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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THE D ELIVERY NOZZLE.
43
On the subject of the losses in diverging nozzles through
which water is flowing, Professor A. H. Gibson, D.Sc., has
conducted an extended series of experiments, the results of
which are given in an article entitled “ The Conversion of
Kinetic to Pressure Energy in the Fiow of Water through
Passages having Divergent Boutidaries,” which appeared in
Engineering of February 16th, 1912.
The most important portion of such article, so far as the
injector is concerned, is given below, by the kind permission
of the proprietors of the above-mentioned journal.
The article also deals with trumpet-shaped pipes or
nozzles, and it was fouud in this case tbat the most efficient
nozzles were those in which the loss of head per unit length
of the passage was constant. Compound pipes or passages
are also dealt with.
Referriug to uniformly tapering pipes, the writer states :
“It would naturally be supposed that by enlarging the
section gradually, shock and -consequent eddy formation and
loss of energy would be reduced, and to determine the
extent to which this conclusion is justified a series of experi-
ments on uniformly tapering pipes was carried out. Some
of these were of circular cross-section, others were square,
and others rectangular, with one pair of sides parallel. The
ratio of final to initial areas ranged between 2'25 to 1 and
9 to 1, the larger diameters being 3 in., while the larger end
of the square and rectangular pipes had the same area as the
circular pipes. The mean results of these experiments are
shown in figs. 22 and 23, from which the foHowing conclusions
are to be drawn :—
(a) In a circular pipe, with uniformly diverging boundaries,
the loss of head, expressed, hs a percentage of - v.i)1 4- 2 g,
varies somewhat with the mean diameter of the pipe, and
with the ratio of final to initial area, as well as with the
angle (9, between its opposite faces. For values of 0
between 6 deg. and 35 deg. the differences are comparatively
small, and the loss of head is given fairly accurately by—
Loss = 0-011 Ø1-22 feet,
2 <7
where t) is measured in degrees.