Surface Morphology and Porosity Evolution of CWS Spheres from a Bench-Scale Fluidized Bed

被引:28
|
作者
Wang, Hui [1 ]
Guo, Shuai [1 ]
Yang, Li [1 ]
Guo, Yongjun [1 ]
Jiang, Xiumin [2 ]
Wu, Shaohua [1 ]
机构
[1] Harbin Inst Technol, Sch Energy Sci & Engn, Harbin 150001, Peoples R China
[2] Shanghai Jiao Tong Univ, Sch Mech Engn, Shanghai 200240, Peoples R China
关键词
WATER SLURRIES; COMBUSTION; PARTICLES; ADSORPTION; MOISTURE; DROPLET;
D O I
10.1021/ef502923t
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
Fluidization suspension combustion technology is an effective method to utilize coal water slurry (CWS) as fuel in industrial boilers. The evolution of surface morphology and pore structure of CWS spheres under fluidization suspension combustion is studied. A bench-scale fluidized bed was used for combustion of CWS spheres with a bed temperature of 850 degrees C, fluidization number of 4, and bed height of 90 him. After 15, 30, and 45 s of combustion, the samples were removed from the bed for scanning electron microscope (SEM) and N-2 adsorption tests. The combustion mechanism of CWS spheres in the fluidization-suspension combustion state is discussed. The results show that after 15 s, the CWS spheres burst due to volatile release, and some particles fragmented to produce a large number of pores. Thus, the specific surface area and volume of pores increased rapidly. After 30 s, combustion occurred mainly at the exterior surface of CWS spheres and appeared as layer by layer inward combustion. This was confirmed by the fact that the specific surface area and volume did not change. After 45 s, as combustion proceeded, the flame front entered the interior surface through pores, and burnt the interior framework to make the pores collapse. Thus, the specific surface area and volume of pores decreased rapidly. In the whole combustion process, the fractal dimension first increased and then decreased, which demonstrates that the pore structure had experienced a process that went from complicated to simple.
引用
收藏
页码:3428 / 3437
页数:10
相关论文
共 50 条
  • [41] Physicochemical Properties and Gasification Reactivity of the Ultrafine Semi-char derived from a Bench-scale Fluidized Bed Gasifier
    ZHANG Yukui
    ZHANG Haixia
    ZHU Zhiping
    NA Yongjie
    LU Qinggang
    JournalofThermalScience, 2017, 26 (04) : 362 - 370
  • [42] Physicochemical properties and gasification reactivity of the ultrafine semi-char derived from a bench-scale fluidized bed gasifier
    Yukui Zhang
    Haixia Zhang
    Zhiping Zhu
    Yongjie Na
    Qinggang Lu
    Journal of Thermal Science, 2017, 26 : 362 - 370
  • [43] Bench-Scale Fluidized-Bed Fast Pyrolysis of Peanut Shell for Bio-Oil Production
    Zhang, Changsen
    Zhang, Ruiqin
    Li, Xipeng
    Li, Yuewei
    Shi, Wen
    Ren, Xiantao
    Xu, Xingmin
    ENVIRONMENTAL PROGRESS & SUSTAINABLE ENERGY, 2011, 30 (01) : 11 - 18
  • [44] Fast Pyrolysis of Corn Straw for Bio-oil Production in a Bench-scale Fluidized Bed Reactor
    Liu, R.
    Deng, C.
    Wang, J.
    ENERGY SOURCES PART A-RECOVERY UTILIZATION AND ENVIRONMENTAL EFFECTS, 2010, 32 (01) : 10 - 19
  • [45] Nonintrusive Uncertainty Quantification of Computational Fluid Dynamics Simulations of a Bench-Scale Fluidized-Bed Gasifier
    Gel, Aytekin
    Shahnam, Mehrdad
    Musser, Jordan
    Subramaniyan, Arun K.
    Dietiker, Jean-Francois
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2016, 55 (48) : 12477 - 12490
  • [46] Ash transformations during combustion of meat-, bonemeal, and RDF in a (bench-scale) fluidized bed combustor
    Öhman, M
    Nordin, A
    Lundholm, K
    Boström, D
    Hedman, H
    Lundberg, M
    ENERGY & FUELS, 2003, 17 (05) : 1153 - 1159
  • [47] Experimental investigation of pyrolysis of rice straw using bench-scale auger, batch and fluidized bed reactors
    Nam, Hyungseok
    Capareda, Sergio C.
    Ashwath, Nanjappa
    Kongkasawan, Jinjuta
    ENERGY, 2015, 93 : 2384 - 2394
  • [48] Comparison of Different Natural Sorbents for Removing CO2 from Combustion Gases, as Studied in a Bench-Scale Fluidized Bed
    Ives, M.
    Mundy, R. C.
    Fennell, P. S.
    Davidson, J. F.
    Dennis, J. S.
    Hayhurst, A. N.
    ENERGY & FUELS, 2008, 22 (06) : 3852 - 3857
  • [49] Numerical Studies of the Gas-Solid Hydrodynamics at High Temperature in the Riser of a Bench-Scale Circulating Fluidized Bed
    Hodapp, Maximilian J.
    Ramirez-Behainne, Jhon J.
    Mori, Milton
    Goldstein, Leonardo, Jr.
    INTERNATIONAL JOURNAL OF CHEMICAL ENGINEERING, 2012, 2012
  • [50] Comparison between coal gasification rate in bench-scale fluidized bed coal gasifier and those in pilot plant
    Fujioka, Y
    Shin, JW
    KAGAKU KOGAKU RONBUNSHU, 1996, 22 (03) : 446 - 457