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 DISTILLING CONDENSER. I 37
It may be admitted (1) at, (2) below, or (3) above, the
ordinary atmospheric pressure. The most convenient
pressure is (1). In this case the gained steam at ordinary
atmospheric pressure simply enters the tubes at the ordi-
nary atmospheric pressure (valve at (A) is really not
a necessity), is condensed into water, which falls into the
bottom pan, and flows to where it is desired. In case
(2), if the secondary steam or vapour enters the tubes
beloio atmospheric pressure, a pump must be used to suck
away the water from (B), which causes a sucking action
at (A), so that the valve at (A) will have to be regulated
by hand, as the low pressure inside the tubes (T) varies.
In case (3) also the valve at (A) will need occasional regu-
lation, and a valve will be needed at (B) to keep up the
pressure in the tubes (T). Put shortly, the system of
working at ordinary atmospheric pressure, as in case (1),
accommodates itself at once to an automatic working
between evaporator and distiller, which can hardly be
said of cases (2) and (3).
5. When the distilled water is required for boiler feed,
it is usually specified that it shall be delivered from the
apparatus at a temperature not exceeding 150°, other-
wise it could not be satisfactorily measured.
(6 ) For Cold Distilled Water—Drinking Water.
7. Let us now examine the type of distiller required to
produce the distilled water cold.
8. It differs from the distiller for feed-water chiefly in
the form of surface—that is to say, a cooling surface has
to be added for cooling the water. This may be con-
veniently provided by having a set of cooling tubes
placed under the condensing tubes, as shown in Fig. 18.