IEA Solar Heating and Cooling Programm - NachhaltigWirtschaften.at
IEA Solar Heating and Cooling Programm - NachhaltigWirtschaften.at IEA Solar Heating and Cooling Programm - NachhaltigWirtschaften.at
IEA SHC Task 38 Solar Air Conditioning and Refrigeration Subtask A Report, Date:… 80 variable speed control on water spray mode off 70 60 50 ] 40 [°C s re 30 tu ra e p20 m e T 10 solar supply loop solar return loop heat rejection supply loop heat rejection return loop cold water supply loop cold water return loop ambient temperature 0 6 :5 1 6 :1 2 1 6 :3 2 1 6 :5 2 1 6 :1 3 1 6 :3 3 1 6 :5 3 1 6 :1 4 1 6 :3 4 1 6 :5 4 1 6 6 6 :1 :3 :5 5 5 5 1 1 1 Time 6 :1 6 1 6 :3 6 1 6 :5 6 1 6 :1 7 1 6 :3 7 1 6 :5 7 1 6 :1 8 1 6 :3 8 1 6 :5 8 1 6 :1 9 1 6 :3 9 1 In Figure 14, the temperatures around the adsorption chiller on the 25 th of August 2010 are shown. It is clearly identifiable, that while the heat rejection temperatures are rising, nearly any temperature difference between supply and return cold water side happens during the variable speed control mode of the heat rejection fans. Therefore, there wasn´t nearly any cooling demand in the offices and the adsorption chiller shouldn´t have been working at all. The control of the absorption chiller is only taking a certain cooling set point temperature on the cold supply water side into account (here 12 °C ). It is therefore the duty of the system controller to turn off the adsorption chiller, when an unreasonable operation like this happens, but that was not adapted by installing the variable speed control mode of the heat rejection fans in July 2010. To avoid the operation, as it happened on the 25 th of August 2010, the cooling set point temperature was changed to 6 °C until the adaptatio n of the system controller happens (see Figure 15).
IEA SHC Task 38 Solar Air Conditioning and Refrigeration Subtask A Report, Date:… 80 70 60 ] [°C s re tu ra e p m e T 50 40 30 20 10 solar supply loop solar return loop heat rejection supply loop heat rejection return loop cold water supply loop cold water return loop ambient temperature 0 4 :0 5 1 6 :1 5 1 8 :2 5 1 0 :4 5 1 2 :5 5 1 4 :0 6 1 6 8 :1 :2 6 6 1 1 Time 0 :4 6 1 2 :5 6 1 4 :0 7 1 6 :1 7 1 8 :2 7 1 5 Summary and Conclusions Within the IEA SHC task 38 for the solar adsorption cooling plant of the Viennese Municipality Department 34 (MA34) following investigations were accomplished: • COP el and COP th of the solar adsorption cooling plant • Operation of hybrid heat rejection in dry or wet cooling mode • Effects of variable speed control of the heat rejection fans on the energy performance Summary of the substantial realizations: • The heat rejection in this plant causes three quarters of the electricity demand, therefore the selection of a heat rejection device with a high efficiency class (preferably wet cooling tower or at least hybrid heat rejection) is essential to achieve a high COP el . • Selection of variable speed, energy-efficient pumps are also important to achieve high COP el . • The monitoring results of the 25 th of August 2010 showed that a COP el of 4,55 is already possible with this plant. Therefore, high desorption temperatures are
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<strong>IEA</strong> SHC Task 38 <strong>Solar</strong> Air Conditioning <strong>and</strong> Refriger<strong>at</strong>ion<br />
Subtask A Report, D<strong>at</strong>e:…<br />
80<br />
70<br />
60<br />
]<br />
[°C<br />
s<br />
re<br />
tu<br />
ra<br />
e<br />
p<br />
m<br />
e<br />
T<br />
50<br />
40<br />
30<br />
20<br />
10<br />
solar supply loop<br />
solar return loop<br />
he<strong>at</strong> rejection supply loop<br />
he<strong>at</strong> rejection return loop<br />
cold w<strong>at</strong>er supply loop<br />
cold w<strong>at</strong>er return loop<br />
ambient temper<strong>at</strong>ure<br />
0<br />
4<br />
:0<br />
5<br />
1<br />
6<br />
:1<br />
5<br />
1<br />
8<br />
:2<br />
5<br />
1<br />
0<br />
:4<br />
5<br />
1<br />
2<br />
:5<br />
5<br />
1<br />
4<br />
:0<br />
6<br />
1<br />
6 8<br />
:1 :2<br />
6 6<br />
1 1<br />
Time<br />
0<br />
:4<br />
6<br />
1<br />
2<br />
:5<br />
6<br />
1<br />
4<br />
:0<br />
7<br />
1<br />
6<br />
:1<br />
7<br />
1<br />
8<br />
:2<br />
7<br />
1<br />
<br />
5 Summary <strong>and</strong> Conclusions<br />
Within the <strong>IEA</strong> SHC task 38 for the solar adsorption cooling plant of the Viennese<br />
Municipality Department 34 (MA34) following investig<strong>at</strong>ions were accomplished:<br />
• COP el <strong>and</strong> COP th of the solar adsorption cooling plant<br />
• Oper<strong>at</strong>ion of hybrid he<strong>at</strong> rejection in dry or wet cooling mode<br />
• Effects of variable speed control of the he<strong>at</strong> rejection fans on the energy performance<br />
Summary of the substantial realiz<strong>at</strong>ions:<br />
• The he<strong>at</strong> rejection in this plant causes three quarters of the electricity dem<strong>and</strong>,<br />
therefore the selection of a he<strong>at</strong> rejection device with a high efficiency class<br />
(preferably wet cooling tower or <strong>at</strong> least hybrid he<strong>at</strong> rejection) is essential to achieve<br />
a high COP el .<br />
• Selection of variable speed, energy-efficient pumps are also important to achieve high<br />
COP el .<br />
• The monitoring results of the 25 th of August 2010 showed th<strong>at</strong> a COP el of 4,55 is<br />
already possible with this plant. Therefore, high desorption temper<strong>at</strong>ures are