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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84 THE STEAM INJECTOR.
heat energy leaves the injector in three forms. In the
first place, a portion, of same is converted into work (1
B.T.U. being the equivalent of 778 foot-pounds), and pro-
vides the propulsive force for imparting velocity to the
delivery jet; a second, and the greatest portion, serves to
give the delivery jet a high temperature; and a thi id
portion radiiates from the injector casing.
We will consider an injector working under the following
■conditions:—
St^am pressure, Ibs. per sq. inch absolute. Feed-water temperature. Height of lift. Pressure in injector, Ibs. per sq. inch absolute. Ratio of water to steam in Ibs. Delivery temperature. Delivery 1 pressure, Ibs. per sq. inch absolute.
95 Deg. F. 97 Ft. 2 5 13 to 1 Deg. F. 175 115
We can readily asoertain the quantity of heat energy
requirød to produce a delivery jet of a certain pres&ure if
the weight of the jet and also its temperature are known.
In the present case the weight of unit mass of the jet
may be taken as 1411®. (1 Ib. steam and 13 Ibs. water),
the delivery pressuæ is 110 Ibs. above the pressure within
the injector (which is 5 Ibs. per square inch absolute), and
the- fluid head equivalent of 1 Ib. pres-sur© when tlie fluid
temperature is 175 <leg. Fah. is 2'375 ft.
Heat energy required to produce the delivery jet
Mass in Ibs. * velocity2
Joule’s equivalent 2 g
W
= — x (Head equivalent of pressure of jet,
' in feet)
14
= WX (11° x 2‘375) •'
= 4'7 B.T. units approximately.