Heat transfer for gas flow through a catalytic fixed bed reactor characterized by small tube/particle diameter ratios

被引：0
|
作者：
Bauer, M [1 ]
Adler, R
机构：
[1] Bayer AG, PF PT IT VE, D-51368 Leverkusen, Germany
[2] Univ Halle Wittenberg, FB Ingenieurwissensch, D-06099 Halle Saale, Germany
来源：
CHEMIE INGENIEUR TECHNIK | 2002年 / 74卷 / 06期
关键词：
D O I：
10.1002/1522-2640(200206)74:6<804::AID-CITE804>3.0.CO;2-3
中图分类号：
TQ [化学工业];
学科分类号：
0817 ;
摘要：
引用
收藏
页码：804 / 808
页数：5
相关论文
共 50 条
  • [21] CATALYTIC COMBUSTION OF NATURAL-GAS IN A FIXED-BED REACTOR WITH FLOW REVERSAL
    SAPUNDZHIEV, C
    CHAOUKI, J
    GUY, C
    KLVANA, D
    CHEMICAL ENGINEERING COMMUNICATIONS, 1993, 125 : 171 - 186
  • [22] Particle Flow and Heat Transfer in Fluidized Bed-in-Tube Solar Receivers
    Le Gal, Alex
    Grange, Benjamin
    Gueguen, Ronny
    Donovan, Michael
    Peroy, Jean-Yves
    Flamant, Gilles
    INTERNATIONAL CONFERENCE ON CONCENTRATING SOLAR POWER AND CHEMICAL ENERGY SYSTEMS (SOLARPACES 2019), 2020, 2303
  • [23] Flow and heat transfer performance and field synergy analysis of structured packed beds with low tube-to-particle diameter ratios
    Cao X.
    Yu H.
    Liu Y.-F.
    Yan C.-L.
    Li Q.-L.
    Gao Xiao Hua Xue Gong Cheng Xue Bao/Journal of Chemical Engineering of Chinese Universities, 2019, 33 (06): : 1386 - 1393
  • [24] A numerical study on the residence time distribution in low and moderate tube/particle diameter ratio fixed bed reactor
    Atmakidis, Theodoros
    Kenig, Eugeny Y.
    PRES'09: 12TH INTERNATIONAL CONFERENCE ON PROCESS INTEGRATION, MODELLING AND OPTIMISATION FOR ENERGY SAVING AND POLLUTION REDUCTION, PTS 1 AND 2, 2009, 18 : 581 - 586
  • [25] A Simplified Method for Modeling of Pressure Losses and Heat Transfer in Fixed-Bed Reactors with Low Tube-to-Particle Diameter Ratio
    Swieboda, Tymoteusz
    Krzyzynska, Renata
    Bryszewska-Mazurek, Anna
    Mazurek, Wojciech
    Wysocka, Alicja
    ENERGIES, 2021, 14 (03)
  • [26] Heat transfer in fixed beds at very low (<4) tube-to-particle diameter ratio
    Dixon, AG
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (08) : 3053 - 3064
  • [27] Influence of the packing structure on the flow through packed beds with small cylinder diameter to particle diameter ratios
    van der Merwe, W. J. S.
    du Toit, C. G.
    Kruger, J-H
    NUCLEAR ENGINEERING AND DESIGN, 2020, 365 (365)
  • [28] The characteristics of gas–solid flow and wall heat transfer in a fluidized bed reactor
    Hang Seok Choi
    Dietrich Meier
    Heat and Mass Transfer, 2012, 48 : 1513 - 1524
  • [29] A numerical study on gas-to-particle and particle-to-particle heat transfer in a conical fluidized bed reactor
    Hashim, Mohamed Y.
    Abdelmotalib, Hamada M.
    Kim, Jong Seok
    Ko, Dong Guk
    Im, Ik-Tae
    JOURNAL OF MECHANICAL SCIENCE AND TECHNOLOGY, 2020, 34 (06) : 2391 - 2402
  • [30] Heat transfer and particle behavior around horizontal tube bundle in gas fluidized bed
    Miyamoto, Masahide
    Katoh, Yasuo
    Idei, Yasumasa
    Nippon Kikai Gakkai Ronbunshu, B Hen/Transactions of the Japan Society of Mechanical Engineers, Part B, 1993, 59 (560): : 1291 - 1297
12345