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Fault Detection and Diagnostics for Rooftop Air Conditioners

Fault Detection and Diagnostics for Rooftop Air Conditioners

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solution procedure involves the non-linear solution of three residual equations in the cycle.<br />

The effect of all five of the operating faults which are being studied can be simulated with<br />

ACMODEL.<br />

Except <strong>for</strong> Rossi <strong>and</strong> Braun, the problem of developing a physical model <strong>for</strong> a rooftop air<br />

conditioning unit <strong>for</strong> FDD purposes has not been specifically addressed in the literature.<br />

Stylianou <strong>and</strong> Nikanpour (1996) considered two different models <strong>for</strong> a reciprocating chiller<br />

to use with a model-based FDD technique. For the problem of fault detection, a gray-box<br />

model was used. This model, developed from first principles <strong>and</strong> first introduced by<br />

Gordon <strong>and</strong> Ng (1994), correlated the equipment COP with the condenser <strong>and</strong> evaporator<br />

inlet water temperatures. This per<strong>for</strong>mance index is used to decide when the impact of a<br />

fault is significant enough to warrant repair. The other model is a black-box model which<br />

will be discussed in the next section.<br />

2.2 Black-box modeling<br />

Since black-box models are easy to develop, accurately fit training data, <strong>and</strong> are<br />

computationally simple, they are popular <strong>for</strong> engineering use. Several kinds of black-box<br />

modeling approaches will be discussed here.<br />

2.2.1 Polynomials<br />

Linear regression polynomials are the easiest <strong>and</strong> most frequently used black-box<br />

models. Grimmelius et al. (1995) used steady-state linear models with three input<br />

variables to predict a number of output states of a vapor compression chiller. The<br />

predicted variables included the temperatures <strong>and</strong> pressures at the inlet <strong>and</strong> outlet of<br />

each component in the refrigeration cycle, suction superheat, liquid subcooling, oil<br />

pressure, temperature, <strong>and</strong> level, the pressure ratio across the compressor, temperature<br />

changes of the water across the evaporator <strong>and</strong> condenser, filter pressure drop, <strong>and</strong><br />

compressor power. The three input variables were the chiller water inlet temperature,<br />

the cooling water temperature into the condenser, <strong>and</strong> the number of compressor<br />

cylinders in operation. The model <strong>for</strong>m which was used is<br />

y = β + β T + β T + β Z + β Z + β Z + β log( T )<br />

i o, i 1, i chwi 2, i cwi 3, i 1 4, i 2 5, i 3 6,<br />

i chwi<br />

−1<br />

+ β ( T ) + β log( T ) + β ( T )<br />

−1<br />

7, i chwi 8, i cwi 9,<br />

i cwi<br />

8

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