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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72
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SEA WATER DISTILLATION.
before, of 1,134 units. But as the primary pressure is
now 25 lbs. per square inch, with a latent heat of 927 units,
the economy will be 1,134 - 927 = 1’22, assuming that
the sensible heat still left in the primary water is
wasted ; but if it is not wasted and is used (say for feed-
water heating) so as to reduce it to, say, 150°, then the
economy will be as follows :—
927 the latent heat of the primary steam at
25 lbs. pressure.
116 the sensible heat left in the primary water
after reducing it to 150° (266 - 150=116).
_____
1,043 B.T.U. total.
____
The economy will then be 1,134 * 1,043 = 1 087__i.e.,
1 087 economy, or 1’087 lbs. of primary steam to obtain
1 lb. of secondary or gained steam.
13. If, lastly, the primary pressure is at 75 lbs. per
square inch, the economy will work out as follows :—
There will be the 1,134 units to provide for, as before.
Then to meet this requirement we shall have as follows :__
888 the latent heat of the steam at 75 lbs. pressure, and
if no use is made of the sensible heat, 277° left in the
primary water, the economy will be 1-277—i.e., 1,134 4-
888. If, however, the heat in the primary water is used,
so as to lower it from 320° down to, say, 150°, the economy
will then be as follows :—
888 the latent heat, as before.
170 the sensible heat (320 - 150 = 170).
1,058 B.T.U. total.
So that the economy will then be 1,134 1’058 = 1'07,