On the agglomeration tendency of carbonaceous fuels in fluidized beds

被引:8
|
作者
Urciuolo, M. [1 ]
Solimene, R. [1 ]
Ammendola, P. [1 ]
Krusch, S. [2 ]
Scherer, V. [2 ]
Salatino, P. [3 ]
Chirone, R. [1 ]
Senneca, O. [1 ]
机构
[1] CNR, Ist Ric Combust, Naples, Italy
[2] Ruhr Univ, Dept Energy Plant Technol, Bochum, Germany
[3] Univ Federico II, DICMAPI, Naples, Italy
关键词
Coal; Fluidized beds; Pyrolysis; Agglomeration; Swelling; Petroleum residues; PARTICLE AGGLOMERATION; COMBUSTION; PYROLYSIS; COAL; GASIFICATION; DEFLUIDIZATION;
D O I
10.1016/j.fuel.2020.118187
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
Single particle pyrolysis and combustion experiments have been carried out in a lab scale fluidized bed reactor at temperatures of 600-850 degrees C. The behavior of three different fuels is compared: a bituminous coal (Auguste Victoria), a typical bitumen used in the cement industry, a carbon rich solid waste from the refinery industry, characterized by a very high content of metals. The bituminous coal and the refinery waste particles, during the pyrolysis stage, produce interesting carbon-sand aggregates. The outer shell of these aggregates is constituted by quartz sand particles embedded in a carbon matrix. The aggregates are hollow inside. The size of the cavity is comparable with that of the original coal particles, while the outer shell is larger. The increase of particle size due to aggregate formation slows down the combustion rate. For bitumen, no carbon-sand aggregates are observed. The relations between the fuel properties and aggregates formation are discussed, in particular the chemical composition and the pyrolysis kinetics are examined. It is concluded that heavy/tarry species formed in the early pyrolysis stages are most likely responsible for the capture of the sand particles and formation of aggregates.
引用
收藏
页数:11
相关论文
共 50 条
  • [31] Agglomeration tendency during top-spray fluidized bed coating with gelatin and starch hydrolysate
    Dewettinck, K
    Messens, W
    Deroo, L
    Huyghebaert, A
    FOOD SCIENCE AND TECHNOLOGY-LEBENSMITTEL-WISSENSCHAFT & TECHNOLOGIE, 1999, 32 (02): : 102 - 106
  • [32] The role of kaolin in prevention of bed agglomeration during fluidized bed combustion of biomass fuels
    Öhman, M
    Nordin, A
    ENERGY & FUELS, 2000, 14 (03) : 618 - 624
  • [33] Reduced bed agglomeration by co-combustion biomass with peat fuels in a fluidized bed
    Lundholm, K
    Nordin, A
    Öhman, M
    Boström, D
    ENERGY & FUELS, 2005, 19 (06) : 2273 - 2278
  • [34] G/S reactor models - packed beds, bubbling fluidized beds, turbulent fluidized beds and circulating (fast) fluidized beds
    Levenspiel, O
    POWDER TECHNOLOGY, 2002, 122 (01) : 1 - 9
  • [35] A novel technique for "in-situ" characterization of devolatilization rate of solid fuels in fluidized beds
    Solimene, R.
    Chirone, R.
    Marzocchella, A.
    Salatino, P.
    Proceedings of the 18th International Conference on Fluidized Bed Combustion, 2005, : 287 - 299
  • [36] Simulation of NOx Emission in Circulating Fluidized Beds Burning Low-grade Fuels
    Gungor, Afsin
    ENERGY & FUELS, 2009, 23 (5-6) : 2475 - 2481
  • [37] Polyolefin Pyrolysis in Multilayer Fluidized Beds: An Innovative Approach to Obtain Valuable Alternative Fuels
    Zukowski, Witold
    Leski, Krystian
    Berkowicz-Platek, Gabriela
    Wrona, Jan
    ENERGIES, 2024, 17 (05)
  • [38] Experimental Investigation of Particle Size Effect on Agglomeration Behaviors in Gas-Solid Fluidized Beds
    Wang, Jingdai
    Shi, Qiang
    Huang, Zhengliang
    Gu, Yubin
    Musango, Lungu
    Yang, Yongrong
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2015, 54 (48) : 12177 - 12186
  • [39] Investigating Agglomeration Behaviors in High Temperature Gas-Solid Fluidized Beds with Liquid Injection
    Shi, Qiang
    Li, Shaoshuo
    Tian, Sihang
    Huang, Zhengliang
    Yang, Yao
    Liao, Zuwei
    Sun, Jingyuan
    Wang, Jingdai
    Yang, Yongrong
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2018, 57 (15) : 5482 - 5494
  • [40] Review of Particle Physics and Chemistry in Fluidized Beds for Development of Comprehensive Ash Agglomeration Prediction Models
    Khadilkar, Aditi B.
    Rozelle, Peter L.
    Pisupati, Sarma V.
    ENERGY & FUELS, 2016, 30 (05) : 3714 - 3734