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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 C Report, D<strong>at</strong>e: 13.01.2009<br />

In conclusion it can be seen from Figure 1-4, th<strong>at</strong> the temper<strong>at</strong>ure level of the driving he<strong>at</strong><br />

has to be increased with increasing he<strong>at</strong> rejection temper<strong>at</strong>ure level significantly. For a low<br />

temper<strong>at</strong>ure he<strong>at</strong> source of 5°C <strong>and</strong> a he<strong>at</strong> rejection temper<strong>at</strong>ure of 30°C the minimum<br />

temper<strong>at</strong>ure level of the driving he<strong>at</strong> is <strong>at</strong> approx. 60°C. If the he<strong>at</strong> rejection temper<strong>at</strong>ure<br />

increases to 50°C the minimum driving temper<strong>at</strong>ure l evel has to be increased to approx.<br />

105°C as well.<br />

In Figure 1-5 the efficiency of different solar collectors <strong>at</strong> varying working temper<strong>at</strong>ure levels<br />

are shown (Heß, 2007). The efficiency of st<strong>and</strong>ard collectors decreases dram<strong>at</strong>ically with<br />

increasing working temper<strong>at</strong>ure. This effect underlines the need of low he<strong>at</strong> rejection<br />

temper<strong>at</strong>ure levels to enable as low driving temper<strong>at</strong>ure levels as possible, st<strong>and</strong>ard fl<strong>at</strong>pl<strong>at</strong>e<br />

collectors <strong>and</strong> increase system efficiency.<br />

Figure 1-5: Comparison of the efficiency of different solar collectors designs <strong>at</strong> varying<br />

working temper<strong>at</strong>ure levels. (Heß, 2007)<br />

Note: Dealing with solar cooling applic<strong>at</strong>ions one important factor is the part load oper<strong>at</strong>ion.<br />

In other words: wh<strong>at</strong> cooling capacity can be achieved <strong>at</strong> certain temper<strong>at</strong>ure levels of the<br />

he<strong>at</strong> sink <strong>and</strong> the he<strong>at</strong> sources. By the use of different assumptions (e.g. th<strong>at</strong> the mass flow<br />

through the solutions pump is constant) a “characteristic equ<strong>at</strong>ion” can be derived. This<br />

equ<strong>at</strong>ion brings together in a linear correl<strong>at</strong>ion the cooling load (Q COL ) <strong>and</strong> a function of the<br />

temper<strong>at</strong>ure levels (∆∆t) in the four main components (Genar<strong>at</strong>or, Absorber, Condenser <strong>and</strong><br />

Evapor<strong>at</strong>or) of an AHP. A detailed description of this correl<strong>at</strong>ion can be found in Ziegler<br />

(1997). Evalu<strong>at</strong>ing the temper<strong>at</strong>ure level of the he<strong>at</strong> rejection system it can be concluded,<br />

th<strong>at</strong> if the he<strong>at</strong> rejection temper<strong>at</strong>ure increases the cooling capacity of an AHP will decrease<br />

significantly.<br />

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