A forward-feed double-effect evaporator, having 10 m? of heating surface in each effect, is used to kg of caustic soda solution from 10 per cent by mass to 30%. During a particular run, concentrate 1 kN when the feed is at 373 kelvin (K), the pressures in the two calandrias are 375 and 180 respectively, while the condenser operates at 30 kN For these conditions, calculate: m2 (a) the load on the condenser. (b) the steam economy c) the overall heat transfer coefficient in each effect. Would there have been any advantages in using backward feed in this case? Heat losses to the surroundings are negligible. Concentration Boiling point rise Specific heat capacity Heat of dilution, kJ/kg wt % deg K kJ/kg K 10 1.6 3.85 20 6.1 3.72 2.3 30 15.0 3.64 9.3 50 41.6 3.22 2.2

Elements Of Electromagnetics
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Author:Sadiku, Matthew N. O.
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A forward-feed double-effect evaporator, having 10 m2 of heating surface in each effect, is used to
kg
concentrate 1 of caustic soda solution from 10 per cent by mass to 30%. During a particular run,
kN
when the feed is at 373 kelvin (K), the pressures in the two calandrias are 375 and 180-
respectively,
m2
while the condenser operates at 30
m2
kN
For these conditions, calculate:
(a) the load on the condenser.
(b) the steam economy
c) the overall heat transfer coefficient in each effect. Would there have been any advantages in using
backward feed in this case? Heat losses to the surroundings are negligible.
Concentration
Boiling point rise
Specific heat capacity
Heat of dilution, kJ/kg
wt %
deg K
kJ/kg K
10
1.6
3.85
6.1
3.72
2.3
30
15.0
3.64
9.3
50
41.6
3.22
2.2
20
Transcribed Image Text:A forward-feed double-effect evaporator, having 10 m2 of heating surface in each effect, is used to kg concentrate 1 of caustic soda solution from 10 per cent by mass to 30%. During a particular run, kN when the feed is at 373 kelvin (K), the pressures in the two calandrias are 375 and 180- respectively, m2 while the condenser operates at 30 m2 kN For these conditions, calculate: (a) the load on the condenser. (b) the steam economy c) the overall heat transfer coefficient in each effect. Would there have been any advantages in using backward feed in this case? Heat losses to the surroundings are negligible. Concentration Boiling point rise Specific heat capacity Heat of dilution, kJ/kg wt % deg K kJ/kg K 10 1.6 3.85 6.1 3.72 2.3 30 15.0 3.64 9.3 50 41.6 3.22 2.2 20
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