Question

Solve I, II and III please. I not in hurry, Solve if you are sure.

Aeuyesent Superheated water vapor 0.406 g/s 2603 k14 Generator 74C 47.54 mbar Solution 9.35 gis 60% LiBr 32C 47 54 mbar Pump Liquid water 0406 g/s 134.08 k)/kg Solution 575% LiBr -165 kl/kg valve 32"C 6.57 mbar Absorber TC 657 mbar Evaporaton Saturated water vapor 2464.89 kl/kg 0406 is

Answer 1

Solution' Blodt diagram of absos ptian deiqeaion cycle CondenSor 3 absor bel Enthalphy values tDfeent points I34- 08 kJik CJ Heat emoved Po Absosbe The Solution floo Rata q구691S Ligi present 57. S7.

Aoua, Calculate the energ balance at absosbes is aths h3 Heat Removed om -he Condense e4o(603 0-1308) ks Heat Added-to-the evaporator ΟΎ06 &. 33081

Cop op the cycle T evapora C-TE Torn 34730s 31 344 698 Calculofion sdo en@fay i 3 ton (given)

XA aling Arbient temperatwe on38 -8-SOS A-o186 A Since uker e Au is the useR eneray taken bu Ai is he total sadiated eneg indent at plate GR is the eneray convected and Radiated bact o the suxtound ina Here, we aie taking the temperatue of Flat plate Some os Generator emperathre and Temperatue sunteunding and some as Condenser Temperature Then thalph of-the uid water

5 The Required enern is Then, he en bolance is .39A 99o42 99. 0442 8-379