The influence of CO2 gas concentration on the char temperature and conversion during oxy-fuel combustion in a fluidized bed

被引:13
|
作者
Salinero, J. [1 ]
Gomez-Barea, A. [1 ]
Fuentes-Cano, D. [1 ]
Leckner, B. [2 ]
机构
[1] Univ Seville, Chem & Environm Engn Dept, Seville 41092, Spain
[2] Chalmers Univ Technol, Div Energy Technol, S-41296 Gothenburg, Sweden
关键词
Fluidized bed; Oxy-combustion; Char temperature; Pyrometry; Coal; Biomass; MASS-TRANSFER COEFFICIENT; PARTICLE COMBUSTION; HEAT-TRANSFER; MULTIPARTICLE SYSTEMS; GASIFICATION REACTION; SURFACE-TEMPERATURE; TRANSPORT PHENOMENA; CONDITIONS; PART; ACTIVE PARTICLES; COAL PARTICLES;
D O I
10.1016/j.apenergy.2018.01.038
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
In spite of the extensive theoretical and experimental work carried out on coal/char oxy-combustion in a fluidized bed (FB), the effect of changing the atmosphere from O-2/N-2 to O-2/CO2 for a high O-2 concentrations is not entirely understood. In this work, experiments with single char particles are conducted in a bi-dimensional FB at 800 and 850 degrees C, varying the O-2 concentration from 11 to 50%(v/v) in N-2 or CO2. The FB reactor has a quartz window for visual observation, allowing the measurement of temperature and tracking the char conversion process by pyrometry with a digital camera. The method is shown to overcome the inherent limitations of other methods used in FB, such as thermocouples or pyrometry with an optical probe. Results indicate that the transfer of O-2 from the bulk gas of the bed to the surface of a char particle controls the overall rate of char conversion in O-2/N-2 and in O-2/CO2. In the latter gas mixture, the carbon consumption by gasification is significant even at a relatively low char temperature (850 degrees C). This additional carbon consumption makes the apparent char consumption rate in both atmospheres roughly equal (at the same O-2 concentration) for char temperatures below 925 degrees C, and higher in O-2/CO2 than in O-2/N-2 for char temperatures above 925 degrees C. Moreover, during the time in which the char stays in the emulsion phase, its temperature is roughly the same in both atmospheres, but when the char is in the bubble or splash zone its temperature is much higher than that in the emulsion phase. As a result, the difference in char conversion rate, observed in both atmospheres, is mainly controlled by the time in which the char particle is out of the emulsion phase. These results underline the importance of paying attention to the movement of a char particle through the different phases of the bed in order to improve the understanding of the oxy-fuel behavior in FB.
引用
收藏
页码:116 / 130
页数:15
相关论文
共 50 条
  • [31] Fundamental study on fuel-staged oxy-fuel fluidized bed combustion
    Duan, Lunbo
    Li, Lin
    Liu, Daoyin
    Zhao, Changsui
    [J]. COMBUSTION AND FLAME, 2019, 206 : 227 - 238
  • [32] Gaseous emissions during oxy-fuel combustion of sewage sludge in a circulating fluidized bed
    Kosowska-Golachowska, Monika
    Luckos, Adam
    Kijo-Kleczkowska, Agnieszka
    Musial, Tomasz
    Wolski, Krzysztof
    Sroda, Katarzyna
    [J]. POWDER TECHNOLOGY, 2020, 371 : 209 - 216
  • [33] The chemical mechanism of the effect of CO2 on the temperature in methane oxy-fuel combustion
    Song, Yu
    Zou, Chun
    He, Yizhuo
    Zheng, Chuguagn
    [J]. INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2015, 86 : 622 - 628
  • [34] Mechanism of CO2 and H2O Action on Char in Oxy-fuel Combustion with Wet Flue Gas Recirculation
    Li, Yukai
    Feng, Dongdong
    Sun, Shaozeng
    Zhao, Yijun
    Zhang, Wenda
    Bai, Chenxi
    [J]. ENERGY & FUELS, 2023, 37 (14) : 10721 - 10725
  • [35] Fluidized bed combustion of a single coal particle in oxy-fuel environments
    Bu, Chang-Sheng
    Zhuang, Ya-Ming
    Liu, Dao-Yin
    Chen, Xiao-Ping
    [J]. Kung Cheng Je Wu Li Hsueh Pao/Journal of Engineering Thermophysics, 2015, 36 (05): : 1143 - 1147
  • [36] Fluidized bed combustion of single coal char particles at high CO2 concentration
    Scala, Fabrizio
    Chirone, Riccardo
    [J]. CHEMICAL ENGINEERING JOURNAL, 2010, 165 (03) : 902 - 906
  • [37] A Review on the Progress of Oxy-fuel Combustion Technology in Circulating Fluidized Bed
    Ge, Chen
    Wang, Chuanhao
    Li, Shiyuan
    [J]. Kung Cheng Je Wu Li Hsueh Pao/Journal of Engineering Thermophysics, 2023, 44 (03): : 840 - 849
  • [38] Current investigation status of oxy-fuel circulating fluidized bed combustion
    Ge, Chen
    Li, Shiyuan
    Wang, Linwei
    [J]. FUEL, 2023, 342
  • [39] Combustion of single char particles from Victorian brown coal under oxy-fuel fluidized bed conditions
    Roy, Bithi
    Bhattacharya, Sankar
    [J]. FUEL, 2016, 165 : 477 - 483
  • [40] Study on N2O reduction with synthetic coal char and high concentration CO during oxy-fuel combustion
    Wang, Chang'an
    Du, Yongbo
    Che, Defu
    [J]. PROCEEDINGS OF THE COMBUSTION INSTITUTE, 2015, 35 : 2323 - 2330