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.
j44 SEA WATER DISTILLATION.
20. Sometimes the surface allowed for the surface
condenser is as follows One square foot of brass tube
(18 I.S.W.G.) surface per 30 lbs. of steam at a temperature
of 212° to 30 lbs. of water at about 100°, with the circu-
lation of 900 lbs. of sea water entering at about 50°, and
discharged at about 90°. This would be for ordinary
climates, but if the sea water used for the circulation is
in the tropics then the surface allowed is 1 square foot
per 16 to 20 lbs. of steam to be condensed.
AMe.—This works out as follows :—
966 units of latent heat in the steam,
112 degrees cooled down (212— 100 — 112).
1 ,078 (total) x 30 = 33,040 units of heat imparted by
the steam.
9 0° temperature of outlet circulation.
5 0° „ inlet
4 0° (difference) X 900 = 36,000 units.
That is to say, 33,040 units imparted to, and 36,000 units
of heat absorbed by the circulation water; which about
balances the heat given and received. If the surface
allowed is 1 square foot per 16 or 20 lbs. of water, other
conditions being the same, it gives almost double the
surface to be allowed for tropical climates.
3 . Dilution and Feed-Water Allowance.
21 As it is usual to take water for diluting the brine
from the lower part of the distiller casing, and more circu-
lation water from the upper part of the casing for evapor-
ator feeding, the total quantity of these two waters should