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
Søgning i bogen
Den bedste måde at søge i bogen er ved at downloade PDF'en og søge i den.
Derved får du fremhævet ordene visuelt direkte på billedet af siden.
Digitaliseret bog
Bogens tekst er maskinlæst, så der kan være en del fejl og mangler.
74
SEA WATER DISTILLATION.
there is still heat in the primary water draining from the
coils, which is generally cooled down to below 150°, so
that the heat in such primary water (from the point at
which it was converted into water) down to, say, 100°,
is available for heating the feed from, say, 100°, and this
should, therefore, be taken into account in a comparison
of the economy.
Note.—In practice the feed-water is not heated quite
up to the boiling point, nor is the primary water dis-
charged quite at the same temperature as the initial
temperature of the feed (100°).
18. We will, therefore, compare three typical cases, as
follows :—
(«)
( Primary pressure, 75 lbs. per square inch.
I Secondary pressure, 25 lbs „
(&)
J Primary pressure, 25 lbs.
I Secondary pressure, 0 lb.
(c)
J Primary pressure, 10 lbs.
I Secondary pressure, - 6 lbs.
(12" of mercury).
1st. Take the secondary heat required.
I n case (a) the secondary heat required is as follows :—
249 B.T.U.
927 „
For heating the feed-water from 100°
to 266° = 166°, and as the quantity
is 1| the evaporation, this would
be 266 - 100 x 1| = 249 B.T.U.
Latent heat to evaporate 1 lb. of
water at 25 lbs. pressure.
1,176
Total heat required.