hydraulics branch official file copy united states … · 2017-11-13 · hydraulic laboratory of...

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l HYDRAULICS BRANCH OFFICIAL FILE COPY UNITED STATES DEPARTMENT OF THE INTERIOR BUREAU OF RECLAMATION HYDRAULIC MODEL STUDI E S OF M ETHO DS TO D I S S IP ATE THE HIGH-VE L OC ITY ,TET FROM THE R EGULATING VALVE IN TECOLOTE TUNN EL- - SA NTA BARBARA PROJECT., CALIFORN IA Hydraulic ;Laboratory Report,No. Hyd. -287 RESEARCH AND GEOLOGY DIVISION BRANCH OF DESIGN AND CONSTRUCTION DENVER, COLORADO February 13, 1�51

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Page 1: HYDRAULICS BRANCH OFFICIAL FILE COPY UNITED STATES … · 2017-11-13 · Hydraulic Laboratory of the Research and Geology Division collabo ... designed to break up the jet from the

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HYDRAULICS BRANCH

OFFICIAL FILE COPY UNITED STATES DEPARTMENT OF THE INTERIOR

BUREAU OF RECLAMATION

HYDRAULIC MODEL STUDI E S OF M ETHO DS TO

D I S S IP ATE THE HIGH-V E L OC ITY ,TET FROM THE

R EGULATING VALVE IN TECOLOTE TUNN EL- ­

SA NTA BARBARA PROJECT., CALIFORN IA

Hydraulic ;Laboratory Report,No. Hyd. -287

RE SEARCH AND GEOLOGY DIVISION

BRANCH OF DESIGN AND CONSTRUCTION DENVER, COLORADO

February 13, 1�51

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Purpose . Conclusions Recommendations Introduction The Investigation

The Model . The Stilling Basin Tunnel Baffles .

Single baffle Two baffles

CONTENTS

Two baffles and a valve flow -guide Pressures in flow guide

Muffler Type Stilling Device

FIGURE LIST

Page

1 1

2 2 3

3 3 4

4 4 4 5

5

Figure

Location Map. . . . . . . .. . , . . . . . . . . . . 1 Gate Chamber and Elevator Shaft;. Sections and Details , 2 Valve of the 1: 10 Scale Model Discharging into Tunnel

with no Provision for Stilling the High Velocity Jet 3 Stilling Basin with Baffle Piers- -Optimum Design , 4 Operation of the 1: 10 Scale Model with the Optimum

Design Stilling Basin with Baffle Piers. . . . . 5 Final Design--Tunnel Baffles and.Valve Flow Guide. 6 Operation of the 1:10 Scale Model of the Final Design

Tunnel Baffle Arrangement . . . . . . . . . . 7 1: 10 Scale Models. . . . . . . . . . . . . . . 8 Operation of 1: 10 Scale Mod.el of Stilling Basin Designs- -

without Baffle Piers . . . . . . . . . . . . . . . . 9 Representative Tunnel Baffles . . . . . . . . . . . . 10 Operation of 1: 10 Scale Model of Tunnel Baffle Designs with

Flow of 100 cfs and 104 Feet Head on Valve 11 Pressures in Flow Guide--Final Outlet Design. . 12 Proposed Muffler Type Stilling Device . . . . . 13 Operation of a 1: 10 Scale Model of a MufUer Type

Stilling Device . . . . . . . . . . . . . . . 14

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.,

UNITED STATES DEPARTMENT OF THE INTERIOR

BUREAU OF RECLAMATION

Branch of Design and Construction Research and Geology Division Denver, Colorado

Laboratory Report No. 2R7 Hydraulic Laboratory Compiled by: L. R. Thompson Reviewed by: W. C. Case February 13, 1951

J. W. Ball

Subject: Hydraulic model studies of methods to dissipate the high­velocity jet from the regulating valve in Tecolote Tunnel-­Santa Barbara Project, California

PURPOSE

To determine the most suitable method of dissipating the energy in the jet from the regulating valve to obtain smooth, free flow in the tunnel into which it discharges.

CONCLUSIONS

1. Two methods, equally satisfactory from a hydraulic viewpoint, to dissipate the valve jet energy are:

(a) A rectangular stilling basin containing floor blocks, with optimum dimensions as shown in Figures 4 and 5.

