Capacity 2 TR ; Concentration of LiBr and enthalpy values for weak solution leaving| generator 0.68 and
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Capacity 2 TR ; Concentration of LiBr and enthalpy values for weak solution leaving| generator 0.68 and 21 kJ/kg respectively; Concentration of LiBr and enthalpy values for strong solution leaving absorber = 0.58 and - 55 kJ/kg respectively. Temperature of water leaving condenser 40°C; Enthalpy of steam leaving evaporator = 2508 kJ/kg ; Specific heat of water = 4.2 kJ/kg K. Determine the mass flow rates of strong and weak solutions in kg/min and the heat transfer rates in the generator and the absorber in kJ/min
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