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An experimental and numerical study of a de-fouling evaporator used in a wastewater source heat pump

机译:废水源热泵用除垢蒸发器的实验与数值研究

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One challenge of recovering heat from waste bathwater using a heat pump is the build-up of bio-fouling on the heat exchanger surfaces. To solve this problem, a novel Dry-Expansion Shell-and-Tube Evaporator (DESTE) with a de-fouling function was developed. The evaporator performance was experimentally and numerically evaluated. Experimental results show that its heat transfer capacity increased with waste-water flowrate and temperature; the coefficient of performance (COP) of heat pump increased with wastewater flowrate; and drop of wastewater temperature through DESTE enlarged with wastewater temperature. A steady-state model was also developed. The evaporator was numerically divided into 45 sections, and the wastewater and refrigerant temperatures in each section were simulated. Statistical comparisons show that the simulated results were not significantly (p > 0.05 for all cases) different from the measured results, thus, making this model useful for predicting evaporator performance at conditions when experimental measurements were difficult. Predicting results show that the heat transfer capacity of DESTE would experience three different stages and can achieve 15.5 kW; fouling would reduce evaporator heat transfer capacity, especially when its thermal resistance was higher than 2.5E-4 m~2 K W~(-1); and cleaning of the fouling could increase heat recovery, although heat transfer coefficients of the refrigerant was slightly decreased in the overheat regions.
机译:使用热泵从废水中回收热量的一个挑战是在热交换器表面积聚生物污垢。为了解决这个问题,开发了一种具有除垢功能的新型干式膨胀管壳式蒸发器(DESTE)。对蒸发器的性能进行了实验和数值评估。实验结果表明,其传热能力随废水流量和温度的升高而增加;热泵的性能系数(COP)随废水流量的增加而增加;通过DESTE产生的废水温度下降随废水温度的升高而增大。还开发了稳态模型。将蒸发器数值划分为45个部分,并模拟了每个部分中的废水和制冷剂温度。统计比较表明,模拟结果与测量结果没有显着差异(对于所有情况,p> 0.05),因此,该模型可用于预测在难以进行实验测量的条件下的蒸发器性能。预测结果表明,DESTE的传热能力将经历三个不同阶段,可达到15.5 kW;结垢会降低蒸发器的传热能力,特别是当其热阻高于2.5E-4 m〜2 K W〜(-1)时;尽管在过热区域制冷剂的传热系数略有降低,但清洁和结垢可以提高热回收率。

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