Page 182 - Low Temperature Energy Systems with Applications of Renewable Energy

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B 35 62
Case 0.123 416 a) b) 352 3030 1160 20 111 389 1185 2160 2550

A 35 100
Case 0.081 605.3 a) b) 102 2856 1200 20 50 100 1150 1960 2646

þ Dt 14 10

x 8 ) h 8 ) h 13 )
t 14 Dt 3 7 h 15 )
x 1 )/(x 1 4(h 1 ¼ h 10 Þ h 10 ) t c (h 10 (h 9

þ h 2 ) þ Dt h:ex: þ f 1 ðh 9 f (h 9 ¼ f þ f þ h 8 )
G 8 /G 2 ¼(x 2 (h 1 t 14 ¼ h 14 1) (f h 3 Dt cooler h 6 q c h 4 h 10 ) h 9 ) 4(h 1

Formula ¼ 4 ¼ q r.c. t 10 a) h 10 b) ¼ h 15 ¼ q h.ex h 2 ¼ q c t 3 ¼ t 7 h 7 ¼ q c h 3 ¼ h 4 h 6 ¼ q 0 (h 7 ¼ q a (h 1 ¼ q g þ

(reflux kJ/kg

condenser C; kJ/kg C

reflux kJ/kg exchanger, inlet, kJ/kg cooler, after kJ/kg

from condenser, heat after generator exchanger, kJ/kg condenser, temperature kJ/kg plant, of kJ/kg kJ/kg
Solution.dcont’d reflux of reflux of load parameters at enthalpy heat of load of load vapor cooler, of load enthalpy capacity absorption, on of, load

4.E2 Parameters withdrawal ratio) heat solution solution heat heat agent heat inlet cooling released heat Generator
Table Specific Specific Weak Strong Specific Specific Cooling Specific Throttle Specific Heat