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
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.
98
______________________________
THE STEAM INJECTOB.
difference between atmospheric pressure and tlie pressure
within the injector) is :
______
V = 7 2
= J 2 x 32-2 (2 + 12 x 2-3)
= 44 ft. per second.
[One pound pressure per square inch is taken as equal to
a water head of 2’3 ft.]
The steam nozzle throat area is now obtained thus—
. _ C (a?2 u-i)
1 s “ B x V'
_ 4 (-956 x 8-1)
13-3 x 1469
= 00158 square foot.
The velocity imparted to the water is obtained as follows :
Momentum Momentum _ Momentum of
of steam + of water ~ delivery jet
1 x 2606 + 13-3 x 44 = 3191 ;
therefore velocity of delivery jet = 223 ft. per second. This
would give the delivery nozzle throat area as—
__________4j<_143
d ” 13 3 x 624 x 223
= ‘00031 square foot.
We thus find that the ratio of areas of steam nozzle
throat to delivery nozzle throat is about 5’1 to 1. In
actual practioe, for the conditians statecl, the said ratio
would be about 3 to 1.
We have already shown that the delivery jet of an
injector only represents the expenditure of a very small
portion of the heat energy of the steam which is available
for imparting velocity to said jet. In the example
oaloulated the delivery jet, instead of having- a velocity
of 223 ft. per second, would probably have a velocity of
about 136 ft. per second,—that is, about 25 per cent more