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Part iii please Project scope The size of the MED plant is 72.000 liters per day and the source of these water is the Bull

Part iii please
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Project scope The size of the MED plant is 72.000 liters per day and the source of these water is the Bull Bay area of the city it is assumed that all the impurities have the same properties as sodium chlorides. The design specification for the plant is detailed below: Parameter Value Number of elects Pressure in effects 20 inches of mercury (cm) Temperature in effects 150C Nominal output 3 m'h distillate Power delivesy 200 kW Seawater feed whater Seawater Centri 35 salt of water The partial molar enthalpy of the seawater is modelled according the equation below at 25C and 1 atmosphere = 25.015 (1 x) + 30.8055612*- 161.50632x2 + 79,0595982"* + 114831492 Uke Where is mele concentration of the salt in solution. The experimental vinal coefficient data are as follows: (Water) B-352 cm'mol 84-3052. comel (Nach B-59cmol For beating purposes, saturated steam at pressure of 60 MPa and temperature 200C will be used Deliverables As the process engincat, you are required to determine the following Generate the ble of results for partial molar enthalpy fue concentratistaging from 0.3%-50% in increments of 19 110 marks! Generate the graph for partial molar enthalpy vs mole fraction based on data generated from part) 15 marki . Determine the expression for the partial molar enthalpy for the water and sodium chloride components and deduce same concentration af 3.5% 110 marks! Determine the fugacity and fugacity coefficient of the team to be used using the viral EOS.cubic RW EOS and general corelations Compare the values obtained from the the methods 115 marks! Determine the fugacity and fugacity coefficient of the scam distillate in the first effect using the viral EOS, and general correlations Compare the values obtained from the two (2) methods [10 marks Determine the fugacity and fugacity cecilicient of the medium chloride and water in the first effect using the viral EOS. 15 mars! Compare the fagacities calculated from the RW EOS for both the heating team and the steam distillate Provide reasons for significant differences, if any, 13 marks VI

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