NBSIR 80-2041

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» FLUID FRICTION LOSSES IN TWO

SETS OF BLACK STEEL PIPE OF

RECENT MANUFACTURE ,

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J. R. Whetstone

National Bureau of Standards

Fluid Engineering Division

Washington, DC 20234

May 1 980

Prepared for American Iron and Steel Institute

1000 16th Street, N.W.

Washington, DC 20036

U.S. DEPARTMENT OF COMMERCE, Philip M. Klutznick. Secretary

Luther H. Hodges, Jr.. Deputy Secretary

Jordan J. Baruch, Assistant Secretary for Productivity, Technology, and Innovation

NATIONAL BUREAU OF STANDARDS, Ernest Ambler, Director

Fluid Friction Losses in Two Sets of

Black Steel Pipe of Recent Manufacture

* by

J. R. Whetstone

Fluid Engineering Division

CMEPT/NEL

Abstract

Two sets of black steel pipes have been flow-tested at the National Bureau

of Standards (NBS) to determine their fluid frictional loss characteristics. Twenty foot lengths of pipe furnished by the American Iron and

Steel Institute ranging from one to three inches nominal pipe size were tested using water in the primary flow measurement facilities at NBS.

These facilities use static gravimetric techniques with precision timing

to determine flow rates to within + 0.13% based upon three standard

deviations. Pipe pressure losses were measured using water and mercury

manometers for pipe flow velocities ranging from 4 to 16 feet per second.

Frictional loss characteristics of each pipe are characterized using the

conventional Hazen-Williams formulation at each flowrate.

Introduction

The basic equation relating fluid head loss or pressure loss to frictional loss in long straight tubes or pipes is the Darcy equation,

h

L

= f (L/D) (V 2

/ 2g) [1]

The loss in pressure or hydrostatic head h^ is proportional to

the velocity head, V^/2g, the length, L, and diameter, D, of the pipe in

compatible units. The dimensionless quantity, f, is known as the friction

factor and has been shown to depend on the pipe roughness and diameter

and the average velocity, V, of flowing fluid. Experimental studies by

Nikuradse [2], Colebrook [3] and Moody [4] have shown that the friction

factor is a function of the Reynolds number and can be related quantitatively to the physical height of the surface topography of the pipewall,

i.e.

,

the roughness height non-dimensionalized by the pipe diameter.

Empirical relations have been derived from experimental test data for

water flowing in pipes under turbulent conditions. One of the more widely

used in the U.S. is that of Hazen and Williams [5] which relates the average

velocity, V, the hydraulic radius R, and the head loss per unit length, S.

V = 1.318 C R0,63 S 0 * 54 [2]

where S = h/L

C = Hazen-Williams coefficient

L = length of pipe over which the head loss occurs

h = head loss in feet of the flowing fluid
2

Substitution of the hydraulic radius for a pipe of circular cross-section

(D = diameter in feet) into this relation yields

V = 1.318

n 0.63 . 0.54

(£> <£>

4 L

Inclusion of the kinematic viscosity, v

, and the Reynolds number, Rp, yields

h

194 D

-0.015

c 1.85 0.15 R 0.15

[(L) (V_)j

D 2g

[3]

This relation has the form of the Darcy equation with the friction factor

given in terms of the Hazen-Wi lliams coefficient.

f= 194 D"* 015

1. 85 0.15 p 0.15

V Kr. [4]

Neglecting the term D

* ^ , i.e. , assuming that its value is nearly

unity, it is evident that the friction factor is dependent only upon the

Reynolds number and Hazen-Wi lliams coefficient for fluids whose kinematic

viscosity exhibits small changes over the region of interest.

Computation of Hazen-Wi lliams Coefficient Values

The Hazen-Wi lliams coefficient may be expressed in the following

form for the purpose of computation from the experimentally determined

values and reported here.

C = Q [4.52 L/PD4 * 87

] °* 54 [5]

where Q

= flowrate gallons/minute (gpm)

P = pressure drop pounds/in^ (psi)

L = distance over which the pressure drop occurs (ft)

D = internal pipe diameter (in).

In this form only dimensional parameters are required to relate the pressure

loss in the pipe to the flowrate which is generally of primary interest.

Presently accepted values for the Hazen-Wi lliams coefficient are

based on data that was taken on steel pipe manufactured in a manner

which may have produced a higher degree of roughness of the wall than is

thought to be the case for steel pipe manufactured using more modern

methods. In order to test the effect of these newer manufacturing techniques
3

the American Iron and Steel Institute (AISI) has sponsored a set of

tests conducted in the primary flowmetering facilities of the National

Bureau of Standards (NBS). This test procedure has been performed with

two sets of five black steel pipes having nominal diameters ranging from

one to three inches and lengths of twenty feet.

Visual Inspection and Dimensional Measurements

Each pipe length was received at NBS with pressure taps installed as per recommendation of the American Society of Mechanical Engineers (ASME)

and placed ten pipe diameters from either end. Each tap was a circular

hole approximately one-eighth inch in diameter with a threaded fitting

welded to it so as to provide connection to the appropriate pressure

measurement device. These holes were inspected visually for smoothness

on the inside pipe wall. No obvious burrs or other irregularities around

the holes were detected. Such burrs or irregularities can cause pressure

drops associated with the holes themselves thereby introducing pressure

losses higher than those which actually occur along nonperf orated pipewalls.

Dimensional measurements were made at NBS to determine the characteristic lengths of the pipe sections. The results of measurements of

the internal diameters and distances between the pressure taps for each

pipe are given below.

Table 1

Pipe Internal Standard Pressure Tap

No. Diameter Deviation Separation

( inches) ( inches) (feet)

1A 1.0557 0.0032 18.86

IB 1.0659 0.0022 18.36

1.25A 1.3813 0.0017 17.83

1.25B 1.3892 0.0029 17.57

1 .5B 1.6238 0.0045 17.18

2A 2.0665 0.0050 16.39

2B 2.0919 0.0033 16.12

2.5A 2.4740 0.0030 15.55

3A 3.0738 0.0068 14.47

3B 3.0994 0.0040 13.63

The internal diameter of each pipe was measured at either end well

inside the slight taper located in the threaded end of the pipe. Several

observations were made on each pipe, involving a change in position of

the internal micrometer such that the micrometer lands contacted different

portions of the wall with each measurement. The value given above is

the average of the observed diameters taken at both ends of each pipe.

The variation in the diameter is indicated by the standard deviation of

the mean value. The accuracy of the micrometer measurements was 0.0005

inches over the diameter range as determined by repetitious observations

on master setting rings. The distance between the pressure taps was measured using a tape measure. This measurement was made between the

centerlines of the holes constituting the pressure taps. The uncertainty

of these measurements is approximately 0.06 inches, the primary component
A

of error being in the determination of the end points and in the nonreproducibility of the catenary of the tape.

Test Set-Up

Each pipe was tested by placing it in the test section of the NBS

primary water flow measurement facilities. Measurement of the water

flow rate through the pipe under test was determined by the gravimetric

technique. This technique of flowrate measurement requires measurement

of the mass of flowing liquid, in this case water, passing through the

pipe or flow measurement device over a measured period of time. The

density of the liquid must also be known or inferred from a measured

temperature. In this case, the temperature of the water is measured in

the pipeline and a value for the corresponding density is obtained from

tabulated values [6]. The flowrate measurement process involves diversion

of the flowing liquid into a weigh tank for the measured amount of time

and then diverted back into the sump of the flow loop. The water is

weighed and the mass flowrate is determined. Volumetric flowrate is

then obtained by division of the mass flowrate value by the density

value inferred from the temperature value. The uncertainty of the flowrate

values is 0.13% (3 standard deviations) for the facilities used in this

test. For the time period of the flowrate measurement the response of

the device under test is observed, i.e. , the pressure drop in the pipe

is measured and an average value determined.

A complete test was comprised of pressure response measurements

made at five flowrate values distributed over the desired range. At

each flowrate setting, five sets of observations were made. Generally,

observations at the five flowrates were made on one day and were repeated

on the following day. For all pipes except the two smallest sizes this

schedule was followed. At the two smallest sizes, all of the observations

were made on the same day although the measurement was shutdown after the

first series of five measurement and then restarted after an hour or two.

The fluid velocity range for these tests was A to 16 feet/second.

In most cases, however, the lower flowrate was approximately 5 feet/second.

These values correspond to approximately 25 to 300 gallons/minute for

these pipes.

The initial setup procedures were done using pipe number 3A. This

pipe was run for several days to shake down the system. This pipe was subjected to the corroding influence of water for a significantly longer

period of time than the other test specimens. The measurement results

reported for 3A reflect this fact.

Pressure difference measurements were made using either water or mercury manometers connected across the pressure taps of the pipe. The

range of the water manometer used is sixty inches corresponding to a pressure differential of approximately 1A50 pascals (Pa) or 2.1

pounds/inchz (psi). For pressures above approximately 2.0 pounds/inch , a mercury manometer was used. Observations of the manometer height were made throughout the time of each flowrate measurement. From A to 20

values were observed visually over the measurement times and the mean

value and standard deviation was calculated.
5

Results

The Hazen-Williams coefficient were calculated using [5] with the

observed flowrates, pressure differentials, lengths and diameters.

Values for the results and measured parameters are listed in Appendix I for each run. Mean values of the test results for each pipe are given in

Table 2 for each pipe. Friction factors have been computed using the

approximate form of equation 4, i.e., assuming D” * is unity.

Figures 1 through 4 are plots of the data.

Figure 1 shows the variation of the Hazen-Williams coefficient with

flow rate for the one inch and for the one and one-quarter inch pipes.

