AD-A142 186 21ST PUMP ING STATION RETTENDORFAOWA …

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AD-A142 186 21ST STREF PUMP ING STATION RETTENDORFAOWA HYDRAULIC 1/I MD EVSAONUAMEUEE AEWEXPER MENT STA ON V CKSBRR MS NDNA. R R COPELAND UNCLASSIF IED APR 84 WES/TN HL84-5 U/ 13/2 N -E ; hEh1h

Transcript of AD-A142 186 21ST PUMP ING STATION RETTENDORFAOWA …

AD-A142 186 21ST STREF PUMP ING STATION RETTENDORFAOWA HYDRAULIC 1/IMD EVSAONUAMEUEE AEWEXPER MENT STA ON V CKSBRR MS NDNA. R R COPELAND

UNCLASSIF IED APR 84 WES/TN HL84-5 U/ 13/2 N

-E ; hEh1h

1111 1. 12 .0

IIIl'2liiiiiiiiiii~lj ___ __ 1.

V TECHN9k ,REPORT HL-84-5

US Amy Crps21st STREET PUMPING STATION,of EngneersBETTENDORF, IOWA

I , - . HYDRAULIC MODEL INVESTIGATION

by

Ronald R. CopelandHydraulics Laboratory

___ U. S. Army Engineer Waterways Experiment Staton-P. 0. Box 631, Vicksburg, Miss. 39180

94

f 01

w i t ' , -- -a II 4~ELECTEN

p.JU Api 19194

Fina ReorPe a pp rovedS.FArm P Ebl i n eer itit Roc l and

LABO ATOY Rck slan, 11. 120"0 845

* I Destroy this report when no longer needed. Do notreturn it to the originator.

The findings in this report are not to be construed as anofficial Department of the Army position unless so

designated by other authorized documents.

The contents of this report are not to be used foradvertising publication, or promotional purposesCitation of trade names does not constitute anoffic:al endorsement or approval of the use of such

commercial products.

V

UnclassifiedSECURITY CLASSIFICATION OF THIS PAGE (When Dete Entered)

REPORT DOCUMENTATION PAGE BEFORE COMPLETIG FORM

A.RREPORT NUMBER SjIIENTS CATALOG NUMBER

Technical Report HL-84-5 A) T4 I T A4. TITLE (ad Subtitle) S TYPE OF REPORT & PERIOD COVERED

21st STREET PUMPING STATION, BETTENDORF, IOWA; Final reportHydraulic Model Investigation *. PERFORMING ORO. REPORT NUMBER

7. AUTHOR(e) S. CONTRACT OR GRANT NUMBER(e)

Ronald R. Copeland

S. PERFORMING ORGANIZATION NAME AND ADDRESS 10. PROGRAM ELEMENT. PROJECT. TASKAREA & WORK UNIT NUMBERS

U. S. Army Engineer Waterways Experiment StationHydraulics LaboratoryP. 0. Box 631, Vicksburg, Miss. 39180

11. CONTROLLING OFFICE NAME AND ADDRESS 12. REPORT DATE

U. S. Army Engineer District, Rock Island April 1984Clock Tower Building IS. NUMBER OF PAGESRock Island, Ill. 61201 77

14. MONITORING AGENCY NAME & ADDRESSIf different from Contolli.J Offlce) IS. SECURITY CLASS. (of thile report)

UnclassifiedISe. DECLASSI FICATION/ DOWNGRADING

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1. DISTRIBUTION STATEMENT (of thl Report)

Approved for public release; distribution unlimited.

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IS. SUPPLEMENTARY NOTES

Available from National Technical Information Service, 5285 Port Royal Road,Springfield, Va. 22161

It. KEY WOROS (Continue mn re ere elde It neceem and Identify by block nuiber)

Pumping stations--Iowa. (LC)Hydraulic models. (LC)Hydraulic machinery. (LC)Pumping machinery--Models. (LC)

I& ABfTRAcr aintame m reverseeb N noeeey adIdenttfy by block riuwSer)

A hydraulic model was used to evaluate the hydraulic performance of the21st Street Pumping Station Suap for the Bettendorf, Iowa, Local Flood Protec-tion Plan. The proposed pumping station consisted of five individual pump baysoriented perpendicular to a box culvert that will provide inflow from two di-rections. The performance of the original design was characterized by surfaceand submerged vortices. Surface vortices were eliminated by lowering the sump

(Continued)

DO I 173 mToNoFSWovssisoOLETE Unclassified

SECUmTY CLASSIFICATION OF THIS PAGE (When Dae Entered)

UnclassifiedSECURITY CLASSIFICATION OF THIS PAGI(Ulmm Datea SEu*o

20. ABSTRACT (Continued).

-floor elevation which increased submergence on the pump. Submerged vorticeswere no longer observed when surface roughness was added to the sump floorsand walls. The forebay in the original design was eliminated which providedfor considerable economic savings. The design developed as a result of themodel investigation operated satisfactorily at different sump water-surfaceelevations and with various combinations of pumps operating.,

Unclassified

59CURITY CLASIICATION OF THIS PA8EWhmi Date Efftmer)

t.F

IPREFACEThe model investigation of the 21st Street Pumping Station reported

herein was authorized by the Office, Chief of Engineers (OCE), U. S. Army, in

September 1981, at the request of the U. S. Army Engineer District, Rock

Island (NCR).

This investigation was conducted during the period October 1981 to

*August 1982, in the Hydraulics Laboratory of the U. S. Army Engineer Waterways~Experiment Station (WES), under the direction of Messrs. H. B. Simons, Chief

of the Hydraulics Laboratory, J. L. Grace, Jr., Chief of the Hydraulic Struc-

tures Division, and under the general supervision of N. R. Oswalt, Chief of

the Spillways and Channels Branch. Project engineers for the model study were

Messrs. R. R. Copeland and S. T Maynord, assisted by E. L. Jefferson.

Mr. B. F. Stanfield is acknowleged for his work in constructing the model.

This report was prepared by Mr. Copeland.

During the course of the study, Messrs. Sam Poak, Don Logsdon, S. K.

Nanda, and Rex Beach of NCR, and John S. Robertson of OCE visited WES to dis-

cuss the program of model tests, observe the model in operation, and correlate

test results with concurrent design work.

Commander and Director of WES during the course of this investigation

and the preparation and publication of this report was COL Tilford C. Creel,

CE. Technical Director was Mr. F. R. Brown.

+~~~~~~ . V " ": ; [ . . .

i .,. '

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II

COPY

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Page

PREFACE . . . . . . . . . . . . . . . . . . . . .1

CONVERSION FACTORS, U. S. CUSTOMARY TO METRIC (SI) UNITS OFMEASUREMENT .. ... .......... ......... ........ 3

PART I: INTRODUCTION. .. ....... ......... ........ 5

The Prototype. .. .*.*.*.*.'.'.*.*.*.*...*.*.*.................5Purpose of the Model Study. .... ......... ........ 6

PART II: THE MODEL .. ....... .......... ......... 8

Description .. ... .......... ......... ..... 8Interpretation of Model Results. .. ....... .......... 8

PART III: TEST RESULTS .. .... ......... ............ 15

Method of Operation .. ... .......... .......... 15Original Sump Design .. ....... .......... ..... 15Modifications to Type I Design Swmp .. ... ............. 17Type 2 Design Sump. .... ......... ............ 26Type 3 Design Swmp. .... ......... ............ 31

PART IV: CONCLUSIONS. .... ......... ............. 35

REFERENCES .. ........ ......... ......... .... 37

TABLES 1-31

PLATES 1-6

2

CONVERSION FACTORS, U. S. CUSTOMARY TO METRIC (SI)UNITS OF MEASUREMENT

U. S. customary units of measurement used in this report can be converted to

metric (SI) units as follows:

Multiply By To Obtain

acres 0.4047 hectares

cubic feet per second 0.02831685 cubic metres per second

Fahrenheit degrees Celsius or Kelvins

feet 0.3048 metres

feet of water 0.03048 kilograms per square centimetre

feet per second 0.3048 metres per second

gallons per minute 3.785412 cubic decimetres per minute

inches 25.4 millimetres

miles (U. S. statute) 1.609344 kilometres

* To obtain Celsius (C) temperature readings from Fahrenheit (F) readings,

use the following formula: C = (5/9)(F - 32). To obtain Kelvin (K) read-ings, use: K = (5/9)(F - 32) + 273.15.

