REACTOR INTERNAL CONTINUOUS HEAT TRANSFER PROCESS FOR SO2 CONVERSION SYSTEM (Ⅰ) HEAT TRANSFER PERFORMANCE OF HEAT PIPE EMBEDDED IN PACKED DUCT
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REACTOR INTERNAL CONTINUOUS HEAT TRANSFER PROCESS FOR SO2 CONVERSION SYSTEM (Ⅰ) HEAT TRANSFER PERFORMANCE OF HEAT PIPE EMBEDDED IN PACKED DUCT
CIESC JournalIssue 6, (2002)
作者机构:
华南理工大学教育部强化传热与过程节能重点实验室
作者简介:
基金信息:
DOI:
CLC:
Online First:25 June 2002,
Published:25 June 2002
稿件说明:
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ZHANG Yajun, DENG Xianhe, XING Huawei
. REACTOR INTERNAL CONTINUOUS HEAT TRANSFER PROCESS FOR SO2 CONVERSION SYSTEM (Ⅰ) HEAT TRANSFER PERFORMANCE OF HEAT PIPE EMBEDDED IN PACKED DUCT[J]. CIESC Journal, 2002, (6).
DOI:
ZHANG Yajun, DENG Xianhe, XING Huawei
. REACTOR INTERNAL CONTINUOUS HEAT TRANSFER PROCESS FOR SO2 CONVERSION SYSTEM (Ⅰ) HEAT TRANSFER PERFORMANCE OF HEAT PIPE EMBEDDED IN PACKED DUCT[J]. CIESC Journal, 2002, (6).DOI:
REACTOR INTERNAL CONTINUOUS HEAT TRANSFER PROCESS FOR SO2 CONVERSION SYSTEM (Ⅰ) HEAT TRANSFER PERFORMANCE OF HEAT PIPE EMBEDDED IN PACKED DUCT
摘要
建立了气体横掠深埋在颗粒填料中的热管时的传热模型
并用数值方法进行求解 .此外
通过实验研究得到了传热的准数关联式
并对理论与实验结果进行了对比
为进一步进行SO2 连续换热的研究提供了基础
Abstract
Based on a reasonable hypothesis and according to the continuity equation
momentum equation
energy equation
boundary layer theory and relevant boundary condition
the mathematial model of heat transfer and fluid mechanics with fluid flowing through the heat pipe immersed in the packed bed is developed in this paper. After analogy transition and numerical calculation
the model is simplified and solved. In addition
convective heat transfer is measured experimentally with the fluid flowing through heat pipe immersed in the packed bed. After analyzing the experimental data
a heat transfer correlation is obtained. The experimental result is in agreement with the theoretical result while Re d<500. The reason why there exists a great difference between the experimental result and theoretical result while Re d>500 is discussed.