The dependence of the coefficient on flowrate is small in both cases and

the reproducibility less than 1%. In the next pipe size. Figure 2, only

one test specimen was supplied, i.e., 1.5 in. The data exhibits a higher

degree of scatter than that found for the smaller pipe sizes, i.e., approximately 2%, and is only slightly dependent on flowrate over this range.

Figure 3 shows that for the two inch size, a different situation has

occurred. The data shows an offset of one and one-half to three percent

between the runs from different days. The offset is essentially constant,

reproducing the shape of the curve characteristic of the previous day’s

data. Pipe 2A shows a significant downward shift of the coefficient

between the first and second set of observations. Pipe 2B shows a similar

shift but of smaller and more constant magnitude. The shape of the

response of the 2A indicates a continuous decrease in the Hazen-Williams

coefficient. This behavior may be explained by the continuous corrosion

of the pipewall by the water causing a steadily increasing wall roughness

and concommitant increase in frictional factor. For both of the two

inch diameter pipes the upper set of points (higher values of Hazen-Williams

coefficient) represent the first days results after which the pipes were

left in a filled condition overnight in the case of 2B or over a weekend

for 2A. It would appear that the longer delay in the case of 2A deteriorated

the walls to a greater degree increasing frictional losses. Only one pipe at the two and one-half inch size was tested. The results are plotted in figure 4. The upper set of points are the first day's results.

This pipe was removed from the test section rinsed with alcohol, and a rag pulled through it to dry the pipewalls. A week later it was installed

in the test section again and the second set of runs were made; the

results are the lower set of points. The results of the test on the

pipe 3B are similar (see Fig. 4) to those of 2. 5A although the coefficient values are higher and show a somewhat stronger dependence on flowrate. This pipe was treated similarly to 2. 5A in the removal and

drying procedure and was tested again about one week later. As discussed

earlier pipe 3A was used for a more extensive length of time and at

higher flowrates than the other pipes. The results listed in table 2 were derived from data taken after two or three days of shakedown testing

during which the level of corrosion of the pipewalls would be expected

to be greater than with those subjected to water for a shorter period of

time. It should be noted that the water used for this testing was highly

aerated by the pumps and diversion procedure, thereby providing the essential ingredients corroding these pipes. Visual observation of the amount

of rust present in each of the pipes after completion of the tests show

similar levels of corrosion in all pipes except 3A which appeared to

have rusted to a higher degree.
Table 2 Mean Values of Test Results

6

AISI PIPE FRICTION TESTS

PIPE DESIGNATION -- 1A

DATE JAN 9 80 OBSERVERS - JM PB

AVE, INNER DIA. - 1.0557 INCHES* TAP' SEPARATION - 18 ,959 FEET

GROUP FLOURATE DIFF. PRESS. HAZEN-UILLIAMS VELOCITY FRICTION PIPE

NO. MEAN STD. MEAN STD. MEAN STD. FACTOR REYNOLDS

( GPM

)

DEV(PSI

)

DEV. DEV. (FT/SEC) NUMBER

1 15.4 0.04 0.990 . OOt-6 148.32 0.05 5.64 0.0207 50366

njL. 20.1 0.07 1.597 .0101 149,30 0.12 7.35 0,0197 66647

3 23.5 0.01 2.107 .0117 150.52 0.42 8.61 0.0189 78319

4 28.0 0.01 2.900 .0030 150.99 0.06 10,27 0.0183 93371

5 31.7 0.03 3.656 .0109 150.91 0.13 11.63 0.0180 105777

6 31.7 0.03 3.655 .0064 150.35 0.03 11.62 0.0180 106598

7 23.0 0.01 2.900 .0031 150.32 0.11 10.25 0,0184 94053

8 23.4 0.02 2.098 .0030 150,12 0.04 8.57 0,0190 78488

oJ 20.1 0.10 1.600 .0023 149.79 0.72 7.39 0,0196 67403

10 15.8 0.01 1.020 .0021 148,37 0,12 5.73 0.0207 52472

AISI PIPE FRICTION TESTS

PIPE DESIGNATION — IB

DATE JAN 9 80 OBSERVERS - MH & JM

AVE, INNER DIA. - 1.065? INCHES? TAP SEPARATION - 13 ,364 FEET

GROUP FLOUR:ate DIFF, PRESS, HAZEN-UILLIAMS VELOCITY FRICTION PIPE

NO > MEAN STD, MEAN STD, MEAN STD, FACTOR REYNOLDS

( GPM

)

TrCII U!_V f ( PSI ) DEV, DEV, ( FT/SEC > NUMBER

1 16,1 0,00 1,016 0060 147,16 0,44 5,79 0 , 020? 547-4

24.0 0,01 2.140 .0040 146,79 0,19 8 , 64 0,0193 8049?

7 23,1 0,01 2.899 .0023 145,74 0.09 10,11 0,0196 94135

A

~T 31,5 0,09 3.606 .0162 144,35 0,09 11.31 0,0195 105630

5 28.0 0.05 2,873 .0109 145.70 0.05 10,06 0,0196 OTQC: L 7 w / -.j L

\J 31.4 0.13 3.593 ,0295 144,78 0,06 11,23 0.0195 105361

7 23.5 0.01 2.034 .0009 145,33 0.04 3,44 0,0202 78794

8 20,3 0,01 1.533 .0026 145,32 0,10 7.29 0 , 0206 67602

g/ 15.9 0.02 1.008 * u045 145,35 0.44 5,72 0,0213 52933

10 20.3 0,01 1,597 ,0087 145.27 0,41 7,30 0 , 0207 6766?
7

Table 2 (cont.)

AISI PIPE FRICTION TESTS

PIPE DESIGNATION — 1.25A

DATE 1/11/30 OBSERVERS - JM JH

AvE * INNER DIA* - 1.3313 INCHES? TAP SEPARATI ON - 17 .833 FEET

GROUP FLOURATE DIFF* PRESS. HAZEN-UILLIAMS VELOCITY FRICTION PIPE

NO* MEAN STD* MEAN STD. MEAN STD. FACTOR REYNOLDS

( GPM

)

DEV

.

(PSI

)

DEV. DEV. ( FT/SEC

)

NUMBER

1 27*5 0.14 0.699 .0056 153.03 0.13 5.39 0.0137 72039

n 35.0 0.11 1.102 .0003 152.22 0.46 7.49 0.0182 92005

3 42*3 0*02 1.573 .0013 151.34 0.14 9.06 0,0173 111216

4 47.7 0*01 1.959 .0033 151.36 0.15 10.20 0.0174 125264

ETxJ 55.1 0*02 2.599 .0035 150.33 0.10 11.81 0.0173 144937

6 55*5 0*06 2.641 .0025 150.36 0.19 11.87 0.0174 145769

V/ 47*3 0*03 1.933 .0029 151.29 0.18 10.23 0,0176 125934

3 41.8 0*01 1.553 .0017 150.60 0.12 8.94 0.0131 110333

9 34*1 0*03 1.070 .0017 150.76 0.14 7.30 0.0186 90.140

10 27.2 0.01 0.705 .0017 150.54 0.17 5.82 0.0193 71370

11 54*3 0*07 2.596 .0121 150.03 0.55 11.74 0,0175 140305

AISI PIPE FRICTION TESTS

PIPE DESIGNATION — 1.25B

DATE 1/11/30 OBSERVERS - JH S. JH

ainVL INNER DIA, - 1.3892 INCHES? TAP SEPARATION - 17 .572 FEET

GROUP FLOURATE DIFF. PRESS. HAZEN-UJLLIAHS VELOCITY FRICTION PIPE

NO i MEAN OTfi u » J.»* MEAN STD. MEAN STD. FACTOR REYNOLDS

( GPM

)

DEV. (PSI ) DEV. DEV. ( FT/SEC

)

NUMBER

4X 26,4 0.02 0,632 .0026 145.51 0.26 5,59 0 , 0206 67691

9 33,9 0.02 1,096 .0024 144,30 0.12 7.17 0 . 0202 36746

2 40.5 0.03 1.551 .0044 142,93 0.12 8.56 0.0200 103682

AT

f s a T J , T 0.13 1.911 .0033 143,23 0.40 9.61 0,0196 116303

ET

xJ

e-"-) o vJi. , U 0.01 2.539 ,0051 141.35 0.13 11.17 0.0196 135229

£* 53.3 0.04 2.647 ,0046 141 , 18 0.16 11.29 0.0196 139009

7/ 45.7 0,02 1.951 .0034 142,69 0,13 9.63 0,0197 119146

8 40.6 0.01 1.566 ,0019 142.72 0,09 8.60 0,0201 105330

9 33.9 0.05 1.106 .0047 143,74 0.14 7.17 0 , 0203 33302

10 26.8 0,01 0.709 .0011 144.53 0.13 5 V u/ 0.0209 69321
8

Table 2 (cont.)

AISI PIPE FRICTION TESTS

PIPE DESIGNATION — 1.5B

DATE JAN 4 SO OBSERVERS - JH & HH

AVE. INNER DIA. - 1.6233 inches; TAP SEPARATION - 17 *177 FEET

ROUP FLOWRATE DIFF* PRESS* HAZEN-UILLIAMS VELOCITY FRICTION PIPE

NO* MEAN STD* MEAN STD. MEAN STD. FACTOR REYNOLDS

( GPH

)

DEV

.

( PSI > DEV

.

