Absorption Refrigeration Cycle Essay

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The membrane contactors can be used in different components of the absorption refrigeration systems such as absorber, desorber, solution heat exchanger etc. In this section absorption refrigeration cycle configurations of the investigations reviewed in the present work are discussed. The principle of operation and the use of membrane contactors in the desorber of absorption refrigeration systems can alter the configuration of the cycle. However, the use of membrane contactors in the absorber has no significant effect on the configuration of the cycle. Ali and Schwerdt (2009 and 2010), Ali (2010a or 2010b or both), Yu et al. (2012) and Isfahani et al. (2013) or Isfahani and Moghaddam (2013) [To check] used the plates-and-frames membrane module absorber with the same configuration of the conventional single-effect water-LiBr absorption cycle as shown in Figure 1 (a). Schaal et al. (2008) and Chen et al. (2006) used the conventional configuration of the single-effect ammonia-water absorption refrigeration cycle using hollow fiber membrane module absorber as shown in Figure 1 (b). The no-conventional cycle configurations used in the investigations reviewed in this work are herein discussed.
[Randel (1932) investigated an NH3/H2O absorption refrigeration cycle employing the principle of supplementary agent for pressure equalization in the evaporator (Qué es? Not Clear). In this case the supplementary agent does not circulate with the cooling agent (What is the cooling agent? Write with your own words. Don’t try to copy full sentences) [Improve the writing style of this part]. The heat of absorption is utilized in the desorber to reduce the heat input [how?]. As shown in Figure 5, the major components of the cycle are the same as those ...

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...enters in the pervaporation membrane unit in which a membrane is employed for separation. Only the refrigerant is passed through the membrane and collected on the other side. Vacuum is created at the downstream of the membrane. The refrigerant is condensed and throttled to the evaporator to produce cooling and then is absorbed in the absorber and the cycle repeats. The schematic diagram of this cycle is shown in Figure 8. The COP of the cycle utilizing pervaporation membrane process for vapour desorption is low as compared to conventional absorption systems as pervaporation process requires very high solution feed flow rate. The authors obtained a COP of 0.06 for their prototype working on the pervaporation membrane principle, they argued that the low COP is due to the high circulation ratio as high feed flow rate is required to operate such pilot membrane module.

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