采用不同的方法模拟了蓄热式通风机的热回收效果

D. Vakulenko, V. Mileikovskyi
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引用次数: 1

摘要

今天的建筑应设计为能效等级不低于c。这需要通风与热回收。在市场上,有不同的紧凑型热回收通风机组分散通风。蓄热式通风机是利用废气热回收进行有效通风的一个有前途的领域。它们循环运行,用于空气的吸入和排出。这些类型的通风机应该在一个阻塞对中工作-每个对中一个用于输入,一个用于输出。否则,效果会下降。为提高“双新鲜”通风口蓄热式通风机陶瓷蓄热器的运行效率,建立了其数学模型。在以往的工作中,基于两种不同的方法,对蓄热器的运行进行了模拟。第一个使用M. Mikheev的努塞尔数公式。二是利用SolidWorks Flow simulation进行计算流体动力学仿真。模拟得到的效率系数有显著的差异-高达66.5%。这项工作的目的是寻找替代方法,以充分确定呼吸机的效率。使用与“Novyi spravochnik khimika i tekhnologa”不同的公式进行数学模拟。protesessy i paraty khimicheskikh technologii”。这个公式考虑了格拉什夫数。得到的值与之前的值有很大的不同——最多相差两倍。在文献中没有关于确定模拟中使用的努塞尔数的实验条件的信息。因此,我们不能假设,哪种方法更接近陶瓷蓄热器的条件。有必要进行实验研究,以确定蓄热式换热器的效率。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Simulation the effectiveness of heat recovery of the regenerative ventilator using different approaches
Today buildings should be designed for energy efficiency class not less than C. This requires ventilation with heat recovery. On the market, there are different compact heat recovery ventilation units for decentralized ventilation. Regenerative ventilators represent a promising area of effective ventilation with exhaust air heat recovery. They operate cyclically for the inlet and outlet of air. These kinds of ventilators should work in a blocked pair(s) – one for input and one for output in each pair. If not, the effectiveness will decrease. A mathematical model of the ceramic heat regenerator in the regenerative ventilator “Twin Fresh” by Vents has been created to improve the efficiency of its operation. In previous works, on the basis of two different approaches, the operation of the heat regenerator was simulated. The first one uses M. Mikheev’s formula for the Nusselt number. The second one is computational fluid dynamic simulation by SolidWorks Flow Simulation. The efficiency coefficients obtained as a result of the simulation had a significant difference – up to 66.5 %. The aim of the work is to find alternative methods for adequately determining the efficiency of the ventilator. A mathematical simulation was performed using a different formula from “Novyi spravochnik khimika i tekhnologa. Protsessy i aparaty khimicheskikh tekhnologii”. This formula takes into account the Grashof number. Values obtained are significantly different from both previous ones – up to two times. There is no information in the literature about the experimental conditions for determining the Nusselt number, which was used in the simulation. Therefore, we can’t assume, what approach is closer to the conditions of the ceramic regenerator. There is a need to conduct experimental studies to determine the efficiency of the regenerative heat exchanger.
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