DEV. (FT/SEC) NUMBER

1 59*1 0.07 1.268 .0021 152.51 0.06 9*15 0.0172 127414

9 68*7 0.16 1.634 « 0085 151.97 0.13 10*64 0*0169 148472

3 75*3 0.29 2*036 .0144 151.48 0,15 11*75 0.0167 164334

4 76.1 0.13 2.050 .0036 151.43 0*09 11*79 0,0163 165193

5 63*1 0.21 1.665 .0105 151.66 0.06 10*55 0*0170 148326

6 61*3 0*47 1.373 .0215 151*55 0*33 9*50 0*0173 133924

~r

/ 75*6 0*03 2.076 .0023 149,39 0*21 11*71 0*0172 160966

3 104.2 1.54 3.392 .0395 146,62 2.35 16*14 0*0170 222594

o/ 99*6 0.31 3.540 .0164 147,60 0.16 15*44 0*0169 213363

10 76.6 0*14 2.151 *0034 148.66 0*13 11*38 0.0173 164574

11 46*6 0*42 0*357 .0145 148*68 0*32 7*22 0,0186 101049

12 36*4 0*04 0.535 *0025 149.39 0*23 5*65 0*0191 73997

13 36*7 0*01 0.545 .0016 149*63 0.23 5.69 0.0191 79661

14 47*0 0*01 0*369 *0007 148*85 0*08 7*29 0,0186 101979

AISI PIPE FRICTION T ESTS

PIPE DESIGNATION — 2A DATE 12/ 28-31/7 OBSERVERS - JH VB

AVE. INNER DIA* - 2*0665 inches; TAP SEPfi(RATION - 16 , 385 FEET

ROUP FLOWRATE DIFF* PRESS, HAZEN-WILLIAHS VELOCITY FRICTION PIPE

NO* MEAN STD* MEAN STD* MEAN STD* FACTOR REYNOLDS

( GPM

)

DEV* (PSI

)

DEV. DEV* ( FT./SEC > NUMBER

i

J. 61.9 0.05 0*414 *0013 151*23 0*28 5*92 0*0180 103374

9 75,7 0.33 0,616 .0073 149*11 0*31 7*24 0,0179 1.27502

-y

vJ 89*1 0*21 0*854 *0013 147,13 0*33 8*52 0*0179 150607

4 105*2 0*14 1*189 *0064 145*23 0.23 10*07 0*0179 178424

5 119.4 0*13 1*537 . 0060 143.47 0*32 11,42 0,0179 202978

6 134*9 0*70 1*997 ,0059 140*75 0*82 12*91 0*0182 230155

7 133*0 0*27 1*986 .0037 139,10 0*47 12*72 0.0187 221604

8 116.2 0*39 1.542 .0077 139*40 0*51 11*11 0,0190 194350

o/ 101.0 0,83 1,197 *0206 139*00 0.69 9.66 0.0195 169430

10 35*7 0.55 0*835 .0033 138*75 0,72 8.19 0,0201 144137

11 70.9 0.18 0*623 .0048 138*14 0.61 6*78 0.0208 119505

i nJ. A. 54 * 5 0*18 0 . 337 *0030 138.14 0*37 5*22 0,0216 92076
9

Table 2 (cont.)

AISI PIPE FRICTION TESTS

PIPE DESIGNATION — 2B

DATE 1/2/80 OBSERVERS - JH VB KH

AVE. INNER DIA. - 2.0919 inches; TAP SEPARATION - 16 .125 FEET

GROUP FLOWRATE DIFF. PRESS. HAZEN-UILLIAKS VELOCITY FRICTION PIPE

NO. KEAN STD. KEAN STD. KEAN STD. FACTOR REYNOLDS

( GPH

)

DEV. (PSI

)

DEV. DEV. (FT/SEC) NUMBER

1 146.6 0.13 1.974 .0027 147.77 0.13 13.69 0.0165 240938

9 127.1 0.06 1.504 .0027 143.37 0.13 11.86 0.0167 209545

3 111.9 0.12 1.182 .0023 143.77 0.18 10.44 0.0170 184669

XT 95.3 0.31 0.874 .0043 149.15 0.36 8.39 0.0173 157770

5 78.6 0.32 0.607 .0033 149.86 0.18 7.34 0.0177 130439

6 62.5 0.32 0.394 .0029 150.44 0.24 5.34 0.0131 103915

7/ 112.5 0.21 1.219 .0009 147.07 0.22 10.50 0.0173 185333

8 126.4 0.10 1.547 .0013 145.32 0.14 11.80 0.0174 209635

9 144.4 0.12 2.018 .0023 143.82 0.16 13.48 0.0174 240206

10 94.5 0.10 0.879 .0026 147.43 0.27 8.32 0.0177 157799

11 78.4 0.17 0.613 .0022 147.93 0.41 7.32 0.0131 131420

12 60.5 0.65 0.380 .0096 148.61 0.76 5.65 0.0136 101736

AISI PIPE FRICTION TESTS

PIPE DESIGNATION — 2.5A

DATE 12/ 19/79 OBSERVERS - JH VB

AVE. INNER DIA. - 2.474 INCHES; TAP SEPARATION - 15. 552 FEET

fi! <p u w r FLOWRATE DIFF. P

Dirc-o

l\l- vJ vJ * HAZEN-UILLIAMS VELOCITY FRICTION PIPE

n

i_> * KEAN qrn 3 » i.» KEAN STD, KEAN STD. FACTOR REYNOLDS

( GPK

)

PCI ! ( PSI ) DEV, DEV, < FT /SEC > NUMBER

i 34.5 1.60 0.238 .0096 152.11 0.32 5.64 0.0174 117890

9 109.3 n no V- V u 0.432 ,0150 143.73 0.50 7.29 0,0175 152946

131.0 0.5/ 0.635 » OOui-^ 147,50 0.30 3,74 0,0173 183774

4 152.9 1.72 0.927 .0236 146.15 0.62 10,20 0.0172 212909

5 200.1 0.72 1.581 ,0036 143.41 0.14 13.36 0.0171 280002

175.7 0.22 1.245 .0015 143.21 0.13 11.72 0.0174 246643

7 208.6 0.55 1.537 .0105 149.13 0,16 13.92 0.0158 291264

O 184.4 0.33 1.259 .0036 149,45 0,27 12.31 0.0160 253119

9 152.9 0.17 0.399 .0023 143.62 0.22 10.21 0.0166 214902

10 132.3 0.07 0.639 ,0027 148.54 0.27 8,33 0.0170 18651.1

11 111.0 0.02 0.493 .0017 143,44 0,23 7.41 0.0175 156964

4 OJL 83.1 0.41 0,290 ,0029 148,86 0.35 5.55 0.0182 117375
10

Table 2 (cont.)

AISI PIPE FRICTION TESTS

PIPE DESIGNATION — 3A

DATE 12/21/79 OBSERVERS - VB 6 JH

A'v'E. INNER DIA. - 3.0733 INCHES? TAF- SEPARATION - 14 .469 FEET

GROUP FLOWRATE DIFF. PRESS. HAZEN-UILLIAMS VELOCITY FRICTION PIPE

NO. MEAN STD. MEAN STD. MEAN STD. FACTOR REYNOLDS

( GPM

)

DEV. (PSI) DEV. DEV. (FT/SEC) NUMBER

1 499.4 1.03 3.278 .0106 131.03 0.12 21.59 0,0182 545252

9 300.3 1.16 1.241 .0114 133.19 0.28 12.98 0.0190 331702

3 276.2 4.97 1.079 .0373 132.15 0.21 11.94 0.0195 301149

4 240.0 0.23 0.806 .0020 134.33 0.21 10.38 0,0194 262850

5 202.3 0.34 0.581 .0021 135.19 0.41 8,74 0,0196 223167

6 160.2 0.59 0.364 .0037 137.87 0.62 6.93 0.0196 177457

7 121.1 0.04 0.209 .0040 140.76 1.43 5.24 0.0197 134573

3 99.2 0.02 0.140 .0027 143.10 1.50 4.29 0.0197 110522

9 122.3 1.55 0.210 .0056 141.85 0.32 5,29 0.0194 138627

10 153.1 0.68 0.363 .0025 136.21 0.16 6.83 0.0201 179709

11 193.3 0.87 0.530 .0066 129.35 0.29 8.36 0.0215 219928

12 224.7 1.43 0.805 .0106 125.95 0.14 9.72 0,0220 256302

13 237.1 0.81 0.913 ,0059 124.18 0.14 10,25 0.0224 27183.1

14 256.5 0.95 1.032 ,0035 122.57 0.14 11,09 0,0227 294884

AISI PIPE FRICTION TESTS

PIPE DESIGNATION — 3B

DATE DEC 19 & 2 OBSERVERS - JH VB M,4 AVE. INNER DIA. - 3.0994 INCHES? TAP SEPARATION - 13 ,635 FEET

GROUP FLOUR:ATE DIFF. PRESS, HAZENHIILLIAMS VELOCITY FRICTION PIPE

NO. MEAN STD. MEAN STD. MEAN STD. FACTOR REYNOLDS

( GPM

)

DEV

,

(PSI

)

DEV. DEV. (FT/SEC) NUMBER

1 99,7 1,43 0,098 .0023 164.87 0.39 4.24 0,0151 109963

9 117.1 1.52 0.138 .0035 161,54 0,67 4.98 0,0153 129492

3 161.3 1.19 0,264 ,0035 156.50 0.37 6.86 0.0155 179054

4 206,2 0.99 0.429 .0037 153.80 0.25 3,77 0.0154 229464

5 231,1 1.14 0.540 ,0053 152.26 0.21 9.33 0.0155 255430

6 231,9 1.94 0.805 .0113 149.66 0.19 11,99 0.0155 312485

7 285.7 0.20 0.794 ,0007 152.89 0.10 12.15 0,0149 314463

8 233.9 0,11 0.540 .0011 154.09 0,16 9.95 0,0151 258407

9 208.6 0.61 0.434 .0027 154,68 0.13 8.87 0.0153 231100

10 161.4 1.03 0.263 .0035 156.81 0.21 6.86 0,0155 179282

11 113.7 0,67 0.133 .0018 159.63 0.30 4.84 0,0158 126933

12 95.0 1.01 0.092 .0021 162,59 0.65 4,04 0,0157 106235
1.25 A

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12

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15

Conclusions

Due to the relatively small dependence on flowrate of the HazenWilliams coefficient over the range of flowrate considered here, an average value may be used to characterize the frictional losses in the

pipes. Table 3 gives these averages for the coefficients for the

various pipes.

