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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MULTIPLE DISTILLATION. 183
less. Thus, although in double distillation the total pro-
duction is more than in single distillation, yet the second-
ary water is less than the primary water, and in treble
distillation, although the total production is more than
in double distillation, yet the tertiary water is less in
quantity than the secondary water, and so on.
Fourthly.—That although at each successive distillation
the production is less in degree (though more in total),
the evaporators all have the same amount of heating
surface. Thus, in quadruple distillation, although the
3rd evaporator affords only a gain of 5'2 tons, as against
8 tons by the 1st evaporator, both evaporators have the
same evaporative surface.
Fifthly.—That the combined or joint production (in
point of time) of all the evaporators in multiple distil-
lation is about the same as the production would be if
only one of the evaporators were used and worked with
the same pressures (initial and final) as the multiple
distilling apparatus. Uniform evaporators are understood.
Note.—To make this point clear—say that in treble
distillation the primary water is 10 tons in a fixed time,
and that the gained water (secondary and tertiary) in
the same time is 14’4, making a total mixed production
of 24'4 tons in the given time, and that the initial pressure
(boiler steam) is 75 lbs. per square inch, and the final
pressure in the 2nd evaporator casing is { lb. If, instead
of the evaporators being coupled together, the boiler steam
at 75 lbs. pressure went into the 1st evaporator, and the
pressure in that evaporator casing is reduced to lb.,
while the 2nd evaporator is cut out altogether, then the
existing surface of the 1st evaporator, with 75 lbs. steam
pressure inside the coil, would be capable of producing