Calcium deactivation during the char-CO2 gasification and its influence on determining the apparent reaction order
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作者:
Geng, Ping
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Dalian Univ Technol, Minist Educ, Sch Energy & Power Engn, Key Lab Ocean Energy Utilizat & Energy Conservat, 2 Linggong Rd, Dalian 116024, Peoples R ChinaDalian Univ Technol, Minist Educ, Sch Energy & Power Engn, Key Lab Ocean Energy Utilizat & Energy Conservat, 2 Linggong Rd, Dalian 116024, Peoples R China
Geng, Ping
[1
]
Zhang, Yan
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Dalian Univ Technol, Minist Educ, Sch Energy & Power Engn, Key Lab Ocean Energy Utilizat & Energy Conservat, 2 Linggong Rd, Dalian 116024, Peoples R ChinaDalian Univ Technol, Minist Educ, Sch Energy & Power Engn, Key Lab Ocean Energy Utilizat & Energy Conservat, 2 Linggong Rd, Dalian 116024, Peoples R China
Zhang, Yan
[1
]
机构:
[1] Dalian Univ Technol, Minist Educ, Sch Energy & Power Engn, Key Lab Ocean Energy Utilizat & Energy Conservat, 2 Linggong Rd, Dalian 116024, Peoples R China
CO2 gasification reactivity and the apparent reaction order of chars derived from calcium-rich and calcium-poor lignites have been investigated via thermogravimetry analysis (TGA) in the temperature range from 825 to 900 degrees C and the CO2 partial pressure range from 0.015 to 0.1 MPa. Chemical forms of Ca species in raw and partially-gasified chars are characterized via X-ray diffraction (XRD). Results indicate that CaO carbonation during the char-CO2 gasification is a direct cause of Ca deactivation, which shows temperature and pressure dependence and follows the equilibrium regularity of CO2 over CaCO3 at different temperatures. The Ca in lignite chars plays a catalytic role at the CO2 partial pressures below 0.1 MPa at temperatures of 875 and 900 degrees C, while Ca deactivation occurred when the CO2 partial pressures are above 0.05 MPa at 825 degrees C and above 0.075 MPa at 850 degrees C. On the one hand, this fact suggests that Ca deactivation exhibits temperature and pressure dependence. On the other hand, char gasification may follow different catalytic mechanisms in the CO2 partial pressure range from 0.015 to 0.1 MPa, from which the determination of the apparent reaction order is less reasonable. The coefficient of determination (R-2) reflects the goodness of r-PCO2 fitting, which becomes poor with the increase of CO2 partial pressure when CaO carbonation takes place. Choosing an appropriate CO2 pressure range for a given temperature is necessary to eliminate the effects of Ca deactivation on the determination of gasification reactivity and the apparent reaction order. The apparent reaction order of chars determined at conditions without Ca deactivation increases as the gasification temperature decreases.
机构:Penn State Univ, John & Willie Leone Family Dept Energy & Mineral, University Pk, PA 16802 USA
Dhaneswar, Sakthivale Roshan
Pisupati, Sarma V.
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Penn State Univ, John & Willie Leone Family Dept Energy & Mineral, University Pk, PA 16802 USAPenn State Univ, John & Willie Leone Family Dept Energy & Mineral, University Pk, PA 16802 USA
机构:
Guangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangdong, GuangzhouGuangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangdong, Guangzhou
Song Q.
Wang X.
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Guangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangdong, Guangzhou
School of Mechanical and Power Engineering, Guangdong Ocean University, Guangdong, ZhanjiangGuangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangdong, Guangzhou
Wang X.
Zhang W.
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Guangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangdong, Guangzhou
School of Energy Science and Engineering, University of Science and Technology of China, Anhui, HefeiGuangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangdong, Guangzhou
Zhang W.
Wang X.
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Guangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangdong, Guangzhou
School of Mechanical and Power Engineering, Guangdong Ocean University, Guangdong, ZhanjiangGuangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangdong, Guangzhou
Wang X.
Li H.
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Guangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangdong, GuangzhouGuangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangdong, Guangzhou
Li H.
Qiao Y.
