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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INTRODUCTION.
3
force is obtained for carrying or injecting water into a
boiler under a pressure equal to or even higher than that of
the steam used.
If we consider the relationship betwæn water and
steam from a thermal standpoint by comparing the heat
energy represented by 1 Ib. of steam with that represented
by 1 Ib. of water at the same temperature and pressure as
the steam, we at once appreciate the advantag© of the
steam over the water as a mechanical force. It is a por-
tion of the superior force or excess of heat energy of the
steam, represented by its latent heat, which is utilised in
the injector for forcing water into the water space of the
boiler in which the steam was generated.
To illastrate the foregoing statements, we will consider
a jet of dry saturated steam issuing from a boiler at
10 Ibs. gauge pressure, which mingles with, and is ulti-
mately condensed by, a water je-t under atmospheric pres-
sure and a head of 2 ft., the ratio by weight of the mixture
being 1 Ib. of steam to 9 Ibs. of water.* At the point
where the steam and water unite a vacuum exists
(due to the condensation of the steam), and we will assume
this to be 20 in. meroury. The theoretical velocity of
dry saturated steam at 10 Ibs. gauge pressure issuing
into a vacuum of 20 in. mercury (5 Ibs. pressure per square
inch absolute) is about 2,330 ft. per second, and the
theoretical velocity of water under atmospheric pressure
and a head of 2 ft. into the same vacuum is about 40 ft.
per second. The resultant velocity of the combined jet
(condensed steam and water) per unit mass (1 Ib.) will
therefore be 269 ft. per second. f A water jet discharging
into a region at an absolute pressure of 5 Ibs. per square
inch with a velocity of 269 ft. per second would be
* In the rough calculations liere given, the effect of the temperature of the
water upon the results lias beeii ignored, so as to make the figures as simple as
po^sible. One pound pressure per square inch has been taken as equal to a water
head of 2'3 ft. The valnes have been calculated by formulæ given later.
t For: Momentum of steam jet + momentum of water jet
= momentum of combined jet
1 X 2330 + 9 X 40 = 2690;
i.e., 10 X velocity = 2690;
therefore velocity = 269 ft. per second.