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Book - School of Science and Technology

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Condensate h<strong>and</strong>ling equipment 221. Miscellaneous,includingLabyrinthThermodynamicImpulse.Some <strong>of</strong> these types are illustrated in Figure 8.18 but specialist texts* <strong>and</strong> manufacturers'literature should be consulted for specific details. It is usual to add auxiliarycomponents to the trap proper in order to make up what is called a trap set <strong>and</strong> thesewill probably include some or all <strong>of</strong>: a strainer at entry; a check valve at exit; a sight glass<strong>and</strong> isolating valves when appropriate. The choice <strong>of</strong> a trap type suitable for anyparticular application depends upon a number <strong>of</strong> factors; load characteristics (constantor fluctuating); inlet <strong>and</strong> outlet pressures; associated thermostatic or other controls to thesteam supply <strong>and</strong> the relative levels <strong>of</strong> trap <strong>and</strong> condensate piping, to name but a few.While it is not possible to generalise for all varieties <strong>of</strong> application, the trap patterns listedin Table 8.1 are generally suited to equipment within the scope <strong>of</strong> this book.In an ideal situation, a trap would discharge into a condensate main run below it <strong>and</strong>the main would then fall in level back to the boiler plant. Such an arrangement maysometimes be possible in an industrial building but it is very <strong>of</strong>ten the case that a trapmust discharge into a main above it; this is quite practicable provided that the steampressure at the inlet to the trap is always adequate to overcome the back pressure imposedby the water in the discharge pipe, Figure 8.19. In simple terms, an available steampressure <strong>of</strong> at least 10 kPa is required for each metre height <strong>of</strong> vertical `lift'.In instances where the steam using equipment is fitted with some type <strong>of</strong> thermostaticor other automatic control which takes the form <strong>of</strong> a throttling valve, it must beremembered that such a valve acts by causing a reduction in steam pressure to theequipment (<strong>and</strong> thus to the steam trap). In consequence, although the initial steam supplypressure to the control valve may be adequate to provide the required lift, this will not bethe case at low loads. It is always good practice, therefore, to avoid a situation wherecondensate has to be lifted from a trap serving equipment fitted with automatic control <strong>of</strong>steam input.Table 8.1 Steam traps: general applicationApplicationDrain points on steam mainsFan convectors (large)Natural convectors <strong>and</strong> radiatorsOil storage tank coils <strong>and</strong> outflow heatersOil tracing linesPlenum heating or air-conditioning heater batteriesStorage <strong>and</strong> non-storage calorifiersUnit beaters (small)Unit heaters (large)Type <strong>of</strong> steam trapMechanical open top, inverted bucket orthermodynamicMechanical ball float or inverted bucketThermostatic balanced pressureMechanical open top or inverted bucketThermostatic bi-metallic or thermodynamicMechanical ball float or inverted bucket: may bemultiple for large unitsMechanical ball float or open bucketThermostatic balanced pressureMechanical ball float or inverted bucket* Northcr<strong>of</strong>t, L. G., Steam Trapping <strong>and</strong> Air Venting. Hutchinson, 1945. Spirax-Sarco. Various excellentinstructional courses <strong>and</strong> texts.

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