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IEA Solar Heating and Cooling Programm - NachhaltigWirtschaften.at

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<strong>IEA</strong> SHC Task 38 <strong>Solar</strong> Air Conditioning <strong>and</strong> Refriger<strong>at</strong>ion Subtask C2-A, November 9, 2009<br />

Appendix<br />

Table 3. Constant parameters of the dynamic model.<br />

No. Constants Unit Value Description<br />

1 r<br />

( pc)<br />

kJkg -1 2450 Evapor<strong>at</strong>ion enthalpy of w<strong>at</strong>er<br />

2 l<br />

( pc)<br />

kJkg -1 272 Solution enthalpy of LiBr/w<strong>at</strong>er solution<br />

3 ( UA ) E,<br />

ext kWK -1 2.9 External he<strong>at</strong> transfer coefficient value of evapor<strong>at</strong>or<br />

4 ( UA ) C,<br />

ext kWK -1 5.2 External he<strong>at</strong> transfer coefficient value of condenser<br />

5 ( UA ) G,<br />

ext kWK -1 4.0 External he<strong>at</strong> transfer coefficient value of gener<strong>at</strong>or<br />

6 ( UA ) A,<br />

ext kWK -1 3.2 External he<strong>at</strong> transfer coefficient value of absorber<br />

7 ( UA ) E, int kWK -1 3.9 Internal he<strong>at</strong> transfer coefficient value of evapor<strong>at</strong>or<br />

8 ( UA ) C, int kWK -1 8.7 Internal he<strong>at</strong> transfer coefficient value of condenser<br />

9 ( UA ) G, int kWK -1 4.3 Internal he<strong>at</strong> transfer coefficient value of gener<strong>at</strong>or<br />

10 ( UA ) A, int kWK -1 3.2 Internal he<strong>at</strong> transfer coefficient value of absorber<br />

11 m &<br />

sol , w kgs -1 0.0559 Mass flow of weak solution<br />

12 m&<br />

hw kgs -1 0.3322 Mass flow of hot w<strong>at</strong>er<br />

13 m&<br />

cw kgs -1 0.7462 Mass flow of cooling w<strong>at</strong>er<br />

14 m&<br />

chw kgs -1 0.808 Mass flow of chilled w<strong>at</strong>er<br />

15 A t m² 4.9*10 -4 Cross area of solution tube<br />

16 h m 0.1 height between solution outlet <strong>at</strong> gener<strong>at</strong>or <strong>and</strong> inlet <strong>at</strong> absorber<br />

17 M<br />

st, sol,<br />

G,<br />

start kg 0.24 Initial condition of accumul<strong>at</strong>ed solution in gener<strong>at</strong>or sump<br />

18 M<br />

st, sol,<br />

A,<br />

start kg 0.19 Initial condition of accumul<strong>at</strong>ed solution in absorber sump<br />

19 ς - 2100 Resistance coefficient of solution he<strong>at</strong> exchanger <strong>and</strong> piping<br />

20 c 1 - 67, 2 time constant for solution flow from gener<strong>at</strong>or to absorber<br />

21 c 2 - 61, 1 time constant for solution flow from absorber to gener<strong>at</strong>or<br />

Mc p<br />

22 ( ) E ext<br />

Mc p<br />

23 ( ) C ext<br />

Mc p<br />

24 ( ) G ext<br />

Mc p<br />

25 ( ) A ext<br />

26 (<br />

p<br />

) E, int<br />

, kJK -1 6.8 Cumul<strong>at</strong>ed he<strong>at</strong> capacity of evapor<strong>at</strong>or, external<br />

, kJK -1 6.4 Cumul<strong>at</strong>ed he<strong>at</strong> capacity of condenser, external<br />

, kJK -1 9.0 Cumul<strong>at</strong>ed he<strong>at</strong> capacity of gener<strong>at</strong>or, external<br />

, kJK -1 9.0 Cumul<strong>at</strong>ed he<strong>at</strong> capacity of absorber, external<br />

Mc kJK -1 38.4 Cumul<strong>at</strong>ed he<strong>at</strong> capacity of evapor<strong>at</strong>or, internal<br />

Mc kJK -1 38.2 Cumul<strong>at</strong>ed he<strong>at</strong> capacity of condenser , internal<br />

27 (<br />

p<br />

) C, int<br />

page 92

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