(b) Two baffles in the tunnel downstream from the valve in combination with a "flow guide" on the valve (Figures 6 and 7).

2. For both methods the jet from the valve must be completely submerged for satisfactory operation.

3. There is no significant difference in the flow pattern whether a needle, tube, or a butterfly valve of the pivot type is used.

4. No objectionable subatmospheric pressures are present in the valve flow guide of method 1 (b) as evidenced by the lowest recorded pressure of 1. 25 feet of water above atmosphere at 25 cfs discharge and 104 feet head on the valve (Figure 12).

5. At the maximum discharge of 100 cfs, the valve discharges against a head of 9 feet of water at the valve centerline when the stilling­basin is used, and 5 feet of water when the flow guide and two tunnel baffles are used.

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6. With regard to the tunnel baffles, the optimum open area in the upstream baffle is about twice the area of the jet, or one-fourth the area of the tunnel. Best results are obtained with the openings uniformly dis-­tributed over the baffle (Figure 6). The downstream baffle should be in the shape of a weir with the crest near the horizontal centerline of the .. tunnel to insure adequate submergence of the valve jet at low discharges.

7. The muffler type stilling device (Figures 13 and 14) has many desirable characteristics which merit its consideration for future instal­lations. Further study is required to establish its practicability and opti­mum dimensions.

RECOMMENDATIONS

1. Use the jet dissipation method utilizing tunnel'baffles and .a/. flow guide. It ·will re.quire less· ex.cavation .than the stilling ,basi�; · the valve will not have to be lowered below the elevation of the tunnel, which would require a bend in the pipe upstream of the valve; and the valve will discharge against a slightly lower head.

2. Vent the tunnel immediately downstream from the downstream baffle to insure an adequate air supply to the tunnel.

INTRODUCTION

Tecolote Tunnel, approximately 6. 4 miles long, is a 7-foot­diameter, horseshoe-shaped tunnel outlet for the Cachuma Reservoir of the Santa Barbara Project (Figure 1). Its purpose is to supply supple­mental domestic water to the city of Santa Barbara, California, and to add to the irrigation water supply for approximately 30, 000 acres of land.

An operating chamber, housing a venturi type meter and the regulating valve, is located in the 7-foot horseshoe tunnel about 800 feet from the inlet. Figure 2 shows the final design which incorporates the model test results.

The outlet is required to release a maximum flow of 100 cfs between heads of 20 and 104 feet and is expected to operate at various heads and quantities between these limits.

If the jet from the valve was admitted directly into the tunnel as shown in Figure 3, the tunnel walls might be damaged or undesirable waves might occur downstream. Hydraulic model studies were made to evolve some means of stilling the high-velocity jet from the valve such that the flow would pass smoothly through the tunnel at subcritical veloc­ity. The stilling process involves a pressure recovery from the velocity head of the jet and an energy dissipation in the form of friction between the jet and slow-moving water into which the jet discharges. A system

2

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designed to accomplish this process would have to include,(U ja flow area greater than that of the jet to permit a reduction in velocity, (2) a restriction of the flow to provide sufficient backwater to keep the jet submerged at all heads and discharges, and (3) some means of dispers­ing the jet to distribute the velocity, and increase the turbulence and eddy losses.

Members of the Canals Division, Mechanical Division and the Hydraulic Laboratory of the Research and Geology Division collabo­rated in developing the final design on the basis of the results of the hydraulic model studies discussed in this report.

THE INVESTIGATION

The Model

A 1: 10 scale model was constructed to include the regulating valve, a stilling basin, and 200 feet of the 7-foot-diameter horseshoe tunnel downstream from the valve (Figure 8). A 3. 2-inch-inlet-diameter tube valve, a 3. 0-inch-inlet-diameter needle valve and a 3. 0-inch but­terfly, pivot-type valve were used in the model tests. The stilling basin consisted of a box 8. 4 inches wide with an adjustable floor and ends so that the length and depth of the stilling basin could be varied. One side of the box was made of glass to permit observation of the flow conditions in the basin. The model tunnel was an 8. 4-inch-diameter horseshoe pipe made of transparent plactic in sections 6, 12, and 24 inches long. The stilling basin could be removed entirely so the valve could discharge through a flow guide directly into the tunnel. With this arrangement, baffles made of 16-gage steel were bolted between the flanges of the plastic pipe to give the effect of a stilling basin in the tunnel. One section of tunnel was fitted with a standpipe to determine the effect of venting. Tail-water elevation was controlled by an adjust­able weir plate on the end of the tunnel. Discharge was measured with an orifice meter, and the head on the valve was measured with a mer-e ury manometer.

