Abstract:SUMMARYThis work presents a mathematical model of a shell-and-tube evaporator based on mass continuity, energy conservation and heat transfer physical fundamentals. The model is formulated as a control volume combination that represents the different refrigerant states along the evaporator. Since the model is based on refrigerant and secondary fluid states prediction, it can be easily adapted for modelling any type of evaporator. The strategy of working with physical fundamentals allows the steady-and dynamic-… Show more
“…The second one, which is used to supply the evaporator with the refrigerant load, consists of a loop working with an ethylene-glycol mixture (50/50% by volume) that enables a constant pressure to be maintained in the evaporator. Further information about the auxiliary systems can be found in previous works presented by the authors [24].…”
“…The second one, which is used to supply the evaporator with the refrigerant load, consists of a loop working with an ethylene-glycol mixture (50/50% by volume) that enables a constant pressure to be maintained in the evaporator. Further information about the auxiliary systems can be found in previous works presented by the authors [24].…”
“…Plant regulation and data validation are performed by two auxiliary systems [23]. The first one is devoted to control the heat rejected in the gas-cooler, which uses water as cooling fluid, and the second one is used to supply the refrigeration load to the evaporator, which operates with an ethylene-glycol water mixture (50%/ 50% by volume) as working fluid.…”
Section: Refrigeration Plant Description and Test Proceduresmentioning
. Influence of the superheat associated to a semihermetic compressor of a transcritical CO refrigeration plant. Applied Thermal Engineering, Elsevier, 2009, 30 (4), pp.302.
“…It is therefore a good tool to understand how the condenser operates and its influence on the complete vapour compression system. This effect is analysed by comparing the theoretical response of a previously presented evaporator model [11] with the one obtained using the condenser model. …”
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