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integration of solid oxide fuel cells and ... - Ea Energianalyse

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3. COMPONENT DESCRIPTION<br />

undergoes a phase transition which by far gives a higher heat capacity<br />

flow.<br />

ɛ = T chill,i − T chill,o<br />

T chill,i − T r,i<br />

(3.38)<br />

The chilling power <strong>of</strong> the evaporator is calculated by the enthalpy<br />

change <strong>of</strong> the chilling water. This change is determined by the energy<br />

balance. The heat ingress from the surroundings defined by the<br />

parameter ˙Q loss , should be either zero or a negative number.<br />

˙Q = Ḣ chill,i − Ḣ chill,o (3.39)<br />

Ḣ r,i + Ḣ chill,i = Ḣ r,o + Ḣ chill,o + ˙Q loss (3.40)<br />

The mass balance is specified for the refrigerant as well as the chilling<br />

water cycle.<br />

ṁ r,o = ṁ r,i (3.41)<br />

ṁ chill,o = ṁ chill,i (3.42)<br />

The pressure losses (given as a negative pressure increases) are defined<br />

as two different ∆P parameters:<br />

p r,o = p r,i + ∆p r (3.43)<br />

p c,o = p c,i + ∆p chill (3.44)<br />

56

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