3

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21st STREET PUMPING STATION, BETTENDORF, IOWA

Hydraulic Model Investigation

PART I: INTRODUCTION

The Prototype

1. The city of Bettendorf, Iowa, is located on the Mississippi River

approximately 3 miles* upstream from Lock and Dam 15. The city of Davenport,

Iowa, borders Bettendorf on the west (downstream) and the cities of Rock

Island and Moline are located across the river in Illinois. These cities are

regionally known as the Quad Cities and are important industrial and commercial

centers for a large and prosperous agricultural area. Bettendorf's location

is shown on the vicinity map in Figure 1.

2. Bettendorf is protected from floods on the Mississippi River by

levees, but the city is subject to flooding from local interior runoff that

collects behind the river levee. The flood problem area consists of about

330 acres of extensively developed industrial, conmercial, and residential

property traversed by an important railroad and highway. The city's main

business district is located in the floodplain. Due to relatively high water

levels in Pool 15, which is adjacent to the city, gravity drainage into the

Mississippi River is usually impractical. Currently, local drainage in the

cities of Bettendorf and Davenport is diverted to the government sewer, which

parallels the levee and discharges into the river below Lock and Dam 15. The

sewer is inadequate to handle the runoff from significant local rainfalls.

3. The local flood protection plan for Bettendorf consists of a series

of earth levees, floodwalls, gated closure structures, drainage structures,

pumping stations, and channel improvements as shown in Figure 1. The

21st Street Pumping Station is one of two pumping stations proposed in the

plan and will be located on the existing government sewer. The plan calls for

closing the government sewer at the Bettendorf-Davenport city boundary when

the sewer reaches capacity. This will relieve pressure on the drainage

A table of factors for converting U. S. customary units of measurements to

metric (SI) units is presented on page 3.

5

structure through the city of Davenport by eliminating rainfall runoff from

Bettendorf. The Bettendorf runoff collected in the sewer would be discharged

into the Mississippi River through the 21st Street Pumping Station.

4. The 21st Street Pumping Station will have five 36-in. pumps with a

combined pumping capacity of 150,000 gpm. The pumps, which will discharge

directly into the Mississippi River through 36-in.-diam discharge lines

equipped with flap gates, will be located in individual pump bays. Sidewalls

will have a 1:4 convergence such that there will be a 0.75-in. clearance be-

tween the walls and the 60-in.-diam suction bell. The floor clearance will be

2.5 ft. The original design sump provided a minimum submergence of 2.4 ft on

the suction bell. The pump bays will be located perpendicular to the govern-

ment sewer, which is 7.5 ft high and 5.5 ft wide at the site. The station

will draw flow from both directions of the sewer in approximately equal quanti-

ties. Operating water-surface elevations will vary between 558.5* and 564.5.

Sump dimensions and flow rates are often related to the suction bell diameter

for comparison purposes. In these terms, characteristics of the original de-

sign of the 21st Street Pumping Station are:

Length (to pump center line) 3.7D

Width 1.8D

Floor clearance 0.50D

Wall clearance 0.012D

Minimum suction bell submergence 0.48D

Q/D5 / 2 * 1.20

Purpose of the Model Study

5. Pump performance can be adversely affected by unfavorable flow con-

ditions at the pump intake caused by low submergence of the pump impeller and

by unequal flow distribution entering the sump. Air entrainment, vortex ac-

tion, prerotation of flow (swirl) into the pump column, and pressure fluctua-

tions can occur and may result in cavitation, vibration, and uneven stresses

on the pump. Although, generalized studies are being conducted by the U. S.

* All elevations (el) cited herein are in feet referenced to the NationalGeodetic Vertical Datum (NGVD).Flow parameter, where Q = discharge in cubic feet per second and D suc-tion bell diameter in feet.

6

Army Engineer Waterways Experiment Station (WES) as part of the Electrical and

Mechanical R&D Program to improve pumping station inflow-discharge hydraulics

and eliminate or reduce these adverse effects, these studies have not yet pro-

duced sufficient information to develop design criteria needed for pump sumps

with conduit approaches.

6. The 21st Street Pumping Station has unique features that are not

adequately covered by existing design criteria. Flow approaches the station

perpendicular to the pump bays, a condition that could cause adverse circula-

tion in the sump and poor flow distribution in the pump bays. Suction bell

submergence is considerably lower than most general criteria recommend. The

location of the converging sidewalls is such that the suction bell clearance

is much less than that generally recommended. The model study was con' ei

to provide an assessment of the sump's hydraulic performance for a ran -f

anticipated operating conditions. The investigation was also intendee de-

velop practical modifications that would improve performance of the pL eL

station and/or reduce construction costs.

7 -*

PART II: THE MODEL

Description

7. The model of the 21st Street Pumping Station was constructed to an

undistorted linear scale ratio of 1:8 and of transparent plastic to allow ob-

servation of submerged flow conditions. A scale was attached to the backwall

of the type I original design sump and to the backwall of the government sewer

in subsequent design sumps to indicate water-surface elevations. The govern-

ment sewer was simulated for lengths of 80 ft in both directions from the sump

and was also constructed of transparent plastic. The model as originally de-

signed is shown in Figure 2.

8. Flow through the model was recirculated by centrifugal pumps. Each

pump column had its own separate pump to permit simulation of various flow

rates and selective operation of the pumps. Water levels were adjusted in the

model by adding or draining water. Flow from each pump was measured by paddle-

wheel flowmeters and displayed electronically. The flow rates were controlled

by automatic valves. Flow from each of the five pumps fed into a manifold

where it could flow to either of two headbays located at upstream ends of the

model. Flow to the headbays was measured by paddle-wheel flow6.eters, con-

trolled by automatic valves, and displayed electronically. Flow rates through

the pumps and into the headbays were controlled and monitored at a console

located adjacent to the model.

9. Various instruments and methods were used to measure the factors

that affect pump sump performance. Confetti and dye were used to observe and

photograph flow patterns in the sump. Velocities approaching the pump column

were measured with a paddle-wheel velocity meter. Visual observations were

used to determine vortex activity. Prerotation of flow (swirl) into the pump

column was measured by counting revolutions of a freewheeling vortimeter with

four zero-pitched blades mounted in the pump column (Figure 3). Electronic

pressure transducers were placed beneath the pump suction bells to measure

instantaneous pressure fluctuations (Figure 3); a time-history was recorded onstrip charts.

