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Experimental investigation of the effect of generator temperature on the performance of solution transportation absorption chiller

机译:发生器温度对溶液输送吸收式冷水机组性能影响的实验研究

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It is effective to recover waste heat to reduce primary energy consumption. From this point of view, we proposed and examined a new idea of heat transportation using ammonia-water as the working fluid in the system named the Solution Transportation Absorption chiller (STA). As waste heat sources are not necessarily located close to areas of heat demand, conventionally, absorption chillers are located on heat source side and produce chilled water that is transported to heat demand side through pipelines with an insulation. In contrast, the proposed system STA divides an absorption chiller into two parts. The generator and the condenser are located on heat source side while the evaporator and the absorber are on heat demand side. Both the conventional system and STA system satisfy the same boundary condition of heat recovery and heat supply to the demand side, STA can work for transferring thermal energy as the conventional system does even though the temperature of the media is ambient without an insulation. Our previous studies of the STA were based on the experimental investigation with the STA facility where the cooling power was 90kW (25.6 refrigeration ton) at the generator temperature 120°C from 0m (normal absorption chiller) to 1000m. Thus, the Coefficient of Performance (COP) of STA was found to have almost the same value of 0.65 with conventional absorption chillers without depending on the transportation distances. The objective of this study is to examine the effect of generator temperature from 100°C to 120°C on the performance of solution transportation of ammonia-water solution, because the generator temperature is directly linked to the waste heat temperature, so its effect needs to be investigated. The experimental facility tested the performance with 0m (normal absorption chiller), 200m and 500m distance. The results indicate that the effect of the generator temperature and solution transportation distances showed no significant on the COP.
机译:有效回收废热以减少一次能源消耗。从这一观点出发,我们提出并研究了一种新的利用氨水作为工作流体的热传输概念,即溶液传输吸收冷却器(STA)。由于废热源不一定位于热需求区域附近,因此,吸收式制冷机通常位于热源侧,并产生冷却水,该冷却水通过具有绝缘层的管道输送到热需求侧。相反,所提出的系统STA将吸收式冷却器分为两部分。发生器和冷凝器位于热源侧,而蒸发器和吸收器位于热需求侧。常规系统和STA系统都满足相同的热回收和向需求侧供热的边界条件,即使介质的温度处于环境温度且没有隔热层,STA也可以像常规系统一样工作以传递热能。我们之前对STA的研究基于对STA设施的实验研究,该设施在发电机温度为120°C的情况下,从0m(正常吸收式制冷机)到1000m,冷却功率为90kW(25.6制冷吨)。因此,发现STA的性能系数(COP)与传统的吸收式制冷机几乎具有0.65的值,而与输送距离无关。这项研究的目的是检验发生器温度从100°C到120°C对氨水溶液的溶液传输性能的影响,因为发生器温度与废热温度直接相关,因此需要对其产生影响有待调查。实验设备在0m(常规吸收式制冷机),200m和500m的距离下测试了性能。结果表明,发生器温度和溶液输送距离对COP的影响不显着。

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