The cold storage is to be maintained between $2C$ to $4C$ to preserve the processed fruit products and the cooling cycle of the pasteurization process is also operated between $2C$ to $4C.$ It is recommended that a ZB series Scroll type compressor manufactured by Emerson Climate Technologies should be used for the refrigeration system and the compressor has an isentropic efficiency of $(75+{0\mathrm{.}5}^{**}x+{0\mathrm{.}3}^{**}Y)\%.$ The meximum compressor delivery pressure should be limited to $1200$ kPa $($absolute$).$ For this delivery pressure the recommended condenser heat exchanger will have a maximum fluid frictional pressure loss of $(22-$ Y$)$ kPG$.($Note: A liquid$-$cooled plate heat exchanger ia to be used for the condenser$).$ It is recommended to use refrigerant R$134$a for this system. The refrigerant will be cooled $(3\mathrm{.}8+0\mathrm{.}2**y.$ C below its saturation temperature by the time it leaves the condenser. The refrigerant leaves the evaporator at a pressure of $240$ kPa $($absolute$)$ and temperature of $(5\mathrm{.}8-{0\mathrm{.}2}^{***}x)$ CC above its saturation temperature. The pressure drop in the evaporator is $(18+vvv)kPa.$ The water demand varies throughout the day and is provided in excel file as a function of $x$ and $Y$ along with the rate of cooling demand for cold storage and pasteurization. $x=7,Y=8.$

$\backslash$table$[[$Time$,\backslash$table$[[$Cooling demand of$],[$cold storage$]],\backslash$table$[[$Cooling demand of$],[$pasteurizer$]],\backslash$table$[[$Hot water for$],[$Peeling and$],[$Juicing process$]],\backslash$table$[[$Water demand for steam$],[$generation$]]],[9$am to $10$am$,$kW$,$kW$,k\frac{g}{s},k\frac{g}{s}$