Interpretation of Model Results

10. The principle of dynamic similarity, which requires that ratios of

8

14)

4)

C14

ON.V

V|

VTRANSDUCER

%E

¥x

- -4

PRESSURE TRANSDUCERDIA. 2" (PROTOTYPE)

PUMP INTAKE

PRESSURE TRANSDUCER

PLAN VIEW ELEVATION

Figure 3. Flow condition monitors used in model investigation

forces be the same in model and prototype, is the basis for the design of

models and the interpretation of results. Models involving a free surface are

scaled to the prototype using the Froudian criteria because the flow phenomena

are determined primarily by gravitational and inertial forces. The general

relations expressed in terms of model scale or length ratio are as follows:

ScaleDimension Ratio Relation

Length L = L 1:8r

Velocity V = LI 2 1:2.83r

Time T = L1/2 1:2.83r

Discharge Qr = L 5 /2 1:181

Pressure P = L 1:8r

Values for length, velocity, time, discharge, and pressure fluctuation can be

transferred quantitatively from model to prototype by means of the scale rela-

tions above. Unless otherwise noted, all results reported herein will be

given in prototype units.

11. Viscous effects can also influence flow patterns and formation of

vortices. Daggett and Keulegan (1974) conducted vortex similarity tests using

drain vortices in cylindrical tanks and defined a limiting Reynolds number

R=Av

where

R = Reynolds number

Q = discharge

A = orifice radius

v = kinematic viscosity

which must be greater than 5(10)4 to yield viscous effects negligible. The

Reynolds number by this definition for the 21st Street model varies between

8.4 x 104 and 1.6 x 105 depending on temperature, thus indicating minimal vis-

cous effects in the model. The work of Anwar and Amphlett (1980) with in-

verted pipe intakes shows that surface tension and viscosity effects become

negligible when the radial Reynolds number

11

I1

- , .. " ,-

V

Rr =

(where h equals submergence above bottom of intake pipe) is greater than43(10) . Using this definition for Reynolds number, it was determined the

21st Street model (Rr = 1.0 X 104 - 1.7 x 10 5) was free of viscous and surface

tension effects at water-surface elevations below 563.0 and where the tempera-

ture was greater than 650 F. Hecker (1981) reviewed available model-prototype

comparisons of free surface vortices and found 16 projects where model flows

were scaled by the Froudian criteria. Fourteen of these projects had model

and prototype vortices essentially equal and five of the projects had vortices

weaker in the model than in the prototype. Hecker concludes from the model-

prototype comparisons that designs that were developed from Froude-scale model

tests to be vortex-free were indeed vortex-free in the prototype, and those

having weak vortices in the model had weak vortices in the prototype. No

cases were found where a weak model vortex corresponded to a strong prototype

vortex resulting in operating problems.

12. There are currently insufficient data to establish definite accept-

able limits of uneven flow distribution, vortex activity, and pressure fluctua-

tion; however, general guidelines have been considered and are used at WES to

develop satisfactory sump designs. The flow distribution approaching the pump

column should be fairly uniform because uneven distributions usually cause ex-

cessive levels of the other indicators. In this model investigation, veloci-

ties were measured at a depth halfway between the floor and the bottom of the

suction bell. Every attempt is made to eliminate surface and submerged vor-

tices. The types of vortex formations and the stages of surface vortex de-

velopment observed in this study are shown and defined in Figure 4. The

severity of swirl is expressed as a dimensionalized rotational flow indicator,

R. The rotational flow indicator is the ratio of the tangential velocity at1

the tip of the vortimeter blade to the average axial velocity in the pump col-

umn, and is equal to the tangent of the indicated swirl angle as used by many

investigators. The rotational flow indicator is computed using the following

formula:

Ri Va

12!1

WATERLEVEL

SURFACE VORTEX

'WALL VORTEX

FLOOR VORTEXSECTION A-A

VORTEX FORMATIONS

SURFACE DIMPLE WITH NO AIR ENTRAINMENT

A

S SURFACE DEPRESSION BECOMES DEEPER

S A TAIL DEVELOPS WHICH MAY HAVE A ROTATINGWATER CORE BENEATH IT, DETECTABLE BY DYE

C

S AIR ENTRAINMENT OCCURS IN THE FORM OF AIRBUBBLES DRAWN INTO THE SUCTION BELL

000

D

FULLY DEVELOPED VORTEX WITH OPEN AIRCORE INTO THE SUCTION BELL

E

STAGES OF SURFACEVORTEX DEVELOPMENT

Figure 4. Vortex formations

,,f t3 f

where

u = nnt/60

n = angular velocity of vortimeter, rpm

2 = length of vortimeter blade (pump column diameter), ft

V a= average axial velocity in pump column, fps

The rotational flow indicator has the same value in model and prototype and

may be used to compare performance of sumps with different sizes and dis-

charges. To ensure satisfactory sump performance, WES recommends that the

rotational flow indicator be less than 0.09, which is equivalent to an indi-

cated swirl angle of 5 deg. Maximum pressure fluctuations, measured as feet

of water, represent turbulence and/or the passage of low-pressure cores across

the pressure transducer located directly beneath the center line of the pump.

In the model investigation, pressures were recorded for a minimum of 7 min

(prototype). WES considers recorded pressure fluctuations greater than 4 ft

of water as excessive. Using these guidelines, it is believed that acceptable

pump sump design can be accomplished through the model investigation procedure.

14

: , : , .. .. . . . _ .. . I I I I4

PART III: TEST RESULTS

Method of Operation

13. The proposed pumping station consists of five pumps designed to

operate between water-surface elevations 558.5 and 564.5. The range of sump

water-surface elevations at which various numbers of pumps would be operating

is shown below:

Number of Sump Water-Surface ElevationPumps Operating Minimum Maximum

1 558.5 560.75

2 559.5 562.0

3 560.75 562.5

4 561.5 563.0

5 562.0 564.5

Due to the large number of possible combinations of pumps operating at various

sump water-surface elevations, a few operating conditions were chosen to com-

pare various modifications. These were generally pump 5 operating between

el 558.5 and 561.5, and all five pumps operating between el 562.0 and 564.5.

Tests were usually conducted at 1-ft intervals within this range. The original

and final designs were tested with several additional operating conditions.

The tests were conducted with a discharge of 67 cfs per pump. Flow entered

the sump in equal quantities from both directions of the government sewer.

Original Sump Design

14. Flow from the government sewer entered the forebay of the type 1

(original) design sump (Figure 5) through three 10-ft wide by 5-ft-high gate

openings. Flow through the center opening was deflected by the two type 1

(original) design baffles. The five pump bays were 21.08 ft long and 9 ft

wide and were oriented perpendicular to the government sewer. The sidewalls

converged toward the 5-ft-diam pump suction bell at an angle of 14 deg such4|

that the clearance between the suction bell and the walls was 0.75 in.

(0.012D). The backwall clearance was also 0.75 in.

15. The hydraulic performance of the type 1 design sump was found to be

15

tI

-. 57.0 FT35.46FT

5FT 5.0FT

5.0 FT A' k

BAFFLE LCONVERING SDEWAL

Figure ~ ~ 1. F.Tp Idsgnsa

3.5 F R16

p *1 - .

w

unsatisfactory. Surface vortices were observed at low sump water-surface ele-

vations. Submerged vortices were observed off the floor and sidewalls whenmore than one pump was operating. Eddies occurred in the pump bays becausethe flow did not enter uniformly. Swirl and pressure fluctuations were within

acceptable limits for most of the operating conditions tested. The generally

acceptable level of swirl is apparently attributed to the closeness of the con-

verging sidewalls to the suction bell. The occurrence of submerged vortices

may also be partially attributed to the sidewall's location. Test results

with various combinations of pumps operating and a range of sump water-surface

elevations are shown in Tables 1-4. Measured velocities and flow patterns in

the pump bays for three operating conditions are shown in Plate 1.

