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Book - School of Science and Technology

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Types <strong>of</strong> refrigeration plant 541lithium bromide as the absorption medium. The equipment has no moving parts exceptpumps. Two-stage plant is also available, incorporating a second concentrator whichutilises heat recovery from the first stage <strong>of</strong> the cycle to provide improved efficiency. Thesource <strong>of</strong> energy being either steam, medium temperature hot water or gas, this type <strong>of</strong>plant is suited to installation where there is a heat source <strong>of</strong> a suitable grade available,such as with combined heat <strong>and</strong> power (CHP) systems. Such plant works under a highvacuum <strong>and</strong> is available in a range from 10 kW to over 5 MW cooling capacity. The heatto be removed by the condenser water with this system is about double that <strong>of</strong> a vapourcompression plant <strong>of</strong> equivalent capacity. For example, an absorption chiller <strong>of</strong> 350 kWcapacity will use a nominal steam quantity <strong>of</strong> 220 g/s, with heat rejection <strong>of</strong> some 900 kW.The equipment is usually very heavy <strong>and</strong> does need a level surface for installation.Steam-jet plantAn interesting type <strong>of</strong> refrigerator, using water as the medium, is that shown in Figure19.9. Its operation depends on the possibility <strong>of</strong> causing water to boil at low temperaturesunder high vacua. As noted previously, water at 7 C boils at an absolute pressure <strong>of</strong>1 kPa, i.e. about one-hundredth <strong>of</strong> atmospheric pressure. The absence <strong>of</strong> any specialrefrigerant is an advantage <strong>and</strong> an economy.The energy input with this equipment is much greater than with the positive compressiontypes owing to the inefficiency <strong>of</strong> jet compression <strong>and</strong> the requirement for condensingwater flow is about five times that <strong>of</strong> a vapour compression plant.A variation <strong>of</strong> the same system, but using a centrifugal compressor in place <strong>of</strong> thesteam-jet compressor, has also been developed <strong>and</strong> this avoids the above mentioneddisadvantage <strong>of</strong> high energy input. The great difficulty with both types is the maintenanceSecondaryejectorsVentSteamNozzlePrimary ejectorEvaporatorCondenserAftercooler4.5ºC 840PaMake up38º C 6.62kPaPumpPumpPumpChilledwaterCondensateto boilerCooling waterto towerFigure 19.9 Diagram <strong>of</strong> steam-jet system

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