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.