Modifications to Type 1 Design Sump

16. Baffles were provided in the type 1 design sump to improve flow

distribution entering the individual pump bays. The type 1 (original) design

baffles were removed and the type 2 design baffles, consisting of two rows of

vertical baffles, were placed in the sump as shown in Figure 6. When all five

pumps were operating, flow distribution in the individual sump bays was im-

proved and swirl was reduced, but submerged vortices continued to occur. For

test conditions with one or three pumps operating, flow distributions in the

* 4. . . . . . .4. d,

A-A -2'4

."2.625'

nooo 0 oo1j3 3 2.625'2.625'

. .. .. { SECTION A-A

Figure 6. Type 2 design baffles

17

_ _ _ _ _

-

individual pump bays were not improved. Swirl increased and in some cases the

severity of surface vortices increased. Submerged vortices continued to occur.

Test results for one, three, and five pumps operating are shown in Table 5;

measured velocities and flow patterns are shown in Plate 2.

17. Tests were conducted to determine if rounded pier noses in combina-

tion with the type 2 design baffles would improve the flow distribution and

sump performance for single pump operations. Two pier noses were tested (Fig-

ure 7). The type 2 design pier nose was semicircular with a diameter equal to

the sump divider wall thickness. The type 3 design pier nose had a diameter

twice the sump divider wall thickness. The pier noses were tested with one

pump operating in pump bay 5; results are shown in Tables 6 and 7. Swirl was

slightly improved with the type 3 design pier nose, but surface and submerged

vortices continued to occur. The rounded pier noses did not significantly im-

prove hydraulic conditions in the sump.

18. An attempt was made with the type 3 design baffles to direct more

flow down the center of the pump bays by moving the baffle rows closer to the

pump bays and interchanging the baffles with the baffle spacings as shown in

R-=.75'DDE jl* 5 j

TYPE 2 DESIGN TYPE 3 DESIGN

Figure 7. Type 2 and 3 design pier noses with type 2 design baffles

18

* . ~:

Figure 8. This design was tested with pump 5 operating alone and with five

pumps operating; results are shown in Table 8 and Plate 3. This design pro-

vided no improvement over the type 1 (original) design sump when one pump was

operating and was less effective than the type 2 design baffles when all five

pumps were operating.

19. Guide vanes (or divider walls) were tested to determine if flow

distribution could be improved. The type 3 design baffles were removed and

the type 1 design guide vane (Figure 9) was placed in pump bay 5 and tested

with one and five pumps operating. Swirl was significantly lower with the

guide vane for single pump operations, but surface vortices were just as

severe as without the guide vane. In addition, submerged vortices were ob-

served with the guide vanes that were not observed with the original design.

Insufficient data were taken to make reliable comparisons for five pumps

operating, but the type 1 design guide vane had excessive swirl and surface

and submerged vortices with the sump water surface at el 562.0. Results of

these tests are presented in Table 9 and Plate 4.

20. Converging sidewalls similar to those in the 21st Street Pumping

Station were concurrently tested at WES as part of the generalized pumping

station research program. These tests were made in a straight approach chan-

nel, so that the flow distribution approaching the pump was uniform. The

21st Street Pumping Station's type 1 (original) design sidewalls had a minimum

2.625"'

A-A

Figure 8. Type 3 design baffles

19

- '

+ 9.75'

8.80' 0.95'

SECTION A-A

A

Figure 9. Type I design guide vane

clearance of O.012D, where D is the suction bell diameter. Sidewall clear-

ances of 0.05D, 0.08D, and 0.17D were tested in the generalized model. Tests

conducted at appropriately scaled flow rates and submergences in the gener-

alized model demonstrated that submerged vortices would occur when the side-

wall clearance was 0.05D. When the sidewall clearance was 0.08D no submerged

vortices were observed at flow rates comparable to those expected at the

21st Street Pumping Station. The tests in the generalized model demonstrated

that even with uniform flow distribution, submerged vortices would occur in

the 21st Street Pumping Station sump with the type 1 (original) design converg-

ing sidewalls with only a clearance of 0.012D. It was concluded that the side-

wall clearance should be increased.

21. The sidewall clearance was increased to 0.10D (0.5 ft) with the

type 2 design sidewalls (Figure 10). This design was tested in pump bay 5 in

combination with the type I design guide vane for one and five pumps operating;

results are shown in Table 10. The type 2 design sidewalls were not success-

ful in eliminating submerged vortices. This failure is attributed to the con-

tinued poor flow distribution in the pump bay. Swirl increased significantly,

well beyond recommended limits, but surface vortex development was essentially

the same. Pressure fluctuations also became excessive with five pumps operat-

ing. Although hydraulic performance deteriorated with the type 2 design

20

f .....

2. 10' 2.40'

I --7 .----V 0.50'

.g

Figure 10. Type 2 design sidewalls

sidewalls, it was felt that a minimum wall clearance of 0.10D would be neces-sary for eventual elimination of submerged vortices. The type 2 design side-walls were therefore retained and further attempts to improve flow distribu-

tion were made.

22. The type I design guide vane was removed from pump bay 5 and adouble guide vane (Figure 11) was installed. This type 2 design guide vane

was tested in combination with the type 2 design sidewalls for one and fivepumps operating (Table 11 and Plate 4). The type 2 design guide vane did not

provide any significant improvement over the type I design guide vane. Oneguide wall would be easier to construct than two, so the type I design guide

vane was put back into the model.

23. Horizontal vortex suppressor beams were added to pump bay 5 incombination with the type I design guide vane and the type 2 design sidewalls

in an attempt to reduce surface vortices. Location and sizing of the beams

(Figure 12) were based on a design from the generalized pumping station re-

search program at WES. The type 1 design vortex beams were tested for one and

~21

8.00

6.83' 1. 17'

fA~f liii SECTION A-A

iliilii

3.0'+.00' 3.00"

Figure 11. Type 2 design guide vane

15.00'

+ 8. 75'

5.50',

EL 564.5

EL 553.6C1

-- CL I 59 -

EL 553.6,Z

CON VERGING]SIDEWALLS

(TYPE 2)

9.00" SIDE VIEW

PLAN VIEW

Figure 12. Type 1 design vortex suppressor beams with type I design guidevane and type 2 design sidewalls

3ti

five pumps operating; results are shown in Table 12. The addition of the

vortex beams to the type 1 design guide vane and the type 2 design sidewalls

reduced surface vortices significantly; stage C vortices were only observed at

the minimum sump elevation of 558.5. Swirl was also significantly reduced,

although it remained excessive for five pumps operating. Pressure fluctua-

tions were reduced but were still excessive when five pumps were operating

with a sump water surface'at el 564.5. Submerged vortices continued to occur

for all conditions tested.

24. The type 2 design vortex suppressor beams (Figure 13) were tested

in pump bay 5 in combination with the type I design guide vane and the type 2

design sidewalls for one and five pumps operating. This design was based on a

design developed in the Pointe Coupee Pumping Station model study conducted at

WES (Copeland 1983). Results of these tests are shown in Table 13 and Plate 4.

The type 2 design vortex suppressor beams eliminated surface vortices when

five pumps were operating, but stage C vortices continued to occur at the mini-

mum sump elevation of 558.5. Swirl was reduced slightly. Submerged vortices

remained a problem. The type 2 design vortex beams were deemed a slight

6.50'

5.50'

EL 564.5

! , EL 553.6

) [ CONVERGINGSIDEWA L L S(TYPE 2

~SIDE VIEW

9.00'/

PLAN ViEW

Figure 13. Type 2 design vortex suppressor beams with type 1 design guidevane and type 2 design sidewalls

23

a9'-..

improvement over the type 1 design vortex beams.