The Stilling Basin

The model stilling basin lengths reHresented prototype lengths varying from 22 to 76 feet and prototype depths from floor to tunnel in­vert of 5 to 15 feet. Without physical aids such as floor blocks no prac­ticable combination of length and depth gave desirable flow conditions (Figure 9). Blocks of various shapes and spacings installed on the basin floor improved the stilling action; but all deflected some water vertically, giving rise to boils and surface rolls. Finally, a "flow guide" consisting of three triangular blocks, surmounted by a cover plate to control the vertical flow, was developed, which gave a very smooth water surface at all heads and discharges. This arrangement with the most satisfac­tory stilling-basin dimensions is shown in Figures 4 and 5.

3

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This arrangement was tested with a tube, needle, and pivot­type butterfly valve. The type of valve used made no apparent difference in the stilling action of the model basin. The water level in the basin was 9 feet above the centerline of the valve at the maximum discharge of 100 cfs.

Tunnel Baffles

Single baffle. The possibility of accomplishing the desired stilling action without using a conventional type of stilling basin was next investigated. Baffle plates of varying designs (Figure 10) were tested singly in the tunnel at various locations. In order to get even flow dis­tribution through the baffle, the open area of the baffle had to be in the form of openings spaced uniformly over the face of the baffle. If the open area was made small enough to maintain sufficient backwater to keep the jet submerged at all discharges, the velocity through the baffle plate was high and caused objectionable turbulence immediately down­stream from the baffle. Thus, one baffle was insufficient (Figure llA).

Two baffles. A system of two baffles was evolved which oper­ated well for one particular head and discharge. In this case, the up­stream baffle had widely distributed openings that broke up the jet action and gave even flow distribution. Also, the open area was large enough t o give appreciable velocity--reduction. The second baffle was in the form of a weir to provide the backwater necessary to keep the jet submerged. The weir-type baffle was particularly needed for combinations of high heads and low discharges, since the normal tail-water elevation in the . tunnel was low for these discharges. The operating range of the two­baffle system was limited by the amount of open area in the upstream baffle. If the amount of open area was too small, the head against which the valve must discharge became restrictive and the velocity through the baffle was too high (Figure l lB). If the amount of open area was too great, the jet was not sufficiently diffused and flow distribution through the baffle was poor, causing objectionable turbulence downstream from t he baffle. Also, too great an open area in the baffles resulted in sub­atmospheric pressures in the tunnel below the valve, and air was drawn into the tunnel through the standpipe. This served to reduce the submer­gence of the jet, resulting in even greater turbulence.

Two baffles and a valve flow-guide. It appeared that the satis­factory flow range of the two-baffle system could be greatly increased by securing even velocity distribution before the water reached the upstream baffle. Since a concrete wall separates the valve house from the tunnel downstream, a steel flow-guide, bolted to the valve, extending through the concrete wall and connecting to the tunnel is necessary. Since turbu­lence in the flow-guide was not considered objectionable, the guide was designed to break up the jet from the valve to obtain better flow distri­bution of the water into the tunnel. The design developed (Figure 6) was very effective in breaking up the jet action and producing an even flow distribution into the tunnel. This flow-guide, in combination with two baffles i.n the tunnel, constitutes a stilling device which is effective over

4

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the entire range of heads and discharges anticipated for the Tecolote .' Tunnel (Figure 7). With this arrangement no air is taken through the standpipe and the water does not rise into the standpipe, indicating atmospheric pressure in the tunnel.

The model studies indicated that the minimum distance between baffles and between the flow-guide and the first baffle is 10 feet. This distance may be increased without adversely affecting flow conditions in the tunnel. The shape of the individual openings in the baffles made no apparent difference; the important feature of each baffle was the amount and the distribution of the open area in the baffle.

