低容量供排气通风机组的热回收式换热器-利用器热力学模式

V. A. Zafatayeu, T. I. Karaliova
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引用次数: 0

摘要

现有建筑围护结构的热防护等级的提高,由于需要符合现行建筑热工程规范的要求,导致建筑热平衡中由于渗透和排风运行造成的热损失部分增加。在用尽了通过改变容积规划解决方案和隔热建筑围护结构来降低能源成本的技术措施的可能性之后,进一步降低热消耗水平应该与使用二次和可再生资源潜力有关。本文以小容量机组为例,介绍了利用排风热势对建筑物强制排风系统送风进行加热的技术经济可行性评价结果。针对一种以多片连续板为翅片的肋状热管为翅片的逆流式空气-空气回热式热器,建立了排风中所含水蒸气相变为液态时,排风物理性质变化对换热器-热器性能及其效率特性的影响。在(-26)至(+8)°C的送风温度范围内确定热交换条件(无冷凝水,换热器-利用器部分有冷凝水,整个换热器-利用器有冷凝水,并有结冰的风险),用于其运行的三种变体,其排气和送风标称量的平衡以及两种不平衡。为了找到供气和排气温度的可能组合,已经研究了不平衡的变体,在这种组合下,在热利用器的整个体积中,排气流中的水蒸气不会相变到液态,这将消除收集和去除冷凝水并防止其冻结的措施的需要。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Recuperative Heat Exchanger-Utilizer Thermodynamic Modes in Low Capacity Supply-and-Exhaust Ventilation Unit
The increase in the thermal protection level of the existing buildings enclosing structures, due to the need to comply with the current norms of building heat engineering requirements, leads to increasing in the part of heat losses in the thermal balance of a building due to infiltration and exhaust ventilation operation. After exhaustion of the possibilities for the implementation of technical measures to reduce energy costs by changing in volumetric planning solutions and insulating building envelopes further decreasing heat consumption level should be associated with the use of the secondary and renewable resources potential. The paper presents the results of assessing the technical and economic feasibility of using the exhaust air thermal potential for heating the supply air in the forced supply-and-exhaust ventilation system of a building taking as a low-capacity unit as an example. For a counterflow air-to-air recuperative type heat utilizer finned with ribbed heat pipes in the form of a plurality of continuous sheets, the influence of changes in the physical properties of the exhaust air during the phase transition of the water vapor contained in it into a liquid state on the heat exchanger-utilizer performance and characteristics of its efficiency has been established. The conditions of heat exchange are determined (without condensate, with condensate in the part of the heat exchanger-utilizer, with condensate in the entire heat exchanger-utilizer and with the risk of icing) in the supply air temperature range from (–26) to (+8) °C for three variants of its operation with a balance of the nominal amount of exhaust and supply air and with two variants of imbalance. Variants with imbalances have been investigated in order to find possible combinations of supply and exhaust air temperatures, at which there would be no phase transition of water vapor in the exhaust air flow to the liquid state in the entire volume of the heat utilizer, which would eliminate the need for measures to collect and remove condensate and preventing it from freezing.
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