Post-combustion CO2 capture with a commercial activated carbon: Comparison of different regeneration strategies

被引:295
作者
Plaza, M. G. [1 ]
Garcia, S. [1 ]
Rubiera, F. [1 ]
Pis, J. J. [1 ]
Pevida, C. [1 ]
机构
[1] CSIC, Inst Nacl Carbon, E-33080 Oviedo, Spain
关键词
CO2; capture; Adsorption cycles; Activated carbon; PRESSURE-SWING ADSORPTION; FLUE-GAS; ZEOLITE; 13X; PSA PROCESS; POWER-CONSUMPTION; SOLID SORBENTS; RECOVERY; DIOXIDE; TECHNOLOGY; NITROGEN;
D O I
10.1016/j.cej.2010.07.030
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A commercial activated carbon supplied by Norit, R2030CO(2), was evaluated as CO2 adsorbent under conditions relevant to post-combustion CO2 capture (ambient pressure and diluted CO2). It has been demonstrated that this carbon possesses sufficient CO2/N-2 selectivity in order to efficiently separate a binary mixture composed of 17% CO2 in N-2. Moreover, this carbon was easily completely regenerated and it did not show capacity decay after 10 consecutive cycles. Three different regeneration strategies were compared in a single-bed adsorption unit: temperature swing adsorption (TSA), vacuum swing adsorption (VSA) and a combination of them, vacuum and temperature swing adsorption (VISA). Through a simple two step TSA cycle, CO2 was concentrated from 17 to 43 vol%. For the single-bed cycle configurations, the productivity and CO2 recovery followed the sequence: TSA < VSA < VTSA. Values of productivity up to 1.9 mol kg(-1) h(-1) and a maximum CO2 recovery of 97% were reached. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:41 / 47
页数:7
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