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.

Download PDF

Digitaliseret bog

Bogens tekst er maskinlæst, så der kan være en del fejl og mangler.

Side af 162 Forrige Næste
THE COMBINING NOZZLE. 29 water temperatures. Further, if the proportion of steam to water is increased or diminished, the cross-sectional area of the combined jet will be altered, as may also the rate of condensation of the steam. The velocity of the incoming steam and also of the water may vary either simultaneously or independently. The boiler or counter-pressure against which delivery is being effected may also alter. These points must affect any decision as to the best form of nozzle to be employed. Thus to set the variable quantities out in full, they are : — (i.) Density of steam. (li.) Temperature of steam. (iii.) Temperature of feed water. (iv.) Ratio of steam to water. (v.) Velocity of incoming steam. (vi.) Velocity of incoming feed water. (vii.) Pressure in vessel being fed. It is obviously impossible to design any one nozzle to meet, with the greatest efficiency, all the conditions which arise even under the most favourable circumstances. The nozzle must therefore be designed to suit certain conditions which are a mean between the extremes likely to occur in service; but this is not easily done. The difficulty in decid- ing upon the best proportions for the combining nozzle is evidenced by the variety found in the appliances of high- class inanufacturers. Thus, combining nozzles of live steam injectors vary in length from, about 9 to 24 times the diameter of the delivery nozzle throat, this measurement being taken between the exit of the steam nozzle or, if two such nozzles are employed (see fig. 1 of the forcing steam nozzle and the throat of the delivery nozzle. The distance between the exits of the lif ting and the forcing steam nozzles, which also forms a por- tion of the combining or mixing area of the injector, varies between four to eight times the diameter of the throat of the delivery nozzle. For what is known as “hot-water” injectors, that is, injectors designeel to deal with high-pressure steam and hot feed water, the length between the forcing steam nozzle