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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 C1 Report, 31 October 2010<br />

KONDENSATOR<br />

CONDENSER<br />

Kühlwasser<br />

cooling w<strong>at</strong>er<br />

ADSORBER<br />

cooling Kühlwasser w<strong>at</strong>er<br />

Wärmeübertrager he<strong>at</strong> exchanger with mit silica Silicagel<br />

DESORBER<br />

Antriebswärme<br />

driving he<strong>at</strong><br />

Wärmeübertrager he<strong>at</strong> exchanger with mit silica Silicagel<br />

autom<strong>at</strong>ische, autom<strong>at</strong>ic internal innere valves Ventile<br />

condens<strong>at</strong>e Kältemittelrücklauf return<br />

Kaltwasser<br />

chilled w<strong>at</strong>er<br />

EVAPORATOR<br />

VERDAMPFER<br />

Figure 11: Scheme of a typical adsorption chiller with two adsorption chambers, one<br />

evapor<strong>at</strong>or <strong>and</strong> one condenser.<br />

The two adsorber adsorption chiller is oper<strong>at</strong>ed in four phases:<br />

1. Phase 1: the left reactor is regener<strong>at</strong>ed, the right reactor is in the adsorption phase.<br />

2. Phase 2: he<strong>at</strong> from the left, hot adsorber is used to pre-he<strong>at</strong> the cold adsorber on the<br />

right h<strong>and</strong> side<br />

3. Phase 3: is similar to phase 1 with exchanged adsorbers<br />

4. Phase 4: similar to phase 2 with exchanged adsorbers.<br />

Kondens<strong>at</strong>or<br />

condenser<br />

Phase 1<br />

desorption Desorption<br />

Adsorption adsorption<br />

Phase 4<br />

Phase 2<br />

Kondens<strong>at</strong>or condenser<br />

Verdampfer evapor<strong>at</strong>or<br />

Kondens<strong>at</strong>or<br />

condenser<br />

Verdampfer evapor<strong>at</strong>or<br />

Wärmerückgewinnung<br />

he<strong>at</strong> recovery<br />

Kondens<strong>at</strong>or<br />

condenser<br />

Phase 3<br />

Verdampfer evapor<strong>at</strong>or<br />

Wärmerückgewinnung<br />

he<strong>at</strong> recovery<br />

adsorption Adsorption<br />

Desorption desorption<br />

Verdampfer evapor<strong>at</strong>or<br />

Figure 12: The four phases of an adsorption chiller with two reactors.<br />

3.2 Main characteristics<br />

The time for the he<strong>at</strong> recovery is critical: on the one h<strong>and</strong> a very good he<strong>at</strong> recovery is<br />

necessary to achieve reasonable COPs, on the other h<strong>and</strong> during the he<strong>at</strong> recovery process<br />

normally no cold is produced, thus reducing the cooling power.<br />

page 29

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