Jibin,
1. You can enter the individual mole fractions or weight fractions for the Shell side fluid if you know the balance of both the liquid components, by adding both components - ie. the fluid and water as well in the components tab just below grid properties tab. If you enter the values, you can see the respective specific properties of the overall shell side fluid. The overall fluid properties will then be inclusive of the water fraction as well, but you will be able to see only the combined fluid properties.
2. Otherwise you can separately use the standard mixing rules for mixing of the individual properties in proportion of their respective mole fractions / wt fractions depending on whether the specific property is based on moles or weight (Eg. enthalpy per mole or enthalpy per kg). and then enter the calculated combined fluid properties by yourself in htri.
But then you will have to separately account for evaporation of the fluid and evaporation of water and their individual vapour properties which will be a tedious task.
3. I would suggest another option is to consider using a process simulator like hysys where you can enter respective fluids, conditions and then calculate the properties from that for the mixed fluid. Then you can enter the mixed fluid properties in place of the shell side fluid.
4. Your water quantity is relatively very low in percentage terms.
If your flow is relatively low you can neglect it.
Regards,
Shantanu
Edited by shantanuk100, 03 December 2015 - 08:18 PM.