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Book - School of Science and Technology

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Choice <strong>of</strong> refrigeration plant 543<strong>of</strong> the order <strong>of</strong> an additional 20% power absorbed by the compressor motor. Since acooling tower may be located at a considerable distance from the refrigeration plant,horizontally or vertically, such a combination has obvious attractions as far as flexibilityis concerned <strong>and</strong> it is common practice for the machinery to be sited in abasement <strong>and</strong> the cooling tower at ro<strong>of</strong> level. It is <strong>of</strong> course necessary that an opencircuit cooling tower should be positioned sufficiently above the refrigeration plant toprevent any drainage or priming problems. Where this cannot be achieved, an intermediateheat exchanger may be installed.Storage systemsAn annual cooling load pr<strong>of</strong>ile, plotted for almost any air-conditioned building, wouldshow that the maximum load only occurs on a few occasions. This is due to the fact thatmany <strong>of</strong> the components <strong>of</strong> the total are not only seasonal but transitory hour-by-hour.Thus, where the central plant is sized to match the peakload, it will operate at considerablyless than its full capacity for the majority <strong>of</strong> the time. An alternative to sizing arefrigeration plant to meet the peakcooling load would, therefore, be to provide somemeans to store a cooled medium (water, ethylene glycol solution, ice, etc.) <strong>and</strong> thus allowa somewhat smaller plant to run for longer periods at full output. The stored energywould then be available, as required, to make up the deficit between the plant capacity<strong>and</strong> the peakrequirement. The advantages <strong>of</strong> such an arrangement are:. reduced size <strong>of</strong> refrigeration plant. reduced maximum dem<strong>and</strong> on power supply. reduced unit energy charge, if run <strong>of</strong>f-peak. inherent st<strong>and</strong>by capacity in the energy store. stability available for control.The parallel disadvantages are:. higher capital cost. increased space requirement. possibility <strong>of</strong> lower coefficient <strong>of</strong> performance with low temperature or ice storagesystems.The storage system concept may be applied in varying degrees. It is not uncommon inthe British Isles for a limited quantity <strong>of</strong> chilled water to be provided for peak lopping <strong>and</strong>,in this case, capacity would be provided to supplement a water chilling plant for one ortwo hours in the day, at the time <strong>of</strong> maximum load. At the other extreme, it would not beimpossible to provide sufficient storage to meet a total peak-day cooling load, the plantrunning during night hours only during the period when an <strong>of</strong>f-peaktariff applies. Afurther option would be to run the plant continuously over 24 hours <strong>and</strong> to provide alimited level <strong>of</strong> storage such that during the whole period <strong>of</strong> dem<strong>and</strong> for cooling, both theplant output <strong>and</strong> the stored energy would be used in parallel. Figure 19.11 illustrates thesethree basic operating modes <strong>and</strong> indicates the relationship between plant size <strong>and</strong> storedwater quantity.Whereas the design <strong>of</strong> a hot water storage system (Chapter 5, p. 138) is able to limit therequired volume <strong>of</strong> the vessels by applying pressure <strong>and</strong> storing water at an elevatedtemperature, parallel action (i.e. storage at a temperature much lower than that <strong>of</strong> usage)is not really practical in the case <strong>of</strong> chilled water. A temperature <strong>of</strong> about 4 C is thatmost usually chosen as the practical minimum but, even at this level, design problems

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