A Practical Manual On Sea Water Distillation
With A Description Of The Necessary Machinery For The Process
Forfatter: Frank Normandy
År: 1909
Forlag: Charles Griffen & Co., LTD.
Sted: London
Sider: 244
UDK: 663.6
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THE EVAPORATOR.
121
much distilled water. The further use of such exhaust
steam in an evaporator coil is, therefore, not a waste of
coal fuel, in the manner that the alternative use of live
steam would be, as such extra live steam would be
converted into primary water without having done any
previous work.
Note.—To ascertain the economy, it is necessary to see
exactly what amount of heat (say per hour) is supplied
to the evaporator in the way of primary steam, and then
how much is used, and how much is returned by the coil
drain, or rather how much, after the primary water has left
the heater.
Heater Surface.
117. The amount of surface put in a heater differs
amongst makers according to the type of heater used,
the heat given to the feed, and the temperature
at which the discharged primary water is to be.
These and other considerations make it impossible to
give an inflexible rule for the amount of surface. It
is sufficient to say that the heating surface of the
heater will always have some relation to the evapor-
ative surface of the evaporator. But this great dis-
tinction must be kept in view—viz., that in the evaporator
coil, the heat that is imparted is the “ latent ” heat of
the primary steam yielded when reduced to water, whilst
the heat that is imparted in the heater coil is only the
“ sensible ” heat left in the primary water which has just
become liquefied, and, therefore, deprived of the latent
heat that was available in the primary steam. Roughly
speaking, the “sensible” heat thus available in the
heater coil is about one-eighth of the “ latent ” heat that
was imparted in the evaporator coil. It must be borne