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State Key Laboratory of Coal Combustion, Huazhong University of Science and Technology, Hubei, WuhanGuangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangdong, Guangzhou
机构:
North China Elect Power Univ, Beijing Key Lab Emiss Surveillance & Control Ther, Beijing 102206, Peoples R China
North China Univ Sci & Technol, Coll Met & Energy, Tangshan 063009, Peoples R ChinaNorth China Elect Power Univ, Beijing Key Lab Emiss Surveillance & Control Ther, Beijing 102206, Peoples R China
Liu, Yun
Qu, Jiangyuan
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North China Elect Power Univ, Beijing Key Lab Emiss Surveillance & Control Ther, Beijing 102206, Peoples R ChinaNorth China Elect Power Univ, Beijing Key Lab Emiss Surveillance & Control Ther, Beijing 102206, Peoples R China
Qu, Jiangyuan
Wu, Xuehui
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North China Elect Power Univ, Beijing Key Lab Emiss Surveillance & Control Ther, Beijing 102206, Peoples R ChinaNorth China Elect Power Univ, Beijing Key Lab Emiss Surveillance & Control Ther, Beijing 102206, Peoples R China
Wu, Xuehui
Zhang, Kai
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North China Elect Power Univ, Beijing Key Lab Emiss Surveillance & Control Ther, Beijing 102206, Peoples R ChinaNorth China Elect Power Univ, Beijing Key Lab Emiss Surveillance & Control Ther, Beijing 102206, Peoples R China
Zhang, Kai
Zhang, Yuan
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North China Univ Sci & Technol, Coll Met & Energy, Tangshan 063009, Peoples R ChinaNorth China Elect Power Univ, Beijing Key Lab Emiss Surveillance & Control Ther, Beijing 102206, Peoples R China
机构:
Xi An Jiao Tong Univ, Sch Energy & Power Engn, State Key Lab Multiphase Flow Power Engn, Dept Thermal Engn, Xian 710049, Shaanxi, Peoples R ChinaXi An Jiao Tong Univ, Sch Energy & Power Engn, State Key Lab Multiphase Flow Power Engn, Dept Thermal Engn, Xian 710049, Shaanxi, Peoples R China
Niu, Yanqing
Liu, Siqi
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Xi An Jiao Tong Univ, Sch Energy & Power Engn, State Key Lab Multiphase Flow Power Engn, Dept Thermal Engn, Xian 710049, Shaanxi, Peoples R ChinaXi An Jiao Tong Univ, Sch Energy & Power Engn, State Key Lab Multiphase Flow Power Engn, Dept Thermal Engn, Xian 710049, Shaanxi, Peoples R China
Liu, Siqi
Yan, Bokang
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Xi An Jiao Tong Univ, Sch Energy & Power Engn, State Key Lab Multiphase Flow Power Engn, Dept Thermal Engn, Xian 710049, Shaanxi, Peoples R ChinaXi An Jiao Tong Univ, Sch Energy & Power Engn, State Key Lab Multiphase Flow Power Engn, Dept Thermal Engn, Xian 710049, Shaanxi, Peoples R China
Yan, Bokang
Wang, Shuai
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Xi An Jiao Tong Univ, Sch Energy & Power Engn, State Key Lab Multiphase Flow Power Engn, Dept Thermal Engn, Xian 710049, Shaanxi, Peoples R ChinaXi An Jiao Tong Univ, Sch Energy & Power Engn, State Key Lab Multiphase Flow Power Engn, Dept Thermal Engn, Xian 710049, Shaanxi, Peoples R China
Wang, Shuai
Zhang, Xiao
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Xi An Jiao Tong Univ, Sch Energy & Power Engn, State Key Lab Multiphase Flow Power Engn, Dept Thermal Engn, Xian 710049, Shaanxi, Peoples R ChinaXi An Jiao Tong Univ, Sch Energy & Power Engn, State Key Lab Multiphase Flow Power Engn, Dept Thermal Engn, Xian 710049, Shaanxi, Peoples R China
Zhang, Xiao
Hui, Shi'en
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Xi An Jiao Tong Univ, Sch Energy & Power Engn, State Key Lab Multiphase Flow Power Engn, Dept Thermal Engn, Xian 710049, Shaanxi, Peoples R ChinaXi An Jiao Tong Univ, Sch Energy & Power Engn, State Key Lab Multiphase Flow Power Engn, Dept Thermal Engn, Xian 710049, Shaanxi, Peoples R China