Heat transfer in a tapered fluidized bed of biomass particles with pulsed gas flow

被引:22
作者
Jia, Dening [1 ]
Bi, Xiaotao [1 ]
Lim, C. Jim [1 ]
Sokhansanj, Shahab [1 ,2 ]
Tsutsumi, Atsushi [3 ]
机构
[1] Univ British Columbia, Dept Chem & Biol Engn, 2360 East Mall, Vancouver, BC V6T 1Z3, Canada
[2] Oak Ridge Natl Lab, Environm Sci Div, Oak Ridge, TN 37831 USA
[3] Univ Tokyo, Collaborat Res Ctr Energy Engn, Inst Ind Sci, Meguro Ku, 4-6-1 Komaba, Tokyo 1538505, Japan
来源
PARTICUOLOGY | 2019年 / 42卷
基金
加拿大自然科学与工程研究理事会;
关键词
Fluidized bed; Gas pulsations; Tapered column; Heat transfer; Biomass; HYDRODYNAMIC CHARACTERISTICS; SPOUTED BEDS; REGIMES; DESIGN; DRYER;
D O I
10.1016/j.partic.2018.01.007
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Bed-to-surface heat transfer of pure biomass particles in a pulsed fluidized bed with a tapered bottom section was investigated. Three biomass species - Douglas fir, pine, and switchgrass - were studied under various operating conditions. Their heat transfer coefficients were found to be closely associated with hydrodynamics dominated by gas pulsations. A higher superficial gas velocity generally yielded better gas-solid contact and higher heat transfer rates. A moderately increasing pulsation frequency promoted convective heat transfer of particles but also reduced pulsation intensity, leading to undesired flow behaviours such as channelling and partial defluidization. The study of the pulsation duty cycle revealed that, for cohesive particles, a smaller duty cycle was preferred to generate powerful pulsations to break up inter-particle forces. Moreover, a duty cycle increase allowed higher gas throughput as long as a suitable fluidization was maintained. The addition of finer particles to a coarse fraction increased particle mobility, and subsequently heat transfer, which also explained the higher heat transfer coefficients of switchgrass as it contained more fines compared with fir and pine. Experimental results in the tapered bed were also compared with those of non-tapered geometry where a 10%-20% increase in heat transfer was observed. (C) 2018 Chinese Society of Particuology and Institute of Process Engineering, Chinese Academy of Sciences. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:2 / 14
页数:13
相关论文
共 50 条
  • [21] Heat transfer in gas-solid fluidized bed with various heater inclinations
    Abid, Balasim A.
    Ali, Jamal M.
    Alzubaidi, Ayar A.
    INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2011, 54 (9-10) : 2228 - 2233
  • [22] Numerical investigation of mixing and heat transfer of mixed biomass and silica sand particles in a bubbling fluidized bed combustor
    Korkerd, Krittin
    Zhou, Zongyan
    Zou, Ruiping
    Piumsomboon, Pornpote
    Chalermsinsuwan, Benjapon
    POWDER TECHNOLOGY, 2024, 433
  • [23] Effects of the ship motion on gas-solid flow and heat transfer in a circulating fluidized bed
    Murata, Hiroyuki
    Oka, Hideyuki
    Adachi, Masaki
    Harumi, Kazuyoshi
    POWDER TECHNOLOGY, 2012, 231 : 7 - 17
  • [24] HEAT TRANSFER FROM AN IMMERSED FIXED SILVER SPHERE TO A GAS FLUIDIZED BED OF VERY SMALL PARTICLES
    Prins, Wolter
    Maziarka, Przemyslaw
    De Smedt, Jonas
    Ronsse, Frederik
    Harmsen, Jan
    Van Swaaij, Wim
    THERMAL SCIENCE, 2019, 23 : S1425 - S1433
  • [25] Systematic Study on Heat Transfer and Surface Hydrodynamics of a Vertical Heat Tube in a Fluidized Bed of FCC Particles
    Yao, Xiuying
    Zhang, Yongmin
    Lu, Chunxi
    Han, Xiao
    AICHE JOURNAL, 2015, 61 (01) : 68 - 83
  • [26] Flow pattern and heat transfer in tube banks of a simulated fluidized-bed heat exchanger
    Ozawa, M
    Umekawa, H
    Matsuda, T
    Takenaka, N
    Matsubayashi, M
    JSME INTERNATIONAL JOURNAL SERIES B-FLUIDS AND THERMAL ENGINEERING, 1998, 41 (03) : 720 - 726
  • [27] LOCAL HEAT-TRANSFER COEFFICIENTS ON THE CIRCUMFERENCE OF A TUBE IN A GAS-FLUIDIZED BED
    SUNDERESAN, SR
    CLARK, NN
    INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1995, 21 (06) : 1003 - 1024
  • [28] Experimental study on hydrodynamic characteristics of gas-solid pulsed fluidized bed
    Bizhaem, Hamed Khosravi
    Tabrizi, Hassan Basirat
    POWDER TECHNOLOGY, 2013, 237 : 14 - 23
  • [29] Heat transfer and hydrodynamics in a gas-solid fluidized bed with vertical immersed internals
    Taofeeq, Haidar
    Al-Dahhan, Muthanna
    INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2018, 122 : 229 - 251
  • [30] Influence of different parameters on the tube-to-bed heat transfer coefficient in a gas-solid fluidized bed heat exchanger
    Bisognin, Priscilla Correa
    Schramm Camara Bastos, Jaci Carlo
    Meier, Henry Franca
    Padoin, Natan
    Soares, Cintia
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2020, 147 (147)