Palacios-Lorenzo María Esther, Marcos José Daniel
Energy Engineering Department, UNED, Juan Del Rosal 12, 28040, Madrid, Spain.
Heliyon. 2024 Feb 5;10(3):e25656. doi: 10.1016/j.heliyon.2024.e25656. eCollection 2024 Feb 15.
Single-effect absorption chillers are the most popular because of their low cost, despite their low COP. Among them, GAX-based AirCooled absorption chillers are very interesting because they have improved COP because of their ability to recover internal heat at low thermal lifts. This workshop analysed the ability of these types of chillers to recover internal heat at high thermal lifts by changing the pressure drop of an extra valve, a feature of the Robur absorption chiller when operating in subzero applications. The complete differential mathematical model analyses the components involved in heat supply and recovery and provides information on their operation. A thorough assessment of exergy destruction in the absorption refrigeration system was carried out. The main results show that when the chiller is driven at a temperature of 210 °C and an ambient temperature of 40 °C, a rise in the pressure drop of the additional valve, Δ, from 175 to 700 kPa causes the extension of the vapour purification process to be reduced by 13.7% in the column of distillation and by 70.6% in the rectifier. Despite the adverse effect of increase on the cooling capacity, there is no risk that the distillation column operates in weeping mode. However, this adjustment increases the internal thermal load of the generator by 26.9%. Furthermore, the mass fraction of the refrigerant flow is very similar. In addition, the occurrence of a two-phase solution flow at the input of a solution cooling absorber is the practical upper limit of Δ. The refrigerant flow in the solution cooling absorber is reduced by 21.3%. Finally, the contribution of the heat recovery loop to the total exergy destruction in the refrigeration system rises slightly by 2.7% when Δ increases due to the contribution of the vapour purification system, which increases at the expense of that of the re-boiler and the SolutionCooled absorber. The results of this study show to what extent the modified GAX-based cycle can function effectively at high thermal lifts.
单效吸收式制冷机因其成本低而最受欢迎,尽管其能效比(COP)较低。其中,基于GAX的风冷吸收式制冷机非常值得关注,因为它们能够在低热升情况下回收内部热量,从而提高了COP。本次研讨会分析了这类制冷机在高热升情况下通过改变一个额外阀门的压降来回收内部热量的能力,这是罗布尔吸收式制冷机在零下应用中运行时的一个特点。完整的微分数学模型分析了供热和热量回收过程中涉及的组件,并提供了它们的运行信息。对吸收式制冷系统中的㶲损失进行了全面评估。主要结果表明,当制冷机在210°C的温度和40°C的环境温度下运行时,额外阀门的压降Δ从175 kPa增加到700 kPa,会导致精馏塔中蒸汽净化过程的延长减少13.7%,在精馏器中减少70.6%。尽管Δ的增加对制冷量有不利影响,但精馏塔不会出现液泛运行模式的风险。然而,这种调整会使发生器的内部热负荷增加26.9%。此外,制冷剂流量的质量分数非常相似。另外,溶液冷却吸收器入口处出现两相溶液流是Δ的实际上限。溶液冷却吸收器中的制冷剂流量减少了21.3%。最后,当Δ增加时,由于蒸汽净化系统的贡献,热量回收回路对制冷系统总㶲损失的贡献略有增加2.7%,蒸汽净化系统的增加是以再沸器和溶液冷却吸收器的贡献为代价的。本研究结果表明,改进后的基于GAX的循环在高热升情况下能有效运行到何种程度。