25. The effect of lengthening the pump bay by extending the divider

wall was tested in pump bay 5 for one and five pumps operating (Table 14).

The type 1 design wall extension (Figure 14) was tested in combination with

the type 1 design guide vane, the type 2 design vortex suppressor beams, and

the type 2 design sidewalls. The divider wall did not provide for any sig-

nificant improvement in sump performance.

26. A sump design without converging sidewalls was developed at WES as

part of the pumping station research program for sumps with uniform flow dis-

tribution approaching the pump. This design (type 51 pump bay), shown in Fig-

ure 15, was tested in pump bay 1 for single pump operations and with five

pumps operating (Table 15). The type 51 design pump bay did not perform

satisfactorily with the poor flow distribution that occurs in the 21st Street

Pumping Station.

27. The type 4 design baffle was located in front of one of the two

side gate openings (Figure 16) and was intended to deflect flow away from the

side pump bay in order to improve overall flow distribution in the sump. The

effect of this design on the type 51 design pump bay is shown by comparing

Tables 15 and 16. When all five pumps were operating at a water-surface ele-

vation of 562.0, the baffles were successful in significantly improving flow

distribution into the side bays. However, as the water level increased to

el 564.5 the baffles became less and less effective. Apparently,

6.22'

DIVIDERWALLEXTENSION

Figure 14. Type 1 divider wall extension

24

[!b

15.00' 3.75'

8.75'5.00'+

EL 564.5 '

Pl EL 56.251.25'

EL_5_ZEL 553.6

SIDE VIEW

PLAN VIEW

Figure 15. Type 51 design pump bay

TYPE : '4 .'.... 4 :--~.... ** 4. BAFL

TYPEE 4 BAFFLES

SECTION A-A

Figure 16. Type 4 design baffle

deflector-type baffles would require different configurations for each operat-

ing condition, making their use impractical.

28. The tests conducted on the type 1 (original) design sump with vari-

ous modifications were unable to develop a sump design with satisfactory hy-

draulic performance. Features that provided for significant improvement in the

sump's performance were the type 1 design guide vane and the type 2 design vor-

tex suppressor beams. Results from the generalized pumping station research

program at WES indicated that type 2 design sidewalls were also desirable.

After viewing the model in operation and discussi-g test results of the type 1

design sump, engineers from the U. S. Army Engineer District, Rock Island, de-

cided to discontinue attempts to improve this design so that testing could

proceed on a revised sump design that would be more economical to construct.

Type 2 Design Sump

29. The type 2 design sump, designed by the Rock Island District, would

be more economical to construct and was similar to an existing prototype pump-

ing station at Marshalltown, Iowa, which has operated satisfactorily since

construction. The type 2 design sump had no forebay so that each pump bay was

connected directly to the government sewer and had individual gates (Fig-

ure 17). The type 2 design sump had the type I (original) design sidewalls

with a suction bell clearance of 0.012D. The type 1 (original) design gates

were 5 ft high by 5 ft wide and were located 13.35 ft upstream from the pump

center line. The total length of the individual pump bays was 22.65 ft. Re-

sults of testing this design are shown in Table 17; measured velocities and

flow patterns are shown in Plate 5.

30. For single pump operations, the type 1 design sump performed

slightly better than the type 2 design sump. Surface vortices occurred because

of the low sump water-surface elevations. Submerged vortices occurred with the

type 2 design sump but were not observed in the type 1 design sump. Swirl was

within recommended limits for the type 1 design sump but exceeded acceptable

values during one test with the type 2 design sump. Pressure fluctuations

were within acceptable limits for both designs. The similarity in performance

of the two designs for single pump operations is attributed to the relatively

low velocities in the government sewer so that adverse eddies are not set up

when flow enters the pump bay.

26

I.I'

• I .-'1 E . . . E__4

+ 7

WALL CLEARANCE 0.063 FT

FLOOR CLEARANCE 2.5 FT

SUCTION BELL DIAMETER 5 FT

u P . .Type 2 design sump

31. The hydraulic performance of the type 2 dpoign sump was much worse

than the type I design sump for three and five pumps operating. Stage C vor-

tices occurred in the type 2 design sump at water-surface elevations where

only surface dimples had occurred in the type I design sump. Where swirl had

been within acceptable limits with the type I design sump, swirl was outside

these limits in every test with the type 2 design sump. With the type 2 de-

sign sump, the maximum rotational flow indicator with three pumps operating

was 0.27 (three times the recommended limit); and with five pumps operating,

the maximum rotational flow indicator was 0.66 (more than seven times the

recommended limit). Pressure fluctuations were also much higher with the

type 2 design sump exceeding recommended limits in at least one pump bay in

every test. The poor performance of the type 2 design sump with multiple pump

operations is attributed to the poor flow distribution entering the pump bays

due to high velocities and turbulence in the government sewer." 32. Submerged sills were tested in the type 2 design sump in an attempt

~to straighten and equalize flow into the pump bays. Two sills were tested;

.27

the type 1 design sill was 2.5 ft high and the type 2 design sill was 1.67 ft

high. The type 1 design sill was placed in all five bays and tested for one

and five pumps operating (Table 18). The type 2 design sill was placed only

in pump bay 1 and tested for one and five pumps operating (Table 19). Sill

location is shown in Figure 18. The type I design sill with five pumps operat-

ing provided for some improvement in flow distribution and swirl at high sump

water-surface elevations. However, at the lower sump water-surface elevations

and single pump operations, turbulence, surface vortex activity, and swirl in-

creased. Decreasing the height of the sill to 1.67 ft (type 2 design sill)

resulted in no significant difference in hydraulic performance.

33. Baffles were placed between the submerged sills and the slide gates

(Figure 19) in an attempt to improve flow distribution in the pump bays. The

type 5 design baffles increased turbulence and vortimeter revolutions were

rapid, indicating excessive swirl in the pump column. Based on these

Q0 0 1.29 FT1.29 FT

0.-0- .-0 1.29 FT

0.5 FTF BAFFLES 8.5 FT HIGH

FLOW FL OWZLI_ \TYPE 1 DESIGN SILL

TYPE 1 SILL2.5 FT HIGH

TYPE 2 SILL 1 FT 3-1/2 IN. SQUARE1.67 FT HIGH 1 FT 3-1/2 IN. SPACINGS

Figure 18. Type I Figure 19. Type 5 designand 2 design sills baffles

28

'4"V

7

observations, this design was deemed inadequate and testing was discontinued.

34. An attempt was made to correct adverse flow patterns by placing

baffles in the channel upstream from the pump bays. The type 6 design baffles

(Figure 20) caused a deterioration of hydraulic performance for single-pump

operations and a slight improvement with five pumps operating (Table 20).

----- ------

DI1.20 E EJ 0 El EPr12. 624' l i

2.624'

Figure 20. Type 6 design baffles

35. In order to provide a greater distance for the asymmetric flow dis-

tribution to straighten, the gates were moved to the front of the pump bays.

The type 2 design gate (Figure 21) was tested for single and five pumps operat-

ing (Table 21). This design caused a slight deterioration in hydraulic per-

formance with single pump operations, but resulted in a considerable improve-

ment in swirl with five pumps operating. However, swirl was still above ac-

ceptable limits.

36. An attempt was made to eliminate submerged vortices by increasing

the wall and floor roughness in the vicinity of the pump. The type 3 design

sidewalls had vertical grooves I in. deep, 1 in. wide, with 1-in. separations.

