Sensitivity Analysis of Carbonate Looping Process Using Twin Fluidized Bed Model

被引:0
作者
Yang, Xuan [1 ]
Qiao, Yishu [1 ]
Han, Xiangyang [1 ]
Liu, Bingcheng [1 ,2 ]
Shah, Kinjal J. [3 ]
Chiang, Pen-Chi [4 ]
机构
[1] Qingdao Univ Sci & Technol, Qingdao 266061, Peoples R China
[2] Inst Climate & Energy Sustainable Dev, Qingdao 266061, Peoples R China
[3] Nanjing Tech Univ, Coll Urban Construct, Nanjing 211816, Peoples R China
[4] Natl Taiwan Univ, Carbon Cycle Res Ctr, Taipei 10672, Taiwan
关键词
CO2; capture; Carbonate looping; Process model; Twin Fluidized bed; Sensitivity analysis; MWTH PILOT-PLANT; CO2; CAPTURE; ATTRITION; SIMULATION; POLLUTANTS; EMISSION; CAPACITY; PROGRESS; REMOVAL; DESIGN;
D O I
10.4209/aaqr.2020.07.0436
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
CO2 as the major greenhouse gas plays an important role in environmental problems. Therefore, it is reasonable to find an effective technology for mitigating large CO2 emissions. Carbonating looping is an efficient post-combustion CO2 capture technology using limestone sorbent, which is more energy-saving than traditional technologies. In our research, a carbonate looping process model had been developed using ASPEN PLUS software. In detail, the sensitivity analysis of main parameters were adopted. The simulation results indicated that the CO2 capture rate of the whole process can achieve above 90% and CO2 concentration in the decarbonated flue gas was less than 4% under the carbonation temperature, the calcination temperature, the F-0/F-CO2 and the gas-solid separation were 630 degrees C, 900 degrees C, 0.04, 1.0, separately. This work gave an potential example for the retrofitting current coal-fired power plant combined with carbonate looping process.
引用
收藏
页码:2889 / 2900
页数:12
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