2022
DOI: 10.1016/j.energy.2022.124127
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Renewable energy-based cascade adsorption-compression refrigeration system: Energy, exergy, exergoeconomic and enviroeconomic perspectives

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Cited by 31 publications
(16 citation statements)
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“…where U l,Tank is the overall heat-transfer coefficient between the tank surface area and the surroundings and is assumed to be 0.83 W m −2 °C−1 , 29 and A Tank (m 2 ) is the overall surface area. 29 The maximum temperature that the tank can provide, T Ex,in,max , (°C), is obtained from the energy balance of the tank during 24 hours of operation, and is calculated as follows:…”
Section: Me-mvc Performance Parametersmentioning
confidence: 99%
See 1 more Smart Citation
“…where U l,Tank is the overall heat-transfer coefficient between the tank surface area and the surroundings and is assumed to be 0.83 W m −2 °C−1 , 29 and A Tank (m 2 ) is the overall surface area. 29 The maximum temperature that the tank can provide, T Ex,in,max , (°C), is obtained from the energy balance of the tank during 24 hours of operation, and is calculated as follows:…”
Section: Me-mvc Performance Parametersmentioning
confidence: 99%
“…The capital recovery factor, CRF, is used to annualize the total costs 36 and can be calculated from ref. 37:…”
Section: Me-mvc Cost Analysismentioning
confidence: 99%
“…The main characteristics of silica gel/water pair are listed in Table 2. The modified Freundlich equation can be used to correlate the adsorption isotherms of the RD silica gel/water pair, as shown below [21]:…”
Section: Isotherms and Kinetics Of Adsorption Working Pairmentioning
confidence: 99%
“…The condenser and evaporator energy balances are estimated using Equations ( 18) and ( 19) to estimate their temperatures 45 d dt…”
Section: Thermal Performance Of the Evaporator And Condensermentioning
confidence: 99%