The vertical grooves were also placed on the backwall. Grooves with the same

dimensions were placed on the sump floor perpendicular to the flow direction.

29

i F L I:t : : ": : /" "; -> '

ori

The grooved floor and walls extended 6 ft up-

stream from the backwall (Figure 22). The

type 3 design sidewalls were tested in pump

bay 5 for single and five pumps operating with

L the type 2 design gates (Table 22). There were

L Oi no observed submerged vortices; however, swirl-

ing low-pressure zones were still present and

GATE 5.OFT became visible when accumulated air bubbles

1.TFT HIGH were periodically pulled off the walls and

floor. The additional boundary turbulence cre-FFLOW ated by the increased surface roughness is ap-

_ _ _parently beneficial in breaking up submerged

vortices.Figure 21. Type 2 37. Modifications to the type 2 design

design gatessump were not successful in providing anything

close to satisfactory sump performance. The type 3 design sidewalls were

found to be beneficial in eliminating submerged vortices and the type 2 design

gate located at the front of the pump bay provided for some improvement in

.t c

Figure 22. Type 3 design sidewalls

30

hydraulic performance. However, surface vortices still occurred at low sump

water-surface elevations and both swirl and pressure fluctuations were exces-

sive for five pumps operating.

Type 3 Design Sump

38. The sump floor was lowered 2 ft to el 551.6 in the type 3 design

sump. The type 3 design sidewalls and the type 2 design gates were included

in the type 3 design sump (Figure 23). The type 3 design sump was tested with

one, three, and five pumps operating. Performance in pump bay 5 is shown in

Table 23. The type 3 design sump was free from surface and submerged vortices.

Increasing minimum bell submergence to 0.88D eliminated the surface vortices,

and the wall and floor roughness grooves prevented submerged vortices from

forming; however, swirl remained extremely high.

39. Trashracks, 8 in. deep, were added to the front of each pump bay to

straighten flow and prevent trash from entering the sump. The prototype

equivalents of the bars in the model were 0.40 in. wide with 3.17-in. spacings,

simulating the obstructed area of a trashrack with bars 0.38 in. wide and

3.0-in. spacings (commonly used by the Rock Island District). The trashracks

were effective in reducing swirl (Table 24).

40. The gates were moved from the top of the vertical drop closer to

the pump. This modification made the elevation of the top of the gate opening

2 ft lower so that flow was forced closer to the pump bay floor. This helped

to straighten flow and decrease swirl. Tests were conducted in pump bay 5 to

optimize gate size and location. Sixteen different combinations of gate sizes

and locations were tested. Surface and submerged vortices were not observed

with any of the gate designs. Swirl was still excessive for many of the gate

configurations as shown in Table 25. Gates 8 ft wide and either 3.75, 4.0, or

4.5 ft high (type 10-18 design gates) provided the lowest level of swirl. For

these gate sizes, swirl was highest when the gate was located 3.0 ft down-

stream from the vertical drop, and generally decreased as the gate was moved

upstream. Maximum pressure fluctuations for the type 10-18 design gates

(Table 26) are generally within recommended limits, with a tendency to in-

crease as the gate moved closer to the vertical drop. A gate location 2.25 ft

downstream from the vertical drop was chosen to achieve the most favorable

swirl and pressure fluctuation conditions. The 4.0- and 3.75-ft-high gates

31

FLOOR EL 553.6 91OFT~7 It

VER ICA L DROP

WALL CLEARANCE 0.75 IN.FLOOR CLEARANCE 2.5 FT

SUCTION BELL DIAMETER 5 FT

4.s

CONVERGING I- GOEN- .:o

SIDEWALLSER

EL 554.1L...E536

Figure 23. Type 3 design sump

(type 15 and 18 design gates, respectively) had the lowest level of swirl at

this location, with the 4.5-ft-high gate (type 11 design gate) slightly higher.

Recommended levels of swirl were exceeded in at least one test of each gate

design. Hydraulic performance was judged to be essentially equal for the

type 11, 15, and 18 design gates. For structural reasons, engineers from the

Rock Island District preferred the 4.5-ft-high gate (type 11 design gate)

which was thereby chosen for more extensive testing.

41. Several combinations of pumps operating and sump water-surface ele-

vations were tested with the type 3 design sump equipped with trashracks and

the type 11 design gates (Figure 24). Results of these tests are shown in

Tables 27-31. Velocity measurements are shown in Plate 6. There were no sur-

face or submerged vortices observed in any of these tests. In several tests,

swirl was greater than that normally recommended by WES; that is, the rota-

tional flow indicator was greater than 0.09 which is equivalent to having an

indicated swirl angle greater than 5 deg. Maximum pressure fluctuations were

within the recommended limit of 4 ft of water in all tests. The type 3 design

sump with trashracks and the type 11 design gates Vas deemed to have adequate

hydraulic performance by engineers from the Rock Island District and was the

final design adopted for construction.

33

TRASHRACKS FLOOR EL 553.6 90 Fr

VERTICAL DROP

SLIDE GATES FLOOR

FLOOR ROUGHNESSELEMENTS

I-IN.-DEEP GROOVESI IN. WIDE k

I-IN. SEPARATION

WALL CLEARANCE 0.75 IN.FLOOR CLEARANCE 2.5 FT

SUCTION BELL DIAMETER 5 FT

TRASHRACK35 BARS 0.40 IN. THICK

3.17-IN. SPACING

6.0 FFT

220.65 FT

o OPENING

V VERGING SEWER

ROUGHNESS.ELEMENT4 IN. WID

"EN SE. P AR5ATI

~17.58 FT

( "..

19.83 FT

22.65 FT

VERTICAL SIEALAND BACKWALL

UGHNESS ELEMENTSI-IN.-DEEP GROOVESI IN. WIDE?-IN. SEPARATION

Figure 24. Type 3 design sump with trashracks and type 11 design gates

.. ,.. : .-ps

, j .

• I i I - I - i t

PART IV: CONCLUSIONS

42. Satisfactory hydraulic performance of a pump sump with flow into

the pump bays perpendicular to the approach flow can be achieved with appro-

priate appurtenances. Converging sidewalls located such that the suction bell

clearance was 0.012D reduced swirl in the pump column. Trashracks with 8-in.-

deep bars were effective in reducing swirl in the 9-ft-wide pump bay. Sub-

merged vortices may be eliminated by adding roughness to the floor and walls.

In this model study, vertical grooves I in. deep, 1 in. wide, with I-in. sepa-

rations were used on the sidewalls and backwalls; grooves with the same dimen-

sions were located perpendicular to the flow on the floor. The additional

boundary turbulence created by the increased surface roughness is apparently

beneficial in breaking up submerged vortices; however, swirling low pressure

zones were still present in the model and became visible when accumulated air

bubbles were periodically pulled off the walls and floor. Surface vortices

can be eliminated in the sump bay by providing adequate suction bell sub-

mergence. In this model study (with a flow parameter of Q/D2 .5 equal to 1.2),

a minimum suction bell submergence of 0.88D eliminated surface vortices. This

level of submergence was achieved by lowering the sump floor by 2 ft. Gate

size and location are important in providing for the best possible hydraulic

performance. Gates at or near the upstream ends of the pump bays serve to

force flow toward the sump floor, helping to straighten flow and decrease

swirl. A combination of these features provided for satisfactory hydraulic

performance with the adopted (type 3) design sump for the 21st Street Pumping

Station.

43. Other features were found to improve flow conditions in the sump

but were not used in the final design. The large forebay in the type 1 design

sump was more effective in distributing flow into the pump bays than were the

type 2 and 3 design sumps. Swirl was much less severe with the large forebay.