Pressures: in.flow..:guide. Pressure readings at points in the flow-guide assembly described above where low pressures were most likely to occur disclosed that no subatmospheric pressures existed (Figure 12). The lowest pressure was 1. 25 feet above atmospheric pres­sure which occurred at 25 cfs discharge and 104 feet head on the valve centerline. The head against which the valve discharged was 5 feet of water on the valve centerline at a discharge of 100 cfs.

Muffler Type Stilling Device

The possibility of developing a muffler type stilling device con­sisting of two concentric cylinders that could be bolted to the end of a regulating valve was proposed by the Mechanical Division (Figure 13). Since the Tecolote Tunnel model could be readily adapted to testing such a device, a preliminary test was made at this time, and the test results were not intended to be applicable to the Tecolote problem. A sheet metal inner cylinder, closed at the downstream end, 5 feet in diameter, 10 feet long, had four rows of 7½-inch-diameter holes on longitudinal centerlines 90° apart. Each row had four holes spaced 20 inches from center to center; the upstream hole in each row was located 20 inches from the valve end. The inner cylinder was bolted to the tube valve. The outer cylinder shown in Figure 13 was represented by the model plastic tunnel. A slotted baffle plate was installed in the tunnel, 40 feet downstream from the cylinder, to provide tail water which kept the in­ner cylinder submerged (Figure 14). It appeared from the limited tests made that this arrangement has good possibilities as a stilling device. Further study is warranted where installation of this stilling device may be practicable .

5

Interior - Reclamation - Denver, Colo.

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CAL/FOR ��NTERIA NIA I !1���

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Jet impinging directly on t unnel lining- -f low 1 0 0 cfs . Head on valve 1 0 4 feet .

TEC OLOTE TUNNE L

F igure 3 R eport Hyd 2 8 7

V alve o f the 1 : 1 0 Scale Model discharging into the tunnel w ith no provis ion for st illing the H igh V elocity J et .

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A . F low 1 0 0 cfs . H ead on valve, 1 04 feet

B . Flow 2 5 cfs . H ead on valve 1 04 feet

TEC OLOTE TUNNE L

F igure 5 Report Hyd 2 8 7

Operation of the 1 : 1 0 Scale Mode l w ith Optimum D e s ign Stilling Bas in w ith Baffle P iers .

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A . F low 1 0 0 cfs . H ead on valve , 1 0 4 feet

B . F low 2 5 cfs . Head on valve , 1 0 4 fe et

TEC O LOTE T UNNE L Operation of the 1 : 1 0 Scale Model of the F inal D esign Tunnel Baffle A rrange ment .

F igure 7 Report Hyd 3 8 7

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FI G U RE 8 Report Hyd. 287

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F igure 9 Report Hyd 2 8 7

A . Basin length 3 2 feet ; height from basin floor to tunnel invert, 9 . 6 feet

B . Bas in length 7 6 fe et; he ight from basin floor to t unnel invert, 1 4 . 5 feet

TEC OLOTE TUNNE L Operation of the 1 : 1 0 Sc ale Model of St illing Basin D e signs - without baffle piers - F low of 1 00 cfs with 1 04 foot Head on Valve . F low fro m R ight to Left .

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TEC OLOTE TUN NE L Repres entative Tunnel Baffles

1 : 10 Scale Model

F igur e 1 0 Report Hyd 2 8 7

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A . One tunnel baffle 1 5 feet from va1ve

F igure 1 1 Report Hyd 2 8 7

B . Two tunne l baffle s , 1 0 and 1 5 feet from valve . Note high water level in standpipe and the turbulenc e be low the s e cond baffle .

TEC OLOTE TUNNE L Operation of 1 : 1 0 S c ale Model of Tunnel Baffle Designs with F low of 1 0 0 cfs and 1 0 4 foot head on Valve .

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P I E Z O M ET E R - ,

L O O K I N G DOWNSTR EAM S I DE V I E W

F LO W G U I D E

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P I E Z O M E T E R PRO T O T Y P E

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I : I O S C A L E M O D E L

F I G U R E 1 2 Report Hyd . 2 8 7

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A . F low 2 0 cfs . Head on valve , 1 1 feet

B . F low 1 0 0 cfs . H ead on valve, 1 0 4 feet

TEC OLOTE T UNNE L

F igur e 1 4 R eport Hyd 2 8 7

Operation of a 1 : 1 0 s c ale model of a m uffler type s t illing devic e .

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