The Steam Injector
A theoretical and practical treatise on the design and operation of injectors and on the flow of fluids through and the design of nozzles.
Forfatter: V. A. B. Hughes
År: 1912
Forlag: The Technical Publishing Company Limited
Sted: London
Sider: 145
UDK: 621.176
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PRINCIPLES OF THE 1NJECTOR.
81
The velocity of a jet of water issuing into a. region at a
pressure of 3 Ibs. per 'square inch absolute from the boiler
(under a pressure of 75 Ibs. per square inch absolute)
supplying the steam for the steam jet aforesaid would be
an amount due to the fluid head equivalent of the boiler
pressure above 3 Ibs. per square inch absolute (i.e., of
72 l)bs. per square inch). Taking 1 Ib. pressure per square
inch to be equivalent to a head of 2'3 ft., the total fluid
head is ]65‘6ft.
Now velocity in feet per second
— J2 g x head in feet
= 764-4 x 165-6
= 103-2.
It will thus be seen thai the oondensed steam jet has a
velocity of 3,250 ft. per second, whilst the boiler water jet
has a velocity of only 103 ft. per second, the original pres-
sures of the steam and water being the same. Obviously
if the two jets were directed against one another in a pipe
the oondensed steam jet would very easily overcome the
boiler water jet and enter the boiler. In this case, hov-
ever, we are only delivering back into the boiler what has
been takem therefrom.
Let us consider the case where, instead of the steam jet
being condensed in an extei'nally-cooled nozzle, it is
directly mixed with water for the same purpose, and let
us assurne that the ratio by weight of the mixture is
15 Ibs of wat-er to 1 Ib. of steam. The wiater av© will
assume to be supplied under a head of 2 ft.
Assuming tha.t the pressure in the mixing nozzle is main-
tained at 3 Ibs. per square inch absolute, due to tihe cotl-
densation of tbe ste'atm by the water, the velocity of tli©
steaim jet will be, as be<fore, 3,250* ft. per second.
The velocity of the water entering the miximg nozzle will
Ije an amount due to the head equivalent of the difference
between atmospheric pressure plus a head of 2 ft. and the
pressurewithin thenozzle. (If the water had been “lifted”
to the nozzle through 2 ft. inlstead of being supplied undor
7 si