Table 3

Average Values of Hazen-Williams Coefficient

For a Flowrate Range of 4 to 16 Feet/ Second for Black

Steel Pipes Having Diameters Ranging From 1 to 3 Inches

Ident. Hazen-Williams Coefficient

No. Mean Range

1A 150.0 148-151

IB 145.7 144-147

1.25A 151.2 150-153

1.25B 143.2 141-145

1.5B 150.0 148-153

2A 142.5 138-151

2B 147.9 143-151

2.5A 147.8 143-152

3A 133.4 122-143

3B 156.6 149-165

The relationship between the friction factor and the relative roughness of the pipe, defined as the ratio of the height of the surface

features to the pipe diameter was developed by Colebrook and Moody. A

portion of a Moody diagram has been reproduced in figure 5 which covers

the range of these tests.

The friction factors for all pipe sizes below three inches are indicative of relative roughness values ranging from .0004 down to the

smooth pipe curve. The points which lie significantly above the .0004 curve are those for the 3A pipe which exhibit the increased friction

factor and, therefore, relative roughness caused by the prolonged exposure

of the specimen to the corrosive effects of the fully aerated water used

throughout this test. The friction factors for the 3B specimen are not

plotted but lie below the smooth pipe curve. With the exception of the

3B pipe the friction factors inferred from this test are in agreement

with the values expected from the Moody diagram.
0.024

( 0/3 ) SS3NH9n0H 3AI1V138

16

CM

2I»a

0?

•H

Pm

U010VJ NOliOldi

REYNOLDS

NUMBER
17

References

1. Streeter, V. L. , Fluid Mechanics , Fifth Ed. , McGraw-Hill, 1971.

2. Nikuradse, J. , "Stromungsgesetge in rauhen Rohren,"

VDI-Forschungshef t , 361, 1933. Translation available in NACA,

Tech. Mem. 1292.

3. Colebrook, C. F. , "Turbulent Flow in Pipes, with Particular

Reference to the Transition Region between the Smooth and Rough

Pipe Laws," Jour. Inst. Civil Engrs. , London, p. 133, Feb. 1939.

4. Moody, L. F. , "Friction Factors for Pipe Flow," Trans. ASME,

Vol. 66, p. 671.

5. Williams, G. S. and Hazen, A., Hydraulic Tables , Third Ed.,

John Wiley and Sons, 1933.

6. Wagenbreth, H. and Blanche, W. , PTB-Mitt. S8425F.

Appendix

Tables of Data and Results

1

AISI PIPE FRICTION TESTS PIPE DESIGNATION - 1A DATE JAM 9 80 OBSERVERS - Jil Pb

AVE. INNER DIA. - 1,0557 INCHES! TAP SEPARATION - 13.359 FEET

RUN TARE GROSS DIVERT MANOMETER HATER STATIC FLOW IuFF. HAZEN PIPE

NO. «T WT TIKE [EIGHT STD. TEMP. TEMP, PRESS. RATE PRESS. WILLIAMS REYNOLDS (RN> (LB) (LB) (SEC) (INCH) DEV. (DEG C) (DEG C) (PSIA) (GPM) (PSD CGEFF, NUMBER

HAND. FLUID - WATER BAROMETER - 75.81 CM OF MERCURY AIR TEMPERATURE - 20.95 DEGREES CELCIUS

1 0.0 200,0 93,443 27,770 0.127 21,80 24,86 110,30 15,4 0,9966 143,26 51043,5

2 0.0 200,0 93,633 27.635 0.089 22,10 24.36 110,20 15.4 0.9917 143,36 50942,6

3 0.0 200,0 93,890 27 . 4-95 0.091 22.20 24.86 110.30 15.4 0,9367 143.37 50803.2

4 0.0 200.0 93,925 27,513 0.120 22,30 24.86 110.30 15,4 0.9873 143,26 50784.2

5 0.0 200,0 93,976 27,460 0.193 22.40 24,86 110.20 15.4 0,9854 143,34 50/ j6.7

MANO. FLUID - WATER BAROMETER - 75,81 CM OF MERCURY AIR TEMPERATURE -- 21.27 DEGREES CELCIUS

6 0.0 200.0 72.3S9 44.000 0.079 22,40 24,86 109,50 19,9 1.5789 DV.Zj 65892.7

7 0.0 200,0 71.804 44,566 0.130 22,50 24,86 109,40 20,1 1,5992 149.43 66429,5

8 0.0 200.0 71.813 44,564 0.111 22,50 Of 07

L\it iJ 109,40 20.1 1,5991 149,43 66984,4

9 0.0 200,0 71.823 44.703 0,146 22,60 o=; 07 iJ. i./ 109.50 20,1 1,6041 149.16 66975,1

10 0.0 200,0 71,846 44,635 0.036 22,55 OS 07 109,40 20.1 1,6017 149.23 66953.7

HAND. FLUID -- FIG BAROMETER -- 75,83 CM OF MERCURY AIR TEMPERATURE - 21.47 DEGREES CELCIUS

11 0.0 200.0 61.440 4,598 0,009 21,40 25,27 110,00 23.5 2,0933 151.00 78293,4

12 0.0 200,0 61,415 4,611 0.005 21,30 25,27 110. 00 23.5 2,0996 150,82 78325,3

13 0.0 200.0 61.430 4.622 0,009 21,35 oc 07 tJ.i/ 110,00 23,5 2,1046 150,59 78306.0

14 0.0 200,0 61,406 4,646 0.003 21,40 25,27 110.00 23.5 2,1154 150.23 78336,3

15 0.0 200,0 61.407 4.661 0,007 21,40 oc; 07Z.J* LJ 110,00 23.5 2.1222 149,96 78335,5

HANQ. FLUID - 14G BAROMETER -- 75,82 CM OF MERCURY AIR TEMPERATURE - 21.48 DEGREES CELCIUS

16 0,0 200,0 51,519 6,365 0.014 21,40 25,27 110,00 28.0 2,8931 151,04 93370.4

17 0,0 200,0 51.503 6.369 0,015 21.50 25,27 110,00 28,0 2,3999 151,02 93390.3

18 0.0 200,0 51,528 6,363 0.016 21.50 OS 07 LxJkLJ 110.00 23.0 2,3995 150.97 93354.1

19 0,0 200.0 51.533 6,363 0,016 21.55 25,27 110,00 28,0 2.8973 151.02 93345,0

20 0,0 200,0 51.504 6.330 0,011 21.60 25.27 110.00 28.0 ro o CO 150,3'? 93397,6

KANO, FLUID - HG BAROMETER -- 75.81 CM OF MERCURY AIR TEMPERATURE - 21.59 DEGREES CELCIUS

21 0.0 200.0 45,450 8,053 0.028 21.60 OS 07 lJ .i/ 110.00 31,7 3.6666 150.77 105838,0

22 0,0 200.0 45.456 8,051 0,025 21.60 OS 07 iJ *u 110.00 31.7 3.6653 150,76 105324.0

23 0,0 200.0 45,424 8,038 0.032 21.70 25,27 110,00 31,8 3.6596 151,01 105299.0

24 0,0 200,0 45.503 8,007 0,010 21,70 25,27 110,00 31,7 3.6454 151,05 10j70^.0

25 0.0 200.0 45,543 8,004 0.019 21.65 OS 07 110,00 31,7 3,6442 150,96 105622,0

HAND. FLUID - HG BAROMETER -- 75.81 CM Ofr MERCURY AIR TEMPERATURE - 20.7 DEGREES CELCIUS

26 0,0 200.0 45,463 8,046 0.023 21.70 25,75 110,00 31,7 3,6635 150.81 106355.0

27 0.0 200.0 45.431 8.030 0,019 21.75 25,75 110.00 31.7 3,6560 150.92 106312,0

28 0.0 200,0 45.545 8,028 0.016 21,80 25,75 110.00 31.7 3.6552 150,73 106662.0

29 0.0 200,0 45,521 8,024 0.016 21,80 25.75 110.00 31.7 3,6532 150,35 106718,0

30 0.0 200.0 45,545 8,007 0.006 21.80 25.42 110.00 31,7 3.6457 150.92 105944,0
2

AISI PIPE FRICTION TESTS PIPE DESIGNATION - 1A DATE JAN 9 £0 OLSEftVtRS - JTS PS

AVE. INNER HI A. -1 , 0jj7 inches; TAP SEPARATION - 13.359 FEET

RUN TARE GROSS DIVERT NANOMETER HATER STATIC FLO'.! DIFF, HAZE)! PIPE

NO, «r HT TIKE HEIGHT STD, TEMP, TEMP. F'RcSS

,

RATE PRESS, UILLLVvS REYNOLDS

(RN)' (LB) (LB) (SEC) (INCH) DEO. (DEG C) (DEG C) (PSIA) (GPM) (PSI) CO-FF, NUMBER

HAND. FLUID - US BAROMETER - - 75,81 CM OF MERCURY AIR TEMPERATURE - 21,75 lEGrvr.ES CELCIUS

31 0,0 200.0 51.553 6,375 0,010 21.30 25,75 110,00 23,0 2,9027 150,83 s9'/231 ,

3

32 0,0 200,0 51.604 6,374 0.003 21.90 25.41 110,00 23,0 2,901? 150,69 93434.9

33 0,0 200,0 51,602 6,350 0,013 21,90 25,75 110,00 28,0 2 1 89u5 150.89 94141.3

34 0,0 200,0 51.551 6,355 0.012 21,90 25,75 110,00 28,0 2,8931 150.96 94235,0

35 0.0 200.0 51.5S6 6.375 0.012 21,90 25.75 110,00 23,0 2,9023 150.74 94171,0

KANO. FLUID -- US BAROMETER -~ 75.81. CM OF MERCURY AIR TEMPFEATURE - 21.8 DEGREES CELCIUS

36 0,0 200,0 61,657 4.619 0,017 21.90 25,75 110.00 23,4 2,1031 150.11 78/89.2

37 0.0 200,0 61.703 4.610 0,007 21,90 25,42 110,00 23.4 2,093? 150.13 78193.8

33 0.0 200,0 61,715 4,607 0,003 21,95 25.75 110,00 23,4 2 , 0 )7 D 150,13 / 3/ ij , 1 3? 0,0 200.0 61,786 4,603 0.035 22,00 25,42 110,00 23,4 2,0957 150,06 78095.1

