Q1. A forward-feed double-effect evaporator, having 10 m2 of heating surface in each effect, is used to concentrate 1 kg/s of caustic soda solution from 10 per cent by mass to 30%. During a particular run, when the feed is at 373 K the pressures in the t wo calandrias are 375

Elements Of Electromagnetics
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Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
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Q1. A forward-feed double-effect evaporator,
having 10 m2 of heating surface in each effect, is
used to concentrate 1 kg/s of caustic soda
solution from 10 per cent by mass to 30%.
During a particular run, when the feed is at 373
K, the pressures in the two calandrias are 375
and 180 kN/m2 respectively, while the
condenser operates at 30 kN/m². For these
:conditions, calculate
.the load on the condenser (a)
the steam economy (b)
the overall heat transfer coefficient in each (c)
.effect
Would there have been any advantages in using
backward feed in this case? Heat losses to the
.surroundings are negligible
Transcribed Image Text:Q1. A forward-feed double-effect evaporator, having 10 m2 of heating surface in each effect, is used to concentrate 1 kg/s of caustic soda solution from 10 per cent by mass to 30%. During a particular run, when the feed is at 373 K, the pressures in the two calandrias are 375 and 180 kN/m2 respectively, while the condenser operates at 30 kN/m². For these :conditions, calculate .the load on the condenser (a) the steam economy (b) the overall heat transfer coefficient in each (c) .effect Would there have been any advantages in using backward feed in this case? Heat losses to the .surroundings are negligible
:Physical properties of caustic soda solutions
Specific Boiling
Heat of
heat
point Concentration
dilution,
сарacity
rise
% wt
kJ/kg
kJ/kg K
deg K
3.85
1.6
10
2.3
3.72
6.1
20
9.3
3.64
15.0
30
2.2
3.22
41.6
50
Transcribed Image Text::Physical properties of caustic soda solutions Specific Boiling Heat of heat point Concentration dilution, сарacity rise % wt kJ/kg kJ/kg K deg K 3.85 1.6 10 2.3 3.72 6.1 20 9.3 3.64 15.0 30 2.2 3.22 41.6 50
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