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HVAC SYSTEMS - HFT Stuttgart

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Page - 25 -<br />

CHAPTER 02<br />

to ensure as low collector supply temperatures as possible. For an ideal heat<br />

exchanger the temperature of the cold fluid could be heated up to the inlet<br />

temperature of the cold fluid. The heat exchanger efficiency describes how<br />

close a heat exchanger comes to the ideal case and is therefore defined as the<br />

ratio between the maximum possible heat transfer and the actual heat transfer<br />

as shown in Equation 2.2.1-24.<br />

m&<br />

1c<br />

1<br />

=<br />

m&<br />

c<br />

1<br />

( T1,<br />

in −T1,<br />

aus )<br />

( T −T<br />

)<br />

1<br />

1,<br />

in<br />

2,<br />

in<br />

m&<br />

2c<br />

2<br />

=<br />

m&<br />

c<br />

1<br />

( T 2,<br />

aus −T<br />

2,<br />

in )<br />

( T −T<br />

)<br />

φ (2.2.1-24)<br />

1<br />

1,<br />

in<br />

The heat exchanger effectiveness of the most common heat exchangers<br />

(counter flow, concurrent flow, cross flow) are functionally dependent on the<br />

ratio between the heat transfer power UA and the capacity flow C& = m&<br />

⋅ c . This<br />

ratio is called as number of transfer units NTU.<br />

UA<br />

NTU =<br />

C&<br />

(2.2.1-25)<br />

The heat exchanger efficiency for counter flow heat exchangers is according to<br />

(Bosnjakovic, 1951) for heat capacity flows C&<br />

1 < C&<br />

2 as follows:<br />

φ =<br />

1 − e<br />

C 1 1 − e<br />

C&<br />

⎛ C ⎞ 1 & −⎜1<br />

⎟<br />

⎜<br />

− ⋅<br />

C&<br />

⎟<br />

2<br />

2<br />

⎛ C&<br />

⎞ 1 UA<br />

−⎜1<br />

⎟<br />

⎜<br />

− ⋅<br />

C&<br />

⎟<br />

2 C&<br />

⎝ ⎠ 1<br />

⎝<br />

& UA<br />

C&<br />

⎠ 1<br />

2,<br />

in<br />

(2.2.1-26)<br />

In INSEL a block called ‘HXS’ is already available based on the equations<br />

shown above. This block is used for the simulation of the counter flow heat<br />

exchangers of the solar systems analysed in Caper 3, 4 and 5.

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