40 0,0 200.0 61,769 4,604 0,005 22,00 25,75 110,00 23,4 2,0961 150,11 / 364 6 , 3

HAND, FLUID - WATER BAROMETER -- 75,8 CM OF MERCURY AIR TEMPERATURE - 21,89 DEGREES CELCIUS

41 0.0 200,0 71,733 44,497 0,170 22.95 25,41 103,90 20.1 1,5966 149.72 o7u4; ,

3

42 0,0 200.0 71.753 44,632 0,035 22,90 25.41 109,80 20,1 1,6015 149.43 67 2/6,6

43 0,0 200,0 71,000 44,617 0,053 23,00 25,41 103,90 20,3 1,600? 151,06 67946.3

44 0,0 200,0 71,776 44.652 0,100 23.05 25,41 103,90 20,1 1,6025 14? , 64 £771 \ 7 0/ 45 0,0 200,0 71,790 44,617 0.103 23.05 25,56 109.00 20.1 1,6003 149.40 6/4 J j,

6

HAND. FLUID - WATER BAROMETER - 75.79 CM OF MERCURY AIR TEMPERATURE - 21,93 DEGREESi CtLCIUS

46 0,0 200,0 92.171 23,532 0.102 23.25 25,56 109,70 15.7 1,0237 143,13 52500,7

47 0,0 200,0 92.219 28,443 0,075 23,25 25,56 109,80 15.6 1,0205 143,35 52473,4

43 0,0 200,0 92,233 23,381 0.128 23.40 25,56 109.90 15.6 1,0132 143,50

49 0,0 200,0 92,221 28,409 0.153 23,40 25,56 109, 9-0 15.6 1,0192 143,45 52472.3

50 0,0 200,0 92,259 28,420 0.192 23.50 25,56 109,80 15,6 1,0196 143.36 52450,7
3

AISI PIPE FRICTION TESTS

PIPE DESIGNATION — 1A

DATE JAN 9 SO OBSERVERS - Jfi PB

AVE» INNER DIA. - 1.0557 INCHES? TAP SEPARATION - 18*859 FEET

GROUP FLOURATE DIFF, PRESS* HAZEN-UILLIANS VELOCITY FRICTION PIPE

NU. HEAH STD. HEAN STD. HEAN STD. FAC 1 OR REYNOLDS

( GPfi

)

DEV* ( PSI

)

DEV. DEV. (FT/SEC) NUHBER

1 15*4 0.04 0.990 ,0046 148.32 0*05 5.64 0.0207 50366

9 20*1 0,07 1.597 .0101 149.30 0.12 / * 35 0.0197 6664/

3 23*5 0*01 2.107 .0117 150*52 0.42 8,61 0.0139 78319

4 23*0 0.01 2,900 .0030 150.99 0*06 10.27 0.0133 93371

5 31,7 0.03 3*656 .0109 150.91 0*13 11.63 0.0130 105777

6 31*7 0*03 3*655 .0064 150.35 0.03 11, iiZ 0.0130 106593

7 28*0 0*01 2.900 .0031 150*32 0*11 10.25 0*0134 94053

oU 23,4 0*02 2.093 .0030 150.12 0*04 3*57 0.0190 73433

9 20*1 0,10 1.600 ,0023 149*79 0,72 7.39 0.0196 67403

10 15*6 0.01 1.020 .0021 143*37 0*12 5.73 0.0207 52472
A

AISI PIPE FRICTION TESTS PIPE DESIGNATION - IB DATE JAN 9 80 OBSERVERS - HH L JM Ml, INNER DIA. - 1.0559 INCHES? TAP SEPARATION - 13,364 FEET

RUN TARE GROSS DIVERT MANOMETER: WATER STATIC FLO') DIFF. HAZEM PIPE

NO. WT WT TIME HEIGHT STD. TEMP. TEMP. PRESS. RATE PRESS, WILLIAMS REYNOLDS (RN) (LB) (LB) (SEC) (INCH) DEV. (DEG C) (DEG C) (PSIA) (GPM) (PSI) CuEFF. NUMBER

HAND. FLUID - WATER BAROMETER -• 75,77 CM OF MERCURY AIR TEMPERATURE ~ 22.42 DEGREES CELCIUS

1 0.0 200.0 89,557 23,570 0,173 23,90 26,69 116,40 16,1 1,0246 146.55 54762.2

0

A. 0.0 200.0 89,532 23,454 0,028 24.00 26,69 116,40 16.1 1,0204 146.33 54746,9

3 0.0 200,0 89.611 23,222 0,422 24,10 26,69 116,50 16.1 1,0120 1(7.44 54729.2

4 0.0 200,0 89,577 28,215 0.255 24,10 26.69 116,50 16.1 1.0113 147,51 54750,0

5 0.0 200,0 89,603 28,212 0,213 24,20 26.69 116,50 16.1 1,0116 147,47 54731,0

HAND. FLUID - HG BAROMETER -- 75.79 CM OF MERCURY AIR TEMPERATURE - 22,77 DEGREES CELCIUS

26 0.0 200.0 60,025 4.691 0.016 22,80 25.97 0,00 24,0 2,1354 146,93 80317 ,

6

27 0.0 200.0 60.003 4,696 0.016 22,80 25.97 0.00 24.1 2,1380 146,94 80547.1 28 0,0 200.0 60,056 4,699 0,024 22,85 25,97 0.00 24.0 2,1394 14u,7

6

80476,0

29 0,0 200,0 60,050 4,700 0.013 22,90 25,97 0,00 24,0 2,1397 146,76 80434,0

30 0.0 200.0 60.060 4,714 0,026 22,90 25,97 0,00 24,0 2,1462 146,49 30470.6

NANO. FLUID - HG BAROMETER -- 75,78 CM OF MERCURY iAIR TEMPERATURE - 22,31 DEGREES CELCIUS

31 0.0 200.0 51.303 6,362 0,029 22,90 25.97 0,00 23,1 2,8963 145*85 942-06,3 32 0,0 200.0 51,30/ 6,365 0.026 22,90 25,97 0,00 28,1 2,8977 145.80 94193,9

33 0.0 200.0 51,292 6.371 0,029 22,90 25,97 0.00 23.1 2,9004 145,77 94226,5

34 0,0 200.0 51,322 6,375 0,023 22,90 25.97 0,00 23,1 2,9022 145.63 94171.4

35 0.0 200.0 51.349 6.367 0,021 23.00 25.97 0,00 28,1 2,8986 145.66 94123,7

HAM. FLUID -- ;HG BAROMETER - - 75.79 CM OF MERCURY AIR TEMPERATUSE - 22,82 DEGREES CELCIUS

36 0.0 200,0 45,716 7,969 0.040 23,00 26,11 0.00 31,6 3,6279 144,92 10&02.L , 0 37 0.0 200.0 45,804 7,936 0.054 23,00 26.11 0.00 31.5 3,6128 144.96 105813,0

38 0.0 200.0 45.830 7,929 0,025 23.00 26,11 0,00 31.5 3,6095 144,30 105643.0

3? 0.0 200.0 45,996 7,833 0,043 23.00 26,11 0,00 31.4 3,5910 144,83 105376,0

40 0.0 200,0 46.033 7,834 0,023 23.00 26,11 0,00 31.4 3.5S92 144.76 105291,0

HAND. FLUID - HG BAROMETER -- 75,76» CM OF MERCURY AIR TEMPERATURE - 22,33 Dl.GrEE:s CELCIUS

41 0.0 200.0 51,423 6,343 0.039 23,00 26,11 0.00 23.1 0 0007

l. *Go7/ 145.69 94255,0

42 0.0 200.0 51.561 6.320 0.027 23.10 26,11 0.00 28.0 2.8771 145.64 Qi.yn 7

7 T'J J » / 43 0,0 200,0 51.662 6,294 0.016 23,05 26,11 0,00 27.9 2,8654 145,68 93319.0

44 0.0 200.0 51 . 633 6,293 0.023 23.05 26.11 0.00 28,0 2.8648 145.78 93371,7

45 0.0 200.0 51.654 6,295 0,020 23.10 26.11 0.00 27,9 2.8657 145.69 93833.5

HANS. FLUID -* HG BAROMETER -- 75,76 CM OF MERCURY AIR TEMPERATURE.- 22,88 DEGREES CELCIUS

46 0.0 200,0 45,721 7,983 0,030 23.15 26,11 0.00 31,6 3.6365 144.72 106010,0

47 0.0 200.0 45.943 7,913 0.027 23.20 26,11 0.00 31.4 3.6023 144,75 105498,0 43 0,0 200.0 46,113 7,859 0.032 23,20 26.11 0,00 31,3 3.5773 144.76 105109.0

