Cycle design and optimization of pressure swing adsorption cycles for pre-combustion CO2 capture

被引:79
|
作者
Subraveti, Sai Gokul [1 ]
Pai, Kasturi Nagesh [1 ]
Rajagopalan, Ashwin Kumar [2 ]
Wilkins, Nicholas Stiles [1 ]
Rajendran, Arvind [1 ]
Jayaraman, Ambalavan [3 ]
Alptekin, Gokhan [3 ]
机构
[1] Univ Alberta, Dept Chem & Mat Engn, Donadeo Innovat Ctr Engn Ice, 12th Floor,9211-116 St, Edmonton, AB T6G 1H9, Canada
[2] Swiss Fed Inst Technol, Inst Proc Engn, CH-8092 Zurich, Switzerland
[3] TDA Res Inc, Wheat Ridge, CO 80033 USA
关键词
Pre-combustion carbon capture; Pressure swing adsorption; Multi-objective optimization; Modeling; Genetic algorithm; Dynamic simulation; GASIFICATION COMBINED-CYCLE; CARBON CAPTURE; PSA PROCESS; FLUE-GAS; TEMPERATURE; H-2; POWER; PERFORMANCE; SIMULATION; HYDROGEN;
D O I
10.1016/j.apenergy.2019.113624
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
Novel pressure-swing adsorption (PSA) cycles were developed based on patented TDA AMS-19 (activated carbon) adsorbent for pre-combustion CO2 capture in integrated gasification combined cycle (IGCC) power plants. A variety of cycles comprising of counter-current blowdown, pressure equalization, steam purge and light product pressurization steps were designed and simulated using an in-house one dimensional detailed model. Full process optimization studies were performed for all cycles to evaluate their feasibility for pre-combustion CO2 capture. The CO2 purity and recovery Pareto fronts obtained using the multi-objective optimization were used to assess their ability to simultaneously achieve high CO2 purity (> 95%) and recovery (> 90%). The cycles that achieved the purity-recovery (95-90%) requirements were subjected to energy-productivity optimizations under the constraints of CO2 purity and recovery. Three cycle designs were ranked in terms of lowest energy consumption at 95% CO2 purities and 90% CO2 recoveries. It was found that a 10-step cycle with three pressure equalization steps achieved a minimum energy consumption of 95.7 kWh(e)/tonne of CO2 captured at a productivity of 3.3 mol CO2 captured/m(3) adsorbent/s.
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页数:13
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