装有管状传热装置的主动建筑热保护围护结构中的静止传热

IF 1 Q4 ENERGY & FUELS
M. S. Purdin, R. Magomedova
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引用次数: 0

摘要

主动热保护围护结构(ATPE)是继“暖地板”和“暖墙”系统之后出现的一种用于保持建筑和结构温度条件的新型系统。本文论述了管状换热装置(THTDs)的热特性研究与实际应用的相关性。建立了ATPE传热问题的一维解析解和二维数值解。对于二维解,给出了考虑热分布层(HDL)和保温层(TIL)之间的共轭传热的数值格式以及建模过程。为了验证结果,进行了数值计算和解析计算,并对不同ATPE版本的热分布层温度分布进行了比较。一维解析解与二维数值计算结果吻合较好。确定了高密度脂蛋白及其表面产生的温差,以及THTD温度过热。提出了一种管式传热装置过热计算方法,进行了实际计算。估计了热防护结构内表面达到标准化温度分布参数时的Biot数值。结果表明,采用装有管状换热装置的ATPE,可以使热载体温度最接近室内温度。这意味着,建筑物和结构的供热系统可以在不显著增加热损失的情况下,特别是在使用低等级热源的情况下,以及在热转换和储存期间,在火用和能源方面更有效。给出了计算THTD放置间距、最低HDL温度和THTD比功率的公式。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Stationary Heat Transfer in an Active Building Thermal Protection Envelope Equipped with Tubular Heat Transfer Devices

Stationary Heat Transfer in an Active Building Thermal Protection Envelope Equipped with Tubular Heat Transfer Devices

Stationary Heat Transfer in an Active Building Thermal Protection Envelope Equipped with Tubular Heat Transfer Devices

An active thermal protection envelope (ATPE) is a new kind of systems for maintaining temperature conditions in buildings and structures, which emerged after the “warm floor” and “warm walls” systems. The article substantiates the relevance of studying the thermal characteristics and practical application of an ATPE comprising tubular heat transfer devices (THTDs). A 1D analytical solution and a 2D numerical solution of the heat transfer problem in an ATPE are developed. For the 2D solution, a numerical scheme that takes into account conjugate heat transfer between the heat distribution layer (HDL) and thermal insulating layer (TIL), as well as the modeling procedure, are presented. For verifying the results, numerical and analytical calculations were carried out, and the temperature distributions in the heat distribution layer for one of the ATPE versions were compared. The 1D analytical solution is in good agreement with the 2D numerical calculation results. The temperature differences arising in the HDL and at its surface, as well as the THTD temperature overheating are determined. A tubular heat transfer device overheating calculation method for carrying out practical computations is proposed. The Biot number value at which the standardized temperature distribution parameters at the thermal protection structure inner surface are achieved is estimated. A conclusion is drawn that, owing the use of an ATPE equipped with tubular heat transfer devices, the heat carrier temperature can be approached closest to the indoor temperature. This means that the heat supply systems of buildings and structures can be made more efficient in exergetic and energy respects at the expense of insignificantly larger heat losses, especially in the case of using low-grade heat sources, and also during heat transformation and storage. Formulas for calculating the THTD placement pitch, minimal HDL temperature, and THTD specific power are presented.

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来源期刊
CiteScore
1.30
自引率
20.00%
发文量
94
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