49 0,0 200.0 46.250 7,815 0,016 23,10 26.11 0.00 31,2 3.5577 144,76 104797.0 50 0,0 200,0 (5.939 7.335 0.030 23,15 26.11 0.00 31,4 3.5396 144.89 105392,0
5

AlSi PIPE FRICTION TESTS PIPE DESIGNAI ION - IS SATE JAN 9 80 OBSERVERS - KH L Jrt AVE, INNER Din. - 1,0659 INCHES} TAP SEPARATION - 18,364 FEET

RUN TARE GROSS DIVERT NANOMETER — WATER STATIC FLOW DIFF, HAZEN PIPE

NO, IIT «T TINE HEIGHT STD, TEN?, TEH?. PRESS. RATE PRESS, WILLIAMS REYNOLDS (RN) (LB) (LB) (SEC) (INCH) DEV, ([DEG C) (DEG C) (PSIA) (GEM) (PSI) COZFF. NUMBER

HAND. FLUID - 1HG BAROMETER - - 75,76 CM OF MERCURY iAIR TEMPERATURE - 22,83 DEGREES CELCIUS

51 0,0 200.0 61.434 4,578 0.041 23.20 26,11 0,00 23,5 2,0841 145.3? / 83^1 ,

j

52 0.0 200.0 61,494 4,591 0,022 23.20 26.11 0.00 23,5 2,0353 145,33 70010 7

, i 53 0,0 200.0 61.521 4,578 0.027 23,20 26,11 0,00 23,5 2,0342 145.30 78784.1

54 0.0 200.0 61,521 4,577 0.029 23,20 26,11 0,00 23.5 2,0333 145.32 7070/ I , \>! v't, i 55 0,0 200,0 61.547 4.575 0,027 23.20 26.11 0,00 23,4 2,0327 145.30 78750,8

NANO, FLUID - HATER BAROMETER - - 75.77 CH OF MERCURY AIR TEMPERATURE — 2^,13 degrees CELCIUS

56 0.0 200,0 71,101 44,225 0,078 24,40 25,72 115,50 20.3 1,5858 145,72 67628,2

57 0,0 200.0 71.039 44,175 0,060 24,40 25,72 115,70 20,3 1,5540 145,84 67639.7

53 0.0 200.0 71,142 44,135 0.162 24,40 25.72 115,70 20.3 1,5326 145,80 6/5s?,s

59 0.0 200.0 71,144 44,027 0,115 24,40 25,72 115,60 20.3 1.5737 145.9? 67u8y , 4 60 0,0 200,0 71.163 44,127 0,261 24,40 25.72 116.10 20.3 1.5823 145,76 67564,6

NANO, FLUID - HATER BAROMETER -- 75,79 CM OF MERCURY AIR TEMPERATURE - 23,26 DEGREES CElCIUS

61 0.0 200.0 90.974 28,220 0,140 24.40 oc* ~n lJu l. 116,50 15,9 1,0119 145,20 528j5,

1

62 0.0 200.0 90,615 28,211 0.163 24.40 25,72 116,60 15.9 1,0116 145,30 JuOvJ^r , J 63 0,0 200.0 90,672 23.196 0.162 24,40 25.72 116.60 15,9 1,0110 145, /

j

5o'j31,

1

64 0.0 200,0 90,732 27,991 0.215 24.40 25,72 116,40 15.9 1,0037 146,23 52996,0

65 0,0 200.0 90,736 27,973 0.164 24,50 25.72 116,50 15.9 1.0030 146,23 52993.7

NANO. FLUID -- HATER BAROMETER -- 75,79 CM OF MERCURY AIR TEMPERhTURe 23.29 DEGREESi CELSIUS

66 0.0 200,0 71.026 44,662 0.202 24.40 25,72 115,70 20.3 1,6015 145,11 67699.6

67 0.0 200.0 71,046 44,562 0,275 24,40 25,72 115,70 20,3 1,5979 145.24 6763 J,

u

68 0,0 200.0 71.059 44,563 0,147 24.40 25,72 115,50 20.3 1,5981 145.20 67663,2

69 0.0 200,0 71,080 44,122 0,264 24.40 25,72 115,50 20,3 1,5822 145,95 67643.2

70 0,0 200,0 71.0/8 44,745 0,297 24.40 25,72 115.00 20.3 1,6045 144,35 L1LC.!\ 1 UJ OJ tn i

ro

ro
6

AISI PIPE FRICTION TESTS

PIPE DESIGNATION — IB

DATE JAN 9 30 OBSERVERS - HH & JH

AVE. INNER DIA. - 1.0659 inches; tat’ SEPARATION - 18 364 FEE 1

GROUP FLOWRATE DIFF. PRESS. HAZEN-UILLIAHS VELOCITY FRICTION PIPE

NO* MEAN STD. MEAN STD. KEAN STD. FACTOR REYNOLDS

( GPM

)

DEV. (PSI ) DEV. DEV. (FT/SEC) NUHBEE

1 16*1 0.00 1.016 .0060 147.16 0.44 5.79 0.0209 54744

2 24.0 0.01 2.140 .0040 146.79 0.19 8.64 0.0198 80499

3 28.1 0.01 2.899 .0023 145.74 0.0? 10.11 0.0196 94185

4 31.5 0.0? 3.606 .0162 144.85 0.09 11.31 0.0195 105630

5 28.0 0.05 2.373 .0109 145.70 0.05 10,06 0.0196 93956

6 31.4 0.13 3.593 .0295 144.78 0.06 11.28 0.0195 105361

7 23.5 0.01 2.084 .0009 145.33 0.04 8.44 0,0202 78794

S 20.3 0.01 1.583 .0026 145.82 0.10 7.29 0.0206 67602

9 15.9 0.02 1.008 .0045 145.85 0.44 5.72 0.0213 52938

10 20.3 O.Oi 1.597 .0087 145.27 0.41 7.30 0.0207 67669

1
7

AISI PIPE FRICTION TESTS

PIPE DESIGNATION - 1.25A

DA 1 L 1/11/80 OBSERVERS - Jrt JH

AVE. INNER DIA. - 1.3313 INCHES! TAP SEPARATION - 17.833 FEET

RUN TARE GROSS DIVERT NANOMETER WATER STATIC FLOW DIFF. HAZEN PIPE

NO. WT UT TIME HEIGHT STD. TEH?, TEH?. PRESS. RATE PRESS

WILLIAMS REYNOLDS (RN) (LB) (LB) (SEC) (INCH) EV. (DEG C) (DEG C) (PSIA) (GPM) (PSI) COEFF, NUMBER

HANO. FLUID - WATER BAROMETER - 75,51 CM OF MERCURY AIR TEMPERATURE - 21,92 DEGREES CELCIUS

1 0.0 200,0 52.085 19,715 0,060 24,00 26,67 123.30 27.7 0,7063 153,21 l

n

\L ~L(\ L

/ L.yjo J ¥ o

2 0.0 200.0 52,36/ 19,567 0,053 24,00 26,67 123,30 27.6 0.7015 153.01 72239.4

3 0.0 200.0 52,6^5 19,408 0,0.44 23,90 26,67 123,30 27.4 0,6958 152,90 71371,6

4 0.0 200.0 52.527 19,435 0,051 23,90 26,67 123,30 27,5 0,6963 153.10 72019.4

5 0.0 200.0 52.772 19.303 0.071 23,90 26,67 123,30 27.4 0,6922 152.93 71685.0

HAM. FLUID — WATER BAROMETER -• 75.5 CH OF MERCURY AIR TEMPERATURE - 22,04 DEGREES CtLCIUS

6 0.0 200.0 41.141 30,765 0.037 23,70 26,81 122,50 35.1 1,1030 152.50 92212.1

7 0.0 200.0 41,471 30,720 0.049 23,70 26,81 122,50 34,8 1,1014 151,40 91478.4

8 0.0 200,0 41,168 30,758 0,122 23,70 26,81 122.50. 35.1 1,1028 152.42 92151.7

9 0.0 200,0 41.191 30.745 0,040 23.65 26,81 122.50 35.0 1.1023 152.36 92100,2

10 0.0 200,0 41.193 30,715 0,056 23.70 26.81 122,50 35,0 1,1013 152.42 92034,5

HANO. FLUID - WATER BAROMETER -- 75,46 CH OF MERCURY AIR TEMPERATURE - 22,1 DEGREES CELCIUS

11 0.0 200.0 34,078 43,810 0.051 23.50 26.81 121,60 42,4 1.5709 152.03 111324.0

12 0.0 200,0 34.114 43.880 0.052 23,50 26,81 121,60 42,3 1,5734 151.78 111206,

Q

13 0.0 200,0 34,109 43,843 0.028 23.50 26,81 121,60 42.3 1,5722 151,87 111223,0

14 0.0 200.0 34.129 43,833 0,065 23.50 26, 8i 121,60 42.3 1,5719 151.80 111153,0

15 0.0 200.0 34.125 43.903 Q.033 23,50 26.81 121,60 42,3 1.5742 151.69 111171.0

HANO. FLUID - HG BAROMETER - - 75.42: CH OF MERCURY AIR TEMPERATURE - 22,13 DEGREES CELCIUS

16 0.0 200.0 30,278 4,292 0.024 21,75 26,31 121,50 47,7 1.9540 152.12 125295,0

17 0.0 200.0 30*201 4,309 0,012 21,80 26.81 121,50 47,7 1.9619 151,77 125283,0

18 0.0 200.0 30.28? 4.303 0.019 21.80 26,81 121.50 47.7 1.9616 151,74 125250,0

19 0.0 200.0 30.297 4,301 0.023 21.80 26,81 121.50 47,6 1,9531 151.85 125217.0

20 0.0 200,0 30,283 4.306 0,018 21.80 26,81 121,50 47,7 1,9607 151,81 125275,0

HANO. FLUID -- HG BAROMETER -- 75,4 CH OF MERCURY AIR TEMPERATURE - 22,2 DEGREES CELCIUS

21 0.0 200.0 26,176 5,719 0.03? 21.90 26,81 121.50 55.1 2.6038 150.66 144930,0 22 0.0 200.0 26,183 5,701 0.041 21.90 26,81 121,50 55.1 2,5956 150,83 144391,0

