The Ca-Cu looping process using natural CO2 sorbents in a packed bed: Operation strategies to accommodate activity decay

被引:4
作者
Diaz, Miriam [1 ]
Alonso, Monica [1 ]
Grasa, Gemma [2 ]
Fernandez, Jose Ramon [1 ]
机构
[1] CSIC, INCAR, Francisco Pintado Fe,26, Oviedo 33011, Spain
[2] ICB, INCAR, Miguel Luesma Castan,4, Zaragoza 50018, Spain
基金
欧盟地平线“2020”;
关键词
Calcium looping; Chemical looping combustion; Packed-bed reactor; Modelling; Hydrogen; CO2; capture; HYDROGEN-PRODUCTION; TECHNOECONOMIC ANALYSIS; CAPTURE EFFICIENCY; CONCEPTUAL DESIGN; RECENT PROGRESS; H-2; PRODUCTION; PILOT-SCALE; CALCINATION; COMBUSTION; KINETICS;
D O I
10.1016/j.ces.2023.118659
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The Ca-Cu looping process is a promising CO2 capture technology designed to produce H2 and power from a fuel gas. The use of inexpensive and widely available limestone would facilitate the scale up of this technology. This work proposes a novel strategy for packed-bed Ca-Cu looping processes consisting of loading the sufficient amount of CuO to calcine only a well-defined fraction of CaCO3 in every cycle during the transient period until the limestone reaches a residual solid conversion of 0.06 (typically after 150- 200 cycles). In this way, the excess of CaCO3 in the bed ensures temperatures below 900 & DEG;C during operation. The feasibility of this strategy is simulated for the conversion of blast furnace gas (BFG) into a H2rich product (35 vol%) diluted in N2 via the Ca-Cu looping process at 2 bar and temperatures between 600 and 850 & DEG;C, while a separated CO2 rich gas (55 vol% CO2 in N2) is obtained. & COPY; 2023 Elsevier Ltd. All rights reserved.
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页数:24
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