28.12.2014 Views

Transactions A.S.M.E.

Transactions A.S.M.E.

Transactions A.S.M.E.

SHOW MORE
SHOW LESS

You also want an ePaper? Increase the reach of your titles

YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.

HOOPER—SALT-VELOCITY MEASUREMENTS AT LOW VELOCITIES IN PIPES 659<br />

rate of diffusion of the solution throughout a cross section due to<br />

turbulent mixing. The percentage of turbulence is certainly<br />

one of the components of the criterion, and includes not only the<br />

velocity, but also the roughness characteristics of the waterway.<br />

Obviously, a size factor of the conduit must also be included<br />

injthe criterion; for a closed channel the area, and for an open<br />

channel, either the wetted area or the hydraulic radius might be<br />

considered.<br />

A third factor, time, must be included. Considering percentage<br />

turbulence as a measure of the spatial rate of transport of<br />

solution throughout the water, it is evident that a certain time<br />

must elapse for the transport of a salt particle from, say, the center<br />

of the conduit to the wall, or vice versa. The time factor<br />

might then be expressed as the ratio of water depth or pipe diameter<br />

to the radial component of the turbulence fluctuations.<br />

The fractional portion of the linear dimension to be employed in<br />

this expression will, of course, depend upon the injection pattern.<br />

If a standard pattern of injection can be adopted the influence<br />

of injection procedure may be eliminated, and more important,<br />

the time factor may be very considerably reduced by the use of<br />

a well-distributed injection pattern.<br />

Assuming the foregoing analysis to be applicable and letting ut<br />

be the mean turbulence fluctuation; A the cross-sectional area<br />

of the channel; and T the time factor; the form of the mixing<br />

criterion might be<br />

M = u, A T ...................................... [1]<br />

having the dimensions L 3 of a volume.<br />

Because of the practical difficulty of measuring u„ it may be<br />

desirable to substitute for u, the expression11 lv, where I is the<br />

Prandtl mixing length, and v is the kinematic viscosity of the<br />

water. Experiment alone will determine the most satisfactory<br />

term to be used as a measure of the turbulent diffusion, the suggestions<br />

given herein being intended principally to indicate the<br />

nature of the term.<br />

The results of the author’s tests to determine the effect of<br />

gravity on the operation of the salt-velocity method are a further<br />

corroboration of the writer’s thesis1 that turbulence in the stream<br />

is the chief factor governing the accuracy of the method.<br />

E. A. T a y l o r .12 The author has described a study which<br />

gives a laboratory answer to a salt-velocity question which has<br />

arisen several times in the field. This question was: “When salt<br />

is introduced into a penstock does the higher specific gravity of<br />

the salt solution drive the salt through the water and toward the<br />

bottom of the penstock, thus changing the time of passage of the<br />

salt solution through the test section, and introducing an error<br />

in salt-velocity measurements”<br />

At many of the high-head power plants, where salt-velocity<br />

tests have been made, the penstocks have very steep slopes and,<br />

at some of them, the penstocks approach the vertical for considerable<br />

distances. If this difference in the specific-gravity question<br />

were important, then the computations for turbine efficiency<br />

at those plants might be appreciably in error.<br />

The results of the laboratory studies described by the author<br />

indicate that the effect of gravity on the salt-velocity method of<br />

water measurement is negligible, when proper salt mixing and<br />

distribution are secured.<br />

In 1939, the salt-velocity method of water measurement was<br />

used in making efficiency tests on the Colorado River Aqueduct<br />

pumps for the Metropolitan Water District of Southern California.<br />

During those tests, a field answer was found to the<br />

specific-gravity question. The question was raised at the Iron<br />

11 “ Modern Developments in Fluid Dynam ics,” edited by S.<br />

Goldstein, Oxford University Press, New York, N. Y., 1938, chapter 5.<br />

I! Consulting Engineer, Worcester, Mass.<br />

Mountain Pumping Station and the district engineers agreed to<br />

turn that plant into a field laboratory to study the subject.<br />

The regular salt-velocity test section, used for pump-efficiency<br />

tests at this plant, was 200 ft long, 100 ft from salt injection to<br />

the first set of electrodes, and another 100 ft to the second set of<br />

electrodes. For this specific-gravity study, two additional pairs<br />

of electrodes were installed in the 10-ft delivery pipe.<br />

These additional electrodes were called spot electrodes and<br />

consisted of small steel plates, 4 in. square and spaced 2 in. apart.<br />

These spot electrodes were fastened 5 ft beyond the regular second<br />

set of electrodes, making the length of test section used for the<br />

spot electrodes 105 instead of 100 ft. One pair of spot electrodes<br />

was located at the top of the pipe and the other pair at the bottom.<br />

During the study, the ammeter connections were alternated,<br />

shot by shot, between the two sets of spot electrodes.<br />

A total of 74 salt shots were made and computed in this study.<br />

Averaging the results of these shots showed that the passage time<br />

to the top spot electrodes was 0.04 sec less than the passage time<br />

to the bottom electrodes. This was regarded as a perfect check<br />

and a conclusive field answer to the gravity question.<br />

As further assurance of the accuracy of the salt-velocity method<br />

of water measurement and confirming the belief that any specificgravity<br />

error was too small to be seriously considered, two volumetric<br />

check tests have been made at Pacific Coast plants, one of<br />

them being a high-head plant with a steep slope in the penstock.<br />

For those check tests, a 3-acre forebay, 20 ft deep, and a 10-<br />

acre reservoir, 10 ft deep, were used as basins for the volumetric<br />

measurements. The volumetric results checked salt velocity,<br />

by 0.75 per cent at one plant and by 0.5 per cent at the other<br />

plant. The latter was the high-head steep-penstock plant where<br />

any gravity effect would be expected to be most apparent.<br />

The author’s conclusion, from laboratory tests, th at “for velocities<br />

lower than those normally found in practice, there exists a<br />

critical mixing velocity below which good mixing of the injected<br />

brine does not occur” is confirmed by some field tests recently<br />

made.<br />

Field efficiency tests were made on the Colorado River Aqueduct<br />

pumps in May and June, 1939. At Intake, the first station<br />

tested, the discharge values for single pumps checked the discharges<br />

when two or three pumps were operating together.<br />

At the second station tested, Gene, the results of the preliminary<br />

tests, comparing single- and multiple-pump discharges, did<br />

not check.<br />

At all five Colorado River Aqueduct pumping stations, one 10-ft<br />

delivery pipe carries the discharge from the three pumps now installed<br />

at each station. When only one pump is operating, the<br />

velocity in the delivery pipe is comparatively slow, about 2 fps.<br />

The inside of these delivery pipes is coated with an enamel finish,<br />

as smooth as glazed porcelain, and there are no rivet heads or<br />

other projections into the inside of the pipe.<br />

This combination of extremely smooth pipe and low velocities<br />

created a condition of low turbulence, too low for satisfactory<br />

salt mixing, during the passage of a shot. This accounted for<br />

the failure of the discharge values to check between single and<br />

multiple pumps.<br />

To provide more turbulence, an artificial agitator, called a “tur-<br />

bulator” was installed beyond the salt-injection station. This<br />

so-called turbulator was a steel disk, 6 ft in diam, fastened in the<br />

center of the delivery pipe and normal to the axis of the pipe.<br />

This disk had an 18 X 24-in. hole in the center and was located<br />

40 ft beyond the pop valves. The turbulator was used<br />

during the remainder of the pump tests and single-pump-discharge<br />

results checked the multiple-pump values.<br />

No artificial turbulator was required at Intake, because the<br />

salt-injection station was just above the manifold where the three

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!