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Fault Detection and Diagnostics for Rooftop Air Conditioners

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37<br />

L<br />

2 1<br />

P<br />

cond<br />

= Pdis<br />

− 0 ( fvdx+<br />

v −v<br />

= P<br />

D<br />

∫ 2 1)<br />

2<br />

0<br />

After the system stops, at least one of the condenser <strong>and</strong> evaporator coils will be<br />

filled with two-phase refrigerant <strong>and</strong> the refrigerant will not be subcooled anywhere. For<br />

a TXV system, since the TXV has the ability to shut off the refrigerant flow when the<br />

compressor stops, the refrigerant in both coils could remain in a two-phase condition. For<br />

a fixed-orifice system, after the system has been off <strong>for</strong> a long time in the daytime, the<br />

refrigerant in the condenser will normally be superheated. However, it takes some time<br />

<strong>for</strong> the high <strong>and</strong> low sides to reach a balance <strong>and</strong> <strong>for</strong> the refrigerant to become<br />

superheated. In addition, in the nighttime at many locations the outdoor temperature is<br />

normally lower than the indoor temperature, so the refrigerant in the condenser will be<br />

two-phase mixture when the system is off. Consequently, it is safe to assume that the<br />

refrigerant in the condenser would be saturated at some time when the system is off <strong>and</strong><br />

the following derivation holds.<br />

T = T ( P ) = T ( P )<br />

(1-13)<br />

cond, pred sat cond sat dis<br />

∆T = T − T = T − T ( P ) 0<br />

(1-14)<br />

cond, norm cond,<br />

meas cond,<br />

pred cond,<br />

meas sat dis<br />

=<br />

However, when there is non-condensable gas in the system <strong>and</strong> according to<br />

Dalton’s law,<br />

P<br />

ref , vapor<br />

= Pdis<br />

− Pncg<br />

= (1 − yncg<br />

) Pdis<br />

, yncg<br />

>> 0<br />

(1-15)<br />

dis<br />

y<br />

ncg<br />

=<br />

P<br />

P<br />

ncg<br />

dis<br />

=<br />

=<br />

( N<br />

1+<br />

( N<br />

1<br />

=<br />

χ<br />

1+<br />

r<br />

ref<br />

ncg<br />

N<br />

ncg<br />

ref , vapor<br />

ncg<br />

1<br />

N<br />

N<br />

ncg<br />

+ N<br />

N<br />

ref , vapor<br />

ref , total<br />

ref , total<br />

)<br />

)<br />

=<br />

( N<br />

ncg<br />

N<br />

( N<br />

ref , total<br />

ncg<br />

N<br />

) + ( N<br />

ref , total<br />

)<br />

ref , vapor<br />

N<br />

ref , total<br />

)<br />

where,<br />

P<br />

ref , vapor<br />

is the refrigerant partial pressure,<br />

ncg<br />

P is non-condensable gas partial<br />

pressure,<br />

y<br />

ncg<br />

is the mole fraction of non-condensable gas in the refrigerant vapor-gas<br />

37

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