This feature was not included in the final design for economic reasons. Vor-

tex suppressor beams were found to be effective in reducing swirl and surface

vortices by forcing flow toward the sump floor and by creating surface turbu-

lence which helps break up surface vortex activity. Vortex suppressors were

not used in the final design because the type 11 design gate served to force

the flow toward the floor, reducing swirl; and the increased submergence in

the type 3 design sump was more effective in eliminating surface vortices.

4 35

7

S "Guide vanes were found to improve flow distribution in the sump, but rela-

tively deep trashracks served the same function and were chosen for the final

design. Forebays, vortex suppressor beams, and guide vanes may provide for

improved hydraulic performance in future sump designs and may be useful in im-

proving existing sumps with poor performance.

44. Several baffle configurations, rounded pier noses, increased side-

wall clearance, a divider wall extension, and submerged sills were tested but

they provided no significant improvement in hydraulic performance. These

modifications have been shown to be successful in other pumping station sumps,

but were not effective in the 21st Street Pumping Station sump where the pump

bays were perpendicular to the approach flow.

36

Ado.

w

REFERENCES

Anwar, H. 0., and Amphlett, M. B. 1980. "Vortices at Vertically InvertedIntake," Journal of Hydraulic Research 18, No. 2.

Copeland, Ronald R. 1983 (Mar). "Pointe Coupee Pumping Station Sump andOutlet Structure, Upper Pointe Coupee Loop Area, Louisiana; Hydraulic ModelInvestigation," Technical Report HL-83-3, U. S. Army Engineer Waterways Ex-periment Station, CE, Vicksburg, Miss.

Daggett, L. L., and Keulegan, G. H. 1974 (Nov). "Similitude in Free-SurfaceVortex Formations," Journal, Hydraulics Division, American Society of CivilEngineers, No. HYII.

Hecker, G. 1981 (Oct). "Model Prototype Comparison of Free Surface Vortices,"Journal, Hydraulics Division, American Society of Civil Engineers, Vol 107,No. HYIO.

37A

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Table 27

Sump Performance, Type 3 Design Sump with Trashracks,

Type 11 Design Gates, I Pump Operating

Maximum PressureSump El Pump Surface Submerged Swirl-Rotational Fluctuationft NGVD Bay No. Vortex Vortex Flow Indicator Feet of Water

558.5 5 0 0 +0.08 2.0

559.5 5 0 0 +0.03 2.4

560.5 5 0 0 +0.05 2.2

561.5 5 0 0 +0.02 2.0

558.5 4 0 0 +0.10 0.6

559.5 4 0 0 +0.06 0.6

560.5 4 0 0 +0.05 0.4

561.5 4 0 0 +0.04 0.4

558.5 3 0 0 +0.08 0.6

559.5 3 0 0 +0.04 0.8

560.5 3 0 0 +0.02 0.8

561.5 3 0 0 +0.01 0.6

Note: + = clockwise rotation.Water temperature = 850-900 F; air temperature = 80--87* F.

Table 28

Sump Performance, Type 3 Design Sump with Trashracks,

Type 11 Design Gates, 2 Pumps Operating

Maximum PressureSump El Pump Surface Submerged Swirl-Rotational Fluctuationft NGVD Bay No. Vortex Vortex Flow Indicator Feet of Water

559.5 4 0 0 -0.08 0.85 0 0 +0.12 2.2

560.5 4 0 0 -0.08 0.45 0 0 +0.14 1.2

561.5 4 0 0 -0.02 0.45 0 0 +0.06 2.4

562.5 4 0 0 -0.04 0.45 0 0 +0.08 3.2

559.5 3 0 0 -0.06 0.45 0 0 +0.13 1.2

560.5 3 0 0 -0.04 0.45 0 0 +0.13 1.6

561.5 3 0 0 -0.04 0.45 0 0 +0.08 3.6

562.5 3 0 0 -0.04 0.45 0 0 +0.05 3.6

599.5 1 0 0 -0.15 2.05 0 0 +0.12 2.0

560.5 1 0 0 -0.12 1.25 0 0 +0.13 2.0

561.5 1 0 0 -0.13 1.25 0 0 +0.09 3.2

562.5 1 0 0 -0.12 1.25 0 0 +0.05 4.0

559.5 2 0 0 -0.09 0.44 0 0 +0.20 0.4

560.5 2 0 0 -0.05 0.44 0 0 +0.13 0.4

561.5 2 0 0 -0.06 0.44 0 0 +0.12 0.4

(Continued)

Note: + = clockwise rotation; and - = counterclockwise rotation.Water temperature 79°-103* F; air temperature 76*-96* F.

- t

Table 28 (Concluded)

Mkaximumn PressureSumnp El Pump Surface Submerged Swirl-Rotational Fluctuation

ft NGVD Bay No. Vortex Vortex Flow Indicator Feet of Water

562.5 2 0 0 -0.05 0.4400+0.11 0.4

559.5 3 0 0 -0.09 0.44 0 0 +0.20 0.4

560.5 3 0 0 -0.05 0.44 0 0 +0.13 0.4

561.5 3 0 0 -0.05 0.44 0 0 +0.10 0.4

562.5 3 0 0 -0.04 0.64 0 0 +0.10 0.4

(a

r

4 Table 29

Sump Performance, Type 3 Design Sump with Trashracks,

Type 11 Design Gates, 3 Pumps Operating

Maximum PressureSump El Pump Surface Submerged Swirl-Rotational Fluctuation

ft NGVD Bay No. Vortex Vortex Flow Indicator Feet of Water

560.5 3 0 0 -0.05 0.84 0 0 +0.04 0.85 0 0 +0.08 2.4

561.5 3 0 0 -0.05 0.5

5 0 0 +0.08 2.6

562.5 3 0 0 -0.06 0.44 0 0 +0.06 0.65 0 0 +0.05 2.2

563.5 3 0 0 -0.05 0.64 0 0 +0.05 0.45 0 0 +0.05 2.4

560.5 2 0 0 -0.11 0.44 0 0 +0.02 0.85 0 0 +0.07 1.4

561.5 2 0 0 -0.08 1.44 0 0 +0.01 1.45 0 0 -0.04 3.4

562.5 2 0 0 +0.11 0.44 0 0 +0.03 0.45 0 0 +0.04 2.0

563.5 2 0 0 -0.12 0.44 0 0 -0.05 0.45 0 0 +0.04 2.4

560.5 1 0 0 -0.11 1.44 0 0 +0.05 2.65 0 0 +0.08 2.0

561.5 1 0 0 -0.08 1.44 0 0 +0.04 1.65 0 0 +0.08 3.6

562.5 1 0 0 -0.04 1.24 0 0 +0.05 0.65 0 0 +0.05 4.0

(Continued)

Note: + =clockwise rotation; and - counterclockwise rotation.Water temperature =840-1050 F; air temperature =76*-97* F.

