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Book - School of Science and Technology

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Steam systems - principles 251Figure 9.13 Connections to a radiator from a single-pipe circuitworks produced before 1950. The very fact that systems having connected loads <strong>of</strong> up to3 MW were designed on this basis may come as a surprise when viewed in the context <strong>of</strong>pressure availabilities <strong>of</strong> not much more than 4 or 5 Pa/m in comparison with the 100±500available today with pumped systems. It is no wonder that pipes <strong>of</strong> 200 mm diameter wererequired in boiler houses serving loads <strong>of</strong> this order <strong>and</strong> that the mass <strong>of</strong> calculationsnecessary was equally formidable!Steam systems - principlesAs will be obvious, no external motive force is required in any normal circumstances toproduce steam flow since pressure is inherent in the state. An argument can be developedas to the practical unit to be used for steam mass, as distinct from that which best suits thepurist approach. The most recent edition <strong>of</strong> the Guide Section C4 has retained kg/s inpreference to the far more useful unit <strong>of</strong> g/s listed in the 1970 edition. The latter equates toan energy supply unit <strong>of</strong> 2.25 kW <strong>and</strong>, moreover, permits working in whole numbersrather than with three or four decimal places.While reasonable care must be taken in the calculations leading to selection <strong>of</strong> pipe sizesfor steam service, it must be remembered that a number <strong>of</strong> imponderables exist in thatheat losses from the pipework, whether insulated or not, will lead to formation <strong>of</strong>condensate. In consequence, the steam pipe will be carrying a mixture <strong>of</strong> vapour <strong>and</strong>liquid, the proportions <strong>of</strong> the two components varying from time to time dependent uponthe external ambient air temperature <strong>and</strong> fluctuations in the rate <strong>of</strong> mass steam flow. Thevariables relating to flow <strong>of</strong> condensate are no less obscure since air <strong>and</strong> flash steam willaccompany the boiling water in pipes which are <strong>of</strong>ten only half full <strong>and</strong> are under achanging mixture <strong>of</strong> pressure influences.Calculation routinesFor selection <strong>of</strong> steam pipe sizes, the following information must be available:. The mass flow required, in g/s. For heating service this will equate to the energyrequirement in watts divided by the latent heat at the pressure <strong>of</strong> utilisation. Forkitchen or other equipment, the manufacturers' data must be consulted.. Where the steam main pipework is comparatively short, heat loss from it may beignored but, for extensive runs, use must be made <strong>of</strong> Tables 6.14 <strong>and</strong> 6.15 (p. 171)<strong>and</strong> the net requirement then adjusted to suit.. The initial pressure available at the steam source.. The minimum pressure required at the point <strong>of</strong> consumption.. Lengths <strong>of</strong> the various pipeline sections, with details <strong>of</strong> all single resistances.

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