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Experimental study of an ammonia-water bubble absorber using a plate heat exchanger for absorption refrigeration machines

机译:板式换热器用于吸收式制冷机的氨水气泡吸收器的实验研究

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The development of absorption chillers activated by renewable heat sources has increased due mainly to the increase in primary energy consumption that causes problems such as greenhouse gases and air pollution among others. These machines, which could be a good substitute for compression systems, could be used in the residential and food sectors which require a great variety of refrigeration conditions. Nevertheless, the low efficiency of these machines makes it necessary to enhance heat and mass transfer processes in the critical components, mainly the absorber, in order to reduce their large size. This study used ammonia-water as the working fluid to look at how absorption takes place in a plate heat exchanger operating under typical conditions of absorption chillers, driven by low temperature heat sources. Experiments were carried out using a corrugated plate heat exchanger model NB51, with three channels, where ammonia vapor was injected in bubble mode into the solution in the central channel. The results achieved for the absorption flux were in the range of 0.0025-0.0063 kg m{sup}(-2) s{sup}(-1), the solution heat transfer coefficient varied between 2.7 and 5.4 kWm{sup}(-2) K{sup}(-1) the absorber thermal load from 0.5 to 1.3 kW. In addition, the effect of the absorber operating conditions on the most significant efficiency parameters was analyzed. The increase in pressure, solution and cooling flow rates positively affect the absorber performance, on the other hand an increase in the concentration, cooling, and solution temperature negatively affects the absorber performance.
机译:由可再生热源驱动的吸收式制冷机的开发已经增加,这主要是由于一次能源消耗的增加,这引起了诸如温室气体和空气污染等问题。这些机器可以很好地替代压缩系统,可用于需要多种制冷条件的住宅和食品行业。然而,这些机器的低效率使得有必要增强主要部件(主要是吸收器)中的传热和传质过程,以减小其大尺寸。这项研究使用氨水作为工作流体,以研究在板式换热器中吸收是如何发生的,该板式换热器在由低温热源驱动的典型吸收式冷却器条件下运行。使用具有三个通道的波纹板式热交换器NB51进行实验,其中氨气以气泡模式注入到中央通道的溶液中。吸收通量的结果在0.0025-0.0063 kg m {sup}(-2)s {sup}(-1)的范围内,溶液的传热系数在2.7至5.4 kWm {sup}(-2)之间变化。 )K {sup}(-1)吸收器的热负荷为0.5到1.3 kW。另外,分析了吸收器工作条件对最重要的效率参数的影响。压力,溶液和冷却流速的增加对吸收器的性能产生积极影响,另一方面,浓度,冷却和溶液温度的增加对吸收器的性能产生负面影响。

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