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Book - School of Science and Technology

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Air systems ± characteristics 165FallRelay pointSee fig 8.20 alsoRelay pointFigure 6.19 Steam main relay pointsCurrent practiceFacilities for the removal <strong>of</strong> condensate so that the steam supply remains dry are amongthe more important features <strong>and</strong> supply pipework must be provided with relay points, asin Figure 6.19, to assist in this respect (see Figure 8.20 also, p. 222). Otherwise, pipeworkfollows a two-pipe pattern very much as might be anticipated, incorporating specialisedequipment as described in Chapter 8.Condensate will, in most normal circumstances, be collected <strong>and</strong> returned to a tank orhot well near to the boiler. Where distance or site levels make direct return impossible,intermediate collection <strong>and</strong> pumping units may be required. At the hot well, to make upfor any losses which may have occurred, a treated water supply will be provided <strong>and</strong> thismay alternatively be directly `on line' or via an intermediate store. The optimum size <strong>of</strong> ahot well will depend upon a number <strong>of</strong> factors such as the order <strong>of</strong> fluctuation in thesteam dem<strong>and</strong>, the corresponding ± but not necessarily equivalent ± rate <strong>of</strong> condensatereturn <strong>and</strong> the operational routine <strong>of</strong> the water treatment plant. It is good practice,nevertheless, to provide a minimum size related to the evaporation capacity <strong>of</strong> the boilerplant over 2 hours.The temperature <strong>of</strong> the returned condensate is likely to be not much below 100 C butthe hot well should nevertheless be provided with a steam coil to maintain that level. Toavoid cavitation at the suction connections <strong>of</strong> the pumping equipment provided to returncondensate to the boilers, the hot well should be elevated where this is practicable, toabout 5 m above that level. Where packaged boilers are used, each is likely to be provided,at works, with a small cylindrical `condense receiver' in association with the prewired feedpump <strong>and</strong> associated controls. The size <strong>of</strong> such receivers is usually quite inadequate toprovide the necessary storage capacity but their volume may be deducted from thecapacity <strong>of</strong> the hot well as proposed above.Air systems ± characteristicsPassing reference was made in Chapter 4 to the use <strong>of</strong> hot air as a heat transfer mediumwithin floor ducts but such an application is a rarity <strong>and</strong> no purpose would be achieved bypursuing it further here. Table 6.9 lists the principal characteristics <strong>of</strong> dry air in contextwith its use for space heating <strong>and</strong> it is <strong>of</strong> interest to compare these with the equivalentvalues for hot water as listed in Table 6.1. The specific heat capacity <strong>of</strong> water, in terms <strong>of</strong>mass, is four times that <strong>of</strong> air at the same temperature <strong>and</strong> in terms <strong>of</strong> volume thedifference is immensely greater.Ventilation systems are dealt with later (Chapter 13) <strong>and</strong> it is necessary to draw a quiteclear distinction between the function which they fulfil <strong>and</strong> that <strong>of</strong> the so-called plenumsystem, using air as a heating medium, which falls under this present heading. The essence<strong>of</strong> the difference lies in the fact that an inlet ventilation system, properly designed, will dono more than introduce a supply <strong>of</strong> air into the space served at a temperature which is

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