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.
77
the same at any pressure such steam is generated, or in
other words, the “ sensible ” heat plus the “ latent ” heat
almost equal the same total heat, at any pressure. (See
Table E, p. 33; also Note on p. 49.)
The above economy is, of course, quite a different
matter from the economy that is obtained by multiple
distillation, which is treated of in the chapter on Multiple
Distillation.
Steady Ebullition.
20. The secondary steam, at whatever pressure it is
generated, should rise steadily from the surface of the
sea water, and not in gulps, otherwise there will be a
tendency to priming—i.e., particles of sea water being
blown up with the secondary steam, and carried over
with it, so as to impair the good quality of the water
condensed from the secondary steam. Baffles are some-
times fitted in the steam room to prevent priming, such
baffles being of various designs to arrest these particles
of sea water, and bring them down again into the sea
water. More will be said as to this when the subject of
“ brine area ” or “ steam delivery area ” is dealt with.
Secondary Steam Valve.
21. The pipe from the evaporator leading the secondary
steam away to be condensed is sometimes fitted with a
valve. The object of this valve is to regulate the flow of
secondary steam, where there is a minus pressure in the
condenser. Or such valve may be used to shut off
altogether the secondary steam, so as to get up a pressure
in the evaporator casing for the purpose of blowing away
the brine at intervals, if required. This will, however,