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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 />

T C,<br />

i − T C,<br />

i−1<br />

( r + c ⋅ ( T G,<br />

i − T C,<br />

i<br />

) + ( M ⋅ c ) ⋅<br />

= ( UA) ⋅ ( T T )<br />

& (29)<br />

∆t<br />

m<br />

v, G,<br />

i<br />

⋅<br />

( pc)<br />

p,<br />

v<br />

p C,int<br />

C,int<br />

C,<br />

i<br />

−<br />

C,<br />

i<br />

m&<br />

v,<br />

A,<br />

i<br />

⋅<br />

( r + l − c ⋅ ( T G,<br />

i − T E,<br />

i ) + c ⋅ ( T G,<br />

i − T A,<br />

i<br />

)<br />

( pc)<br />

T A,<br />

i − T A,<br />

i−1<br />

( M ⋅ c ) ⋅<br />

= ( UA) ⋅ ( T − T )<br />

p A,int<br />

( pc)<br />

∆t<br />

p,<br />

v<br />

A,int<br />

p,<br />

w<br />

A,<br />

i<br />

A,<br />

i<br />

+ Q&<br />

SHX , i<br />

+<br />

(30)<br />

Equ<strong>at</strong>ions (27) <strong>and</strong> (28) describe the internal he<strong>at</strong> transfer in evapor<strong>at</strong>or <strong>and</strong> gener<strong>at</strong>or,<br />

respectively. There, the he<strong>at</strong> which is given off by the he<strong>at</strong> exchanger (right-h<strong>and</strong> side) partly<br />

he<strong>at</strong>s up the internal parts of the vessel (second term on left-h<strong>and</strong> side) <strong>and</strong> partly is used for<br />

the he<strong>at</strong>ing of solution <strong>and</strong> refrigerant (first term on left-h<strong>and</strong> side). In analogy, equ<strong>at</strong>ions (29)<br />

<strong>and</strong> (30) describe condenser <strong>and</strong> absorber, respectively. There, the he<strong>at</strong> which is given off<br />

by the solution <strong>and</strong> refrigerant (first term on left-h<strong>and</strong> side) is used partly to he<strong>at</strong> the internal<br />

parts of the he<strong>at</strong> exchanger (second term on left-h<strong>and</strong> side) <strong>and</strong> partly to he<strong>at</strong> the cooling<br />

w<strong>at</strong>er (right-h<strong>and</strong> side).<br />

The equ<strong>at</strong>ion system is being solved in MATLAB using a Newton-Raphson procedure with<br />

finite-difference Jacobian approxim<strong>at</strong>ion [6].<br />

Experimental Verific<strong>at</strong>ion<br />

The agreement between simul<strong>at</strong>ed <strong>and</strong> experimental d<strong>at</strong>a has been tested using an<br />

experimentally measured hot w<strong>at</strong>er input step from 75 to 85 °C. The results of the simul<strong>at</strong>ion<br />

using these input d<strong>at</strong>a are shown in Figure 5. The hot w<strong>at</strong>er inlet <strong>and</strong> outlet temper<strong>at</strong>ures in<br />

Figure 5 are taken from experimental measurements of the Phoenix absorption chiller. They<br />

show the transient behaviour of the chiller for a 10K step in hot w<strong>at</strong>er inlet temper<strong>at</strong>ure.<br />

<strong>Cooling</strong> <strong>and</strong> chilled w<strong>at</strong>er inlet temper<strong>at</strong>ures as well as all external mass flow r<strong>at</strong>es were kept<br />

constant during the step. It can be seen th<strong>at</strong> it takes approx. 600s or 10 minutes to achieve a<br />

new steady-st<strong>at</strong>e in hot w<strong>at</strong>er inlet temper<strong>at</strong>ure after the step. This is shorter than the 15<br />

minutes it takes for all parameters to achieve steady-st<strong>at</strong>e again. The simul<strong>at</strong>ion was<br />

performed using the measured d<strong>at</strong>a as inputs in the model <strong>and</strong> comparing simul<strong>at</strong>ed <strong>and</strong><br />

measured hot w<strong>at</strong>er outlet temper<strong>at</strong>ures.<br />

page 73

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