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Book - School of Science and Technology

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594 Hot water supply systemsA complete discussion <strong>of</strong> this subject would be beyond the scope <strong>of</strong> this book <strong>and</strong> thebrief notes which follow are intended only as an introduction to the methods commonlyused to treat cold water supplies to hot water systems. Further information may be foundin the CIBSE Guide G6 but specialist advice should be sought where particular problemsare known to exist.Hardness <strong>of</strong> waterThe calcium <strong>and</strong> magnesium salts present in raw water exist in two forms, as bicarbonateswhich form what is known as temporary hardness <strong>and</strong> as sulphates, chlorides <strong>and</strong> nitrateswhich form what is known as permanent hardness. The salts within the temporarycategory fall out <strong>of</strong> solution when the water temperature is raised to about 70 C whichsituation occurs adjacent to heat exchange surfaces even when the storage temperature isbelow that level. The salts <strong>of</strong> permanent hardness remain in solution at the temperaturesgenerally encountered in indirect systems but calcium sulphate may cause problems indirect systems at boiler surfaces or where the primary medium <strong>of</strong> an indirect system is athigh temperature.Commercial installationsHere, dependent upon circumstances, it is probable that a full scale water treatment plantwill be installed. This is most likely to be a base- or ion-exchange process which makes use<strong>of</strong> beds <strong>of</strong> either natural or synthetic zeolites (sodium aluminium silicates). These mineralscontain sodium in combination <strong>and</strong> have the property <strong>of</strong> exchanging this with the calcium<strong>and</strong> magnesium salts in a raw water to form sodium bicarbonate which is not hard-scaleforming. Natural zeolites (greens<strong>and</strong>s) are impermeable <strong>and</strong> have a lower capacity forexchange, per unit volume, than the synthetic type. The latter, as a result <strong>of</strong> their porousstructure, must not be used with an unfiltered raw water supply <strong>and</strong> have a shorter lifethan the natural material.The exchange process does not continue indefinitely since the capacity <strong>of</strong> the zeolite issaid to be exhausted when all the sodium content has been exchanged: it is then necessaryto regenerate the mineral by slow flushing with a strong solution <strong>of</strong> common salt (sodiumchloride) followed by brisk backwash to remove the brine residual <strong>and</strong> dispose <strong>of</strong> thecalcium <strong>and</strong> magnesium. It must be emphasised that the process <strong>of</strong> base exchange, whilstreducingscale deposition, does not reduce the total content <strong>of</strong> dissolved solids in the water.DosingInternal water treatment by dosingboiler make-up water has been a familiar process inthe case <strong>of</strong> industrial plant where the facilities exist to allow the effect to be monitored <strong>and</strong>the quantities <strong>of</strong> additive adjusted accordingly. For use at domestic level, it has beennecessary to develop simple methods for automatic metering<strong>of</strong> dosage which require noskill to operate <strong>and</strong> will not permit overfeed. A number <strong>of</strong> devices which allow suitablequantities <strong>of</strong> phosphates <strong>and</strong> polyphosphates to be injected into an incomingmains watersupply is now available for use at domestic level. This injection modifies the hardness saltssuch that, followingtreatment, they remain suspended in the water, instead <strong>of</strong> bondingone to another <strong>and</strong> formingscale when temperature is increased. The process requiresonly that the bulk supply <strong>of</strong> chemicals introduced be renewed from time to time, in theform <strong>of</strong> powder or spheroid concentrates.

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