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Book - School of Science and Technology

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216 Pumps <strong>and</strong> other auxiliary equipmentmargin but it is almost inevitable that at some time during the life <strong>of</strong> the system there will be apump failure <strong>of</strong> some sort: it is usual therefore not to rely upon this added margin.The required volume <strong>of</strong> the cylinder, if left uninsulated, is a function <strong>of</strong> the polytropicexpression where PV n is a constant. It has been found by experiment that n ˆ 1:26approximately <strong>and</strong> thus the movement <strong>of</strong> the water level may be calculated from:a ˆ h (1 e 0:794 )wherea ˆ movement in the water level (m)h ˆ height <strong>of</strong> gas space prior to the start <strong>of</strong> compression (m)e ˆ P 1 /P 2P 1 ˆ initial absolute pressure in gas space (kPa)P 2 ˆ final absolute pressure in gas space (kPa)Control <strong>of</strong> the pump <strong>and</strong> spill valve is greatly simplified if the movement <strong>of</strong> the waterline in the pressure cylinder is at a maximum: this movement is independent <strong>of</strong> thediameter <strong>of</strong> the cylinder but that dimension must be considered in conjunction with theduty <strong>of</strong> the pressure pump which should have a realistic running time <strong>of</strong> at least twominutes between start <strong>and</strong> stop when restoring the water level. The pump duty is afunction <strong>of</strong> the rapid contraction which would take place if the boilers were to be shutdown in emergency while the circulation continued.Application <strong>of</strong> pressurisationAlthough the equipment <strong>and</strong> packaged units which have been described under the precedingthree headings were suggested as being appropriate to low, medium <strong>and</strong> hightemperature heating systems in that sequence, this was merely to note that they were <strong>of</strong>tenso applied. There is <strong>of</strong> course no reason why packages for pumped or gas pressurisationshould not be applied to any category <strong>of</strong> system provided that they have been designed tosuit the pressure <strong>and</strong> volume conditions obtaining <strong>and</strong> that their use can be justified ineconomic terms.Non-storage calorifiersA calorifier is a heat exchanger, i.e. an item <strong>of</strong> equipment used to transmit heat from onefluid, at a higher temperature, to another at a lower temperature. The non-storage pattern,which is the subject <strong>of</strong> the following paragraphs, is so called to distinguish it from thoserelated to hot-tap supplies which are large by comparison <strong>and</strong> provide a reservoir <strong>of</strong> hotwater. While non-storage calorifiers are manufactured to suit either steam or water as thehigher temperature source, the latter are now less commonly used for duties such as thatwhich was shown in Figure 6.5(a), the function they fulfilled now being dealt with byinjection circuits as Figure 6.5(b). They are, however, still required for particular applications,such as the heating <strong>of</strong> chlorinated swimming pool water, where separation betweenthe higher temperature (primary) <strong>and</strong> lower temperature (secondary) contents is necessary.Subsequent references here are directed principally to steam-to-water types butapply with little revision to water-to-water equipment.

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