I

(Table 29 (Concluded)

Maximum Pressure

Sump El Pump Surface Submerged Swirl-Rotational Fluctuationft NGVD Bay No. Vortex Vortex Flow Indicator Feet of Water

563.5 1 0 0 -0.12 0.84 0 0 +0.07 o.45 0 0 +0.04 3.6

560.5 2 0 0 -0.11 0.43 0 0 +0.09 1.44 0 0 +0.16 0.6

561.5 2 0 0 -0.08 0.83 0 0 +0.03 0.44 0 0 +0.12 0.8

562.5 2 0 0 -0.09 0.43 0 0 -0.02 0.84 0 0 +0.14 0.6

563.5 2 0 0 -0.10 0.43 0 0 -0.02 0.84 0 0 +0.16 0.6

Table 30

Sump Performance, Type 3 Design Sump with Trashracks,

Type 11 Design Gates, 4 Pumps Operating

Maximum PressureSump El Pump Surface Submerged Swirl-Rotational Fluctuationft NGVD Bay No. Vortex Vortex Flow Indicator Feet of Water

561.5 2 0 0 -0.08 0.43 0 0 -0.03 2.04 0 0 +0.03 1.25 0 0 +0.06 2.8

562.5 2 0 0 -0.13 0.43 0 0 -0.03 1.64 0 0 +0.08 0.65 0 0 +0.05 2.8

563.5 2 0 0 -0.13 0.43 0 0 +0.02 0.44 0 0 +0.08 0.55 0 0 +0.05 2.0

561.5 1 0 0 -0.09 1.23 0 0 -0.02 0.64 0 0 +0.02 0.85 0 0 +0.10 1.6

562.5 1 0 0 -0.09 1.23 0 0 -0.04 0.64 0 0 +0.08 0.65 0 0 +0.04 2.4

563.5 1 0 0 -0.12 1.03 0 0 -0.05 0.84 0 0 +0.09 0.65 0 0 +0.05 2,0

561.5 1 0 0 -0.08 1.62 0 0 -0.02 0.44 0 0 +0.05 0.65 0 0 +0.10 2.8

562.5 1 0 0 -0.09 2.02 0 0 -0.02 0.44 0 0 +0.07 0.65 0 0 +0.04 2.0

563.5 1 0 0 -0.14 0.82 0 0 ±0.01 0.44 0 0 +0.05 0.45 0 0 +0.04 3.8

Note: + clockwise rotation; -=counterclockwise rotation; and ±=alter-nating rotation.Water temperature =94*-105* F; air temperature =800-94* F.

Table 31

Sump Performance, Type 3 Design Sump with Trashracks,

Type 11 Design Gates, 5 Pumps Operating

Maximum PressureSump El Pump Surface Submerged Swirl-Rotational Fluctuationft NGVD Bay No. Vortex Vortex Flow Indicator Feet of Water

562.5 1 0 0 -0.07 1.2

2 0 0 -0.05 0.4

3 0 0 ±0.01 0.6

4 0 0 +0.04 1.0

5 0 0 +0.08 1.2

563.5 1 0 0 -0.12 1.0

2 0 0 +0.02 0.8

3 0 0 -0.03 1.0

4 0 0 +0.08 o.4

5 0 0 +0.08 1.2

564.5 1 0 0 -0.11 1.2

2 0 0 +0.05 o.4

3 0 0 +0.02 o.6

4 0 0 +0.03 0.8

5 0 0 +0.04 1.2

Note: + = clockwise rotation; - = counterclockwise rotation; and - alter-nating rotation.Water temperature = 890-960 F; air temperature = 860-910 F.

.................................

F fF

• • I U i I S , UII

1.[a2 .8 1.3141.5 / 0.0 l.1' 9 1.21,4 .8 2.0

07 1.6 1.41.2 0. 09 1.1t It ,-. .,1' * . * t t 4 %r, .0' 'u•g ' S . .3.1..23.3 9 1. 1.4 1.21.01.0 1.2 1.44 32!,

0.9 1 1.0 -

a9 ae, 8

Aa A A .b # 4 n

i4 i3 1' 1.2-' I I

1.2 aI 1.4

SUMP WATER-SURFACE E L 562.0 FT5 PUMPS OPERATING

2. 0.2 1. *

t '16 2 2 1.57' . 142 1 8 ' f 294P6

I /t~at"'~ 10.7 ll

LEGENDI*. MEASURED VELOCITY, FPS

-- ----. F LOW DIRECTION BASEDON DYE INJECTION

TYPE 1 (ORIGINAL) DESIGN SUMPVELOCITY MEASUREMENTS

1.25 FT FROM FLOOR

PLATE 1

rr 4

o. .1. 0 8 o&'a8a 09 '0.6 06080-90076786.00077 0000

14£ &9 A i.14 f E.17a8a a39,0 a 4l50.7 6 081-0 s 1 7 0.6f 0. 0 .8a7

2.2 _0. 1 1 .502.71 1 . . *I It, £ -A I a7b o. 0.51.6~

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~~~~SUMP WATER-SURFACE EL 560.75 FT M AE-UFC L585F3~~~~ PUMPS OPERATING 1PM PRTN

LEGENDA

1.51.5- 91 .25 FT RO FLOO

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7 1__ _ _ _._t 1 4 4 0_______;2.

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1.7 1, 16 1.42 1. 10 1-SUMP WATER-SURFACE EL 558.5 FT

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2120 21 21

t922 131. 1.7 2~21.2 rn

2.2 2.1 . 22 2.21 2.3 1.4

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1 .9' 2. 0 ,-2 . 1. I 14?'~~~ 4 4' A i

1 2.12.2 12

TYPE 10DESIGN++

GUPEIDESIN TYPE 2 DESIGNGUIDEVANEGUIDE VANE

i " LEGEND

2.? -Z 4 -?a 29MEASURED VELOCITY. FPS---... FLOW DIRECTION BASED

ON DYE INJECTION

21 2.2 22

It I ""

1.92 1.7 1 ]

VELOCITY MEASUREMENTSTYPE 1 DESIGN GUIDE VANE 1.25 FT FROM FLOOR

TYPE 2 DESIGN VORTEX SUMP WATER-SURFACE EL 550.5 FTSUPPRESSOR BEAMS 1 PUMP OPERATING

PLATE 4

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NO. 5 NO. 4 NO. 3 NO. 2 NO. 1

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S'.5 ,If , , 2 5A it

SUMP WATER-SURFACE EL 562.0 FT* 5 PUMPS OPERATING

NO. 3 NO. 2 NO. 1 NO. 5

.1 12 a7 a

2-1 22 3. 3.4254~~15 t 22 1. +r33 ~l s,+123 124 + *

26 ag a . A~'

I I! It,.

-------- -------- ---------

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/ " SUMP WATE R-SURFACESUMP WATER-SURFACE EL 560.5 FT EL585FT

3 PUMPS OPERATING I PUMP 5 OPERATINGI I

LEGEND

MEASURED VELOCITY. FPS

--- --- FLOW DIRECTION BASEDON DYE INJECTION TYPE 2 DESIGN SUMP

VELOCITY MEASUREMENTS1.25 FT FROM FLOOR

PLATE 5

,. rF " .. I ..- , .

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NO. 5 NO. 4 NO. 3 NO. 2 NO. 1

73.0 4714.1 -. 17.a7 3 0 3 aI13.6

i',; f lu ,".;

SUMP WATER-SURFACE EL 562.0 FT

5 PUMPS OPERATING

NO.5 NO.4 NO.3 NO.5

293. 3. 4 .0. 340 3.~29 8' 4.4 #44 3. *

I I I I

i i

SUMP WATER-SURFACE EL 560.5 FT SUMP WATER-SURFACE EL 558.5 FT

3 PUMPS OPERATING 1 PUMP OPERATING

LEGEND.MEASURED VELOCITY. FPS

....- FLOW DIRECTION BASEDON DYE INJECTION

TYPE 3 DESIGN SUMP

~VELOCITY MEASUREMENTS

1.25 FT FROM FLOOR

PLATE 6

S W A T E R -S U R F A C E E L 5 . 5 F S W A E R S R E 558 .5 F T

.~~~~ PUMPS OPERTIN 1.. PUM .. ."P...ERAT:I- :I I ING