Answer :
Answer:
Check the explanation
Explanation:
Going by the question above for parta, the feed flow rate is stated to be 9072g/hr.& result is offered for part a considering the same. if the unit is kg/hr, then kindly let me know & i shall make slight modification that might be required in solution which in that case, area & steam consumption answer shall differ.
In the b part of the question, reduced flow rate is higher than the initial flow rate therefore same has been considered in gram /hr.
Kindly check the attached images below to see the step by step solution to the above question.




In this exercise we have to use the knowledge of mechanics to calculate the steamused of the solution, in this way we will have to:
a) [tex]M_S=\frac{H_S}{\lambda_S} = 8.43 KG/h[/tex] , [tex]A= 0.0526 m^2[/tex]
b) We can assume that all water shall evaporate and produd shell contain solid only.
So from the data informed in the exercise we have that:
- [tex]F= 9072 g/h[/tex]
- [tex]M_f=907,2 g/h[/tex]
- [tex]M_L=1814.4 kg/h=L[/tex]
So apply overall mass balance, will be:
[tex]F=L+V\\9072=1814.4-V\\V=7.2576 kg/h[/tex]
Now, for enthalpy balance we shall make assumption that, all liquid phase enthalphy is that heet capacity of water is constant, so the data will be:
- [tex]C=4.18 kJ/kg[/tex]
- [tex]T_c=15.6[/tex]
- [tex]P=20KPa[/tex]
- [tex]T_P=60[/tex]
So, find the enthalpy of liquid, we have;
[tex]H_L= L*C_P*(T_P-T_F)\\=(1.8144)(4.18)(60.0586-15.6)\\H_v=V*(P(t_P-T_F)+\lambda)\\=(7.2576)(4.18(60.0586-15.6)+2357.5477))H_s=H_L+H_V\\H_S= (1.8144)(4.18)(60.0586-15.6)+(7.2576)(4.18(60.0586-15.6)+2357.5477))\\=18796.051 KJ/h[/tex]
Now, we can find the mass flow rate, that will be;
[tex]M_S=\frac{H_S}{\lambda_S} = 8.43 KG/h[/tex]
Now we can find the area of evaporator, that will be:
[tex]H_S=UA=(T_S-T_P)\\A=0.0526m^2[/tex]
See more about enthalpy at brainly.com/question/7827769