23 0.0 200.0 26.185 5.701 0,049 21.90 26,81 121,50 55.1 2,5956 150.87 144830.0 24 0.0 200.0 26.162 5,706 0,05? 21.95 26,81 121.50 55,2 2,5979 150,93 145303. Q

25 0.0 200,0 26.168 5,712 0,022 22,00 26.81 121,50. 55,2 2 ttiOOi) 150.81 144974.0

HANO. FLUID - HG BAROMETER -- 75.37 Cit OF

: MERCURY AIR TEMPERATURE - 22.27 DEGREES CELCIUS 26 0.0 200.0 25.995 5.7?y 0,018 22,00 26.81 121,50 55.5 2,6402 150,53 145939.

Q

27 0.0 200.0 26,071 5,797 0,020 22,00 26,81 121,50 55,4 2,6393 150.17 145514.0 23 0.0 200.0 26,005 5,797 0.016 22,05 26,81 121,50 55,5 2,6393 150.55 145883.0

29 0.0 200,0 26,029 5,809 0.020 22,05 26.81 121,50 55.5 2.6447 150,24 145743.0

30 0.0 200.0 26,027 5, SO6 0.016 22,05 26,81 121,50 55,5 2,6434 150.2? 145760.

Q
8

AISI PIPE FRICTION TESTS PIPE DESIGNATION - 1.25A DATE 1/11/80 OBSERVERS - JrS JH Mi, INNER BIAi - 1,3313 INCHES! TAP SEPARATION - 17,833 FEET

RON TARE GROSS DIVERT HA,MASTER WATER STATIC FLOW DIFF. HAZEN PIPE.

NO, UT WT TIME HEIGHT STD, TEH?. TEMP. PRESS, RATE PRESS, WILLIAMS REYNOLDS (RN) 06 ) (LB) (SEC) (INCH) DEV, i(DEG C) (DEG C) (PSIA) (GPH) (PSI) COEFF. (UNDER

HAM. FLUID - HG BAROMETER - - 75,35 CH OF MERCURY AIR TEMPERATURE -- 22,33 DEGREES CELCIUS

31 0,0 200,0 30.210 4.351 0,024 22,10 26,94 121,50 47,8 1,9810 151,34 1259 L 3,0 32 0,0 200,0 30,187 4,362 0.014 22,10 26,94 121.50 47.8 1,9859 151,25 126004,0

33 0.0 200,0 30,132 4,349 0,021 22,20 26,94 121,50. 47,8 1.9800 151.52 iz60zj i

34 0.0 200.0 30,230 4,362 0.015 22.20 26,94 121,50 47,7 1.9860 151.03 125324,0

35 0,0 200,0 30,209 4,352 0,016 22,20 26.94 121,50 47.8 1.9814 151.33 125912.0

NANO, FLUID - WATER BAROMETER - - 75,29 CH OF MERCURY AIR TEMPERATURE - 22,46 DEGREES CELCIUS

36 0.0 200,0 34,563 43,368 0,030. 24.25 27,08 121,50 41,8 1,5543 150.79 » 0 37 0,0 200,0 34,559 43,460 0,033 24,25 27,08 121,50 41.8 1,5581 150,64 li'Ju/ j» Q 38 0.0 200,0 34,570 43.475 0.067 24,20 27,03 121,50 41,8 1,5536 150,56 110340.0

3? 0.0 200.0 34.573 43,465 0.044 24,20 27,03 121,50 41,8 1,5583 150,56 510330,0

40 0.0 200.0 34,538 43.478 0,028 24,20 27,03 121,50 41.7 1,5587 150,48 110282.0

HAM, FLUID -- WATER BAROMETER - - 75,26 CH OF MERCURY AIR TEMPERATURE - 22,5 Dl.Gi\uLS CELCIUS

41 0.0 200,0 42.250 29,898 0,066 24,20 27.03 122.50 34.2 1.0/18 150.83 90232.5

42 0,0 200.0 42,307 29,770 0.073 24,05 27.03 122,50 34,1 1,0673 150,97 90160,9

43 0,0 200,0 42,333 29,818 0.043 24,10 27,03 122,53 34,1 1,0690 150,73 90094,9 44 0,0 200,0 42.347 29,833 0,053 24,10 27,03 122,50 34,1 1,0695 150,66 90075,7 45 0,0 200.0 42.342 29,850 0,095 24. IQ 27,03 122,60 34,1 1 ,0/01 150,63 90036,3

HAM. FLUID — WATER BAROMETER -- 75.22 CH OF MERCURY AIR TEHPEKbTURE - 22,53 DEGREES CELCIUS

46 0,0 200.0 53,075 19,644 0.045 24.00 27,03 123,40 27.2 0.7042 150,67 71363.7

47 0.0 200.0 53,096 19,632 0.065 24,10 27.06 123,30 07 0

L.I S L. 0,7038 150,66 71311,3

48 0,0 200,0 53,053 19.746 0,056 24,00 27,03 123,30 27,2 0,70/9 150.29 71391,8

49 0,0 200,0 53.055 19,658 0.0/5 24,00 27,08 123,30 27.2 0,7047 150,66 71895.8

50 0,0 200.0 53,064 19,710 0,054 24,00 27.03 123,40 07 0

4./ 0,7066 150.42 71383,6

HANG. FLUID - HG BAROMETER -- 74,93 CH OF MERCURY AIR TEMPERATURE — 23,24 DEGREES CELCIUS

51 119,5 1124,0 132,111 5,665 0.015 22,50 26.20 114,00 54,9 2,5793 150,67 142430,0

52 120.4 1123.0 131.746 5,695 0,000 22,70 26,25 114,00 54,9 2,5927 .150,38 142719,0

53 119,2 1123,0 132,030 5,697 0,012 22.80 26,25 114.00 54,8 2,593a 150,15 142529.0

54 120,4 1125.0 132,295 5,719 0.024 22.90 23.29 114.00 54.8 2,6035 149.61 133958.0 55 120.5 1123,0 132,135 5.736 0.013 23, QO 26,23 114.00 54.7 2,6114 149,34 142372,0
9

AISI PIPE FRICTION TESTS

PIPE DESIGNATION — 1.25A

DATE 1/1 1/80 OBSERVERS - JH JH

AVE. INNER DIA. - 1.3813 INCHES i TAP SEPARATION - 17 .833 FEET

GROUP FLOURATE DIFF. PRESS. HAZEN-UILLIAKS VELOCITY FRICTION PIPE

NO. KEAN STD. KEAN STD. KEAN STD. FACTOR REYNOLDS

( GPU

)

