
    Qasem, N. A. A.
    Peedikakkal, A.
    Laoui, T.
    Ali, M.
    [J]. APPLIED ENERGY, 2016, 161 : 225 - 255
  • [4] Adsorption of gases in multimolecular layers
    Brunauer, S
    Emmett, PH
    Teller, E
    [J]. JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1938, 60 : 309 - 319
  • [5] COMPARISON OF ACTIVATED CARBON AND ZEOLITE 13X FOR CO2 RECOVERY FROM FLUE-GAS BY PRESSURE SWING ADSORPTION
    CHUE, KT
    KIM, JN
    YOO, YJ
    CHO, SH
    YANG, RT
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (02) : 591 - 598
  • [6] Water adsorption on zeolite 13X: comparison of the two methods based on mass spectrometry and thermogravimetry
    Cortes, F. B.
    Chejne, F.
    Carrasco-Marin, F.
    Moreno-Castilla, C.
    Perez-Cadenas, A. F.
    [J]. ADSORPTION-JOURNAL OF THE INTERNATIONAL ADSORPTION SOCIETY, 2010, 16 (03): : 141 - 146
  • [7] Carbon monoliths: A comparison with granular materials
    Crittenden, B
    Patton, A
    Jouin, C
    Perera, S
    Tennison, S
    Echevarria, JAB
    [J]. ADSORPTION-JOURNAL OF THE INTERNATIONAL ADSORPTION SOCIETY, 2005, 11 (Suppl 1): : 537 - 541
  • [8] Nonuniform Channels in Adsorbent Monoliths
    Crittenden, B. D.
    Camus, O.
    Perera, S. P.
    Mays, T. J.
    Sanchez-Liarte, F.
    Tennison, S. R.
    Crezee, E.
    [J]. AICHE JOURNAL, 2011, 57 (05) : 1163 - 1172
  • [9] Do D. D, 1998, ADSORPTION ANAL EQUI
  • [10] HOMOGENEOUS AND HETEROGENEOUS MICROPORE STRUCTURES IN CARBONACEOUS ADSORBENTS
    DUBININ, MM
    STOECKLI, HF
    [J]. JOURNAL OF COLLOID AND INTERFACE SCIENCE, 1980, 75 (01) : 34 - 42