Q$2)$ A chemical engineer works at a petrochemical company in Turkey. In this company, methanol

synthesis by catalytic dehydrogenation of carbon dioxide was produced by using flue gas as a

feedstock. A chemical engineer's demand is that she$/$he will build an adiabatic cooling tower for

utilization of wastewater which comes from the condensers in the plant. She$/$He wants a help from

you at the calculation parts and answer the following questions.

The stream of cooled water will be returned to the condensers from the cooling tower

with the same flowrate. Some data needed are as follows:

Exiting wastewater stream from condensers at $50C$ enters a cooling tower with a mass

flowrate of $20,000k\frac{g}{h}.$ Make$-$up water is added from water reservoir at $25C.$ Atmospheric air

enters the cooling tower at $17C$ of wet bulb temperature with $50\%$ relative humidity. The

volumetric flowrate of air into the cooling tower is $26,190\frac{m^3}{h}.$ Desired exit conditions of air at

top section is $60\%$ relative humidity; and the exit dry bulb temperature of air should not be more

than $16C$ of the inlet dry bulb temperature of air. Additionally, atmospheric pressure is $1$atm.

a$)$ Plot the flow diagram of the cooling tower process. $(10$ pt$.)$

b$)$ Write mass and energy balances at steady state conditions $($state your assumptions$).$

$(20$ pt$.)$

c$)$ Determine the temperature of the cooled liquid water exiting cooling tower. $(40$ pt$.)$

d$)$ Find the efficiency of the tower and state five factors that affect the cooling tower

efficiency. $(10$ pt$.)$

Table $1$: Specific enthalpy values of liquid water at $1$atm. SOLVE BY HAND AND DO NOT COPY PLEASE!