DEV. (PSI ) DEV. DEV. (FT/SEC) NUMBER

1 27.5 0.14 0.699 .0056 153.03 0.13 5.89 0.0137 72039

2 35.0 0.11 1.102 .0008 152.22 0.46 7.49 0.0182 92005

3 42.3 0.02 1.573 .0013 151.84 0.14 9.06 6.0178 111216

4 47.7 0.01 1.959 .0033 151.86 0.15 10.20 0.0174 125264

tj 55.1 0.02 2.599 .0035 150.83 0.10 11.81 0.0173 144937

6 55.5 0.06 2.641 .0025 150.36 0.19 11.87 0.0174 145769

7 47.8 0.03 1.983 .0029 151.29 0.18 10.23 0.0176 125934

8 41.3 0.01 1.553 .0017 150.60 0.12 8.94 0.0181 110333

9 34.1 0.03 1.070 .0017 150.76 0.14 7.30 0.0186 90140

10 27.2 0.01 0.705 .0017 150.54 0.17 5.82 0.0193 71370

11 54.8 0.07 2.596 .0121 150.03 0.55 11.74 0.0175 140305
10

AISI PIPE FRICTION TESTS

PIPE DESIGNATION ~ 1.258 DATE l/li/30 OBSERVERS - JH 4 Jll AV£. JhNER DIA. - 1,3892 IO£S> TAP SEPARATION - 17,572 FEET

RUN TARE GROSS DIVERT MANOMETER: WATER STATIC FLOW BIFF. HAZEN PIPE

NO. BT WT TIKE HEIGHT STD. TEMP, TEMP, Press » RATE PRESS, WILLIAMS RtiNOiDS

(RN) (LB) ( LB > (SEC) (INCH) DEV. (DEG C) (DEG C) (PSIA) (GPM) (PSD CUEFF, NUMBER

HANO, FLUID -- WATER BAROMETER - 75,71 CH OF MERCURY AIR TEMPERATURE -- 20,09 DEGREES CELSIUS

1 0.0 200,0 54,557 19.112 0,274 21,70 25,83 112,00

c-

* J 0,6859 145, 26 67777,8

0

L 0.0 200,0 54,60/ 18.946 0.084 21,70 25,83 112,00 26.4 0.6799 145,81 67715,7

3 0.0 200,0 54,663 19,048 0,163 21,65 25,33 112,20 26,4 0,6836 145,24 67646,3

4 0,0 200.0 54,657 13,938 0.061 21,70 25,83 112,20 26,4 0,6796 145,71 67653.7

5 0,0 200.0 54 , 650 18,990 0.066 21,65 25,83 112,20 2&»4 0,6815 145,51 67662,4

HANO. FLUID - WATER BAROMETER -- 75,71 CH OF MERCURY AIR TEMPERATURE - 20,17 DEGREES CELCIUS

6 0,0 200.0 42,603 30,650 0,061 21,55 25,83 121.70 33,9 1,0995 144.13 86795.5

7 0.0 200,0 42,617 30,593 0.133 21.45 25.83 121,70 33,9 1,0975 144.23 36767,0

8 0,0 200,0 42.616 30.515 0.009 21,45 25,83 121,70 33,9 1.094/ 144,43 86769,0

9 0,0 200,0 42,627 30.523 0.0/2 21.40 25,83 121,70 33.9 1,0950 144.37 86746,6

10 0.0 200.0 42,673 30.485 0.040 21,40 25,83 121.70 33,8 1,0936 144,31 85653,

1

HANO* FLUID - lHATER BAROMETER -- 75.7 CM OF MERCURY AIR TEMPERATURE - 20,24 DEGREES CELCIUS

11 0,0 200.0 35.550 43.460 0.022 21,40 25,83 120,80. 40.6 1.5591 143,01 104015,0

12 0,0 200,0 35.632 43,240 0,062 21.40 25.83 120.8-0 40.5 1.5512 143,07 103782.0

13 0.0 200.0 35,694 43,173 0.033 21.40 25,83 120,80. 40.4 1,5490 142.94 103j?u*

0

14 0,0 200.0 35.726 43,168 0.042 21.40 25.83 120,80. 40,4 1,5486 142,83 10350.3,0 15 0,0 200.0 35.723 43,188 0.139 21.40 25,33 120,80 40.4 1.5494 142,80 103512.0

HANO. FLUID -- HS BAROMETER -- 75.69 CH OF MERCURY AIR TEMPERATURE - 20,33 DEGREES CELCIUS

16 0,0 200,0 31,804 4,204 0,018 20.20 25,83 121,00 45,4 1,9144 143. 07 116267,0

17 0.0 200,0 31,632 4,199 0,015 20.20 25,83 121,00 45,6 1,9121 143,94 116899,0

18 0.0 200.0 31,826 4.193 0.015 20,20 25,83 121,00 45.3 1.9113 143,07 li 6186,0

19 0.0 200.0 31,841 4.201 0.010 20.15 25,83 121,00 45,3 1,9129 142.96 116132,0. 20 0,0 200,0 31,868 4,185 0.019 20,10 25.83 121,00 45.3 1.9057 143.13 116033,0

HANO. FLUID - HG BAROMETER - - 75.71 CH OF MERCURY AIR TEMPERATURE - 20.09 DEGRE.ES CELCIUS

21 0.0 200.0 27,340 5.695 0.021 20.05 25.83 121.00 52,8 2,5933 141.24 135251,0

22 0,0 200,0 27.341 5.690 0,031 20.10 25,83 121.00 52,8 2,5910 141.30 135246.0 23 0,0 200,0 27.354 5.674 0,034 20.00 25.83 121.00 52,8 2,5838 141.45 135181.0

24 0.0 200,0 27,346 5,673 0,026 20,10 25,83 121,00 52.8 2,5333 141,51 135221.0 25 0,0 200,0 27,341 5,696 0.024 20.10 25.83 121,00 52,8 2,5933 141,22 135246,0

HANG, FLUID -- HG BAROMETER -“ 75.65 CH OF HERCUxY AIR TEMPERATURE -• 20,98 DEGREES CELCIUS

26 0,0 200,0 27,059 5,800 0.035 20,40 26,67 121,00 53.3 2.6410 141,34 139010.0

27 0.0 200,0 27,053 5,803 0,014 20,40 26,67 121,00 53.3 2.6+24 141.31 139015.0

28 0.0 200,0 27,024 5,821 0.026 20,40 26,67 121,00 53,4 2,6506 141.25 139190,0 29 0,0 200.0 27,0/1 5.821 0,036 20.40 26,67 121,00 53.3 2,6506 141,00 138948,

Q

30 0.0 200,0 27.084 5,316 0,024 20,40 26,67 121.00 53,3 2,6431 141,01 138382.0
11

AISI PIPE FRICTION TF.5TS PIPE fir SI GNAT ION - 1,258 DATE 1/11/80 OBSERVERS - JM i JH

AVE, INNER DIA. - 1,3892 INCHES! TAP SEPARATION - 17,572 FEET

RON TAPE GROSS DIVERT HANOftE TER WATER STATIC FLOW BIFF, HAZEM PIPE

NO, UT UT TIKE HEIGHT STD. TEMP. TEN?. PRESS, RATE PRESS. WILLIAMS REYNOLDS (RN) (LB) (LB) (SEC.) (INCH) DEV. (DEG C) (DEC C) ( F'SIA

)

(GPM) (PSD CliEFF, NJrii>c.K

NANO. FLUID - 1US BAROMETER - 75,65 CM OF MERCURY AIR TEMPERATURE ~ 21.12 DEGREES CLLCIU3

31 0,0 200,0 31.572 4.287 0,017 20.50 26,67 121,00 45.7 1,951? 142,64 119139,0.

32 0.0 200,0 31.566 4.273 0,020 20,50 26,67 121.00 45.7 1,9455 142,93 119162.0 33 0.0 200,0 31.575 4,286 0,016 20,50 26.67 121.00 45.7 1.9515 142.65 119128,0. 34 0.0 200.0 31,554 4.2V3 0.010 20,60 26,67 121.00 45.7 1,954? 142.61 119207,0

35 0.0 200.0 31.534 4,285 0,016 20,60 26,67 121,0-0 45.7 1.9’jll 142.62 119094,0

NANO. FLUID - WATER BAROMETER - 75,64 CM OF MERCURY AIR TEMPERATURE - 20,23 Dil'REto CELCIUS

36 0,0 200.0 35.532 43,725 0,018 21,90 26.67 120,80. 40.6 1,5685 142,65 10.5862,0 37 0.0 200.0 35.546 43.630 Q.054 21,90 26,67 120,80 40,6 1,5651 142,77 105320,0

38 0.0 200,0 35.530 43.690 0.052 21.95 26.67 120,80 40,6 1,5672 142,72 105363,0

39 0,0 200.0 35.546 43.595 0.063 22.00 26,67 120,80 40,6 1,5633 142,83 105320,0 40 0.0 200,0 35.559 43.690 0,067 22.00 26,67 120.30 40.6 1,5672 142,6!. 105/32.0

NANO, FLUID -- WATER BAROMETER - 75.63 CN OF MERCURY AIR TEMPERATURE ~ 21.36 DEGREES CELCIUS

41 0,0 200.0 42,638 30.698 0,051 22,20 26.67 121.70 33,9 1,1010 143,94 83213,6

42 0.0 200,0 42.693 30,673 0.027 22.30 26,67 121,70 33,8 1,1001 143,82 8310.5,0

43 0.0 200.0 42.565 30,915 0.097 22.30 26.67 121.70 33,9 1,1 OSS 143,64 8u3o9 ,

9

44 0,0 200,0 42.533 30.920 0,059 22.30 26.67 121.70 33,9 1,1090 143.71 83426,0

45 0.0 200.0 42.554 30,943 0,056 22,40 26,67 121,70 33,9 1,1093 143,61 83392.8

NANO. FLUID - WATER BAROMETER - 75.61 CN OF MERCURY AIR TEMPERATURE - 21.46 DEGREES; CELCIUS

46 0.0 200.0 53,862 19,784 Q.037 22.45 26.67 122,60 26,8 0,7095 144.4? 69335,2

47 0.0 200,0 53,859 19,733 0.0/6 22,45 26.67 122,60 26.3 0,70/9 144.63 69339.1 48 0.0 200.0 53,883 19,736 Q.058 22,55 26.67 122,60 26,8 0,7078 144,62 69303,0

49 0,0 200,0 53»8b9 19,764 0.036 22.55 26,67 122,60 26.3 0.7038 144.50 69300.2

50 0,0 200.0 53,373 19.810 0.0/4 22.60 26.67 122,60 26,8 0,7104 144,36 69320.9
12

AISI PIPE FRICTION TESTS

PIPE DESIGNATION — 1.25B

DATE 1/1 i/80 OBSERVERS - JM & JH

AVE. INNER DIA. - 1.3892 inches; TAP SEPARATION - 17 .572 FEET

GROUP FLOURATE DIFF. PRESS. HAZEN-UILLIAHS VELOCITY FRICTION PIPE

NO* MEAN STD. MEAN STD. MEAN STD. FACTOR REYNOLDS

< GPM

)

DEV. (PSI) DEV. DEV. ( FT/SEC

)

NUMBER

1 26.4 0.02 0.682 .0026 145.51 0.26 5.59 0.0206 67691

2 33*9 0.02 1.096 .0024 144.30 0.12 7.17 0.0202 86746

3 40.5 0.08 1.551 .0044 142.93 0.12 8.56 0.0200 103682

4 45.4 0.13 1.911 .0033 143.23 0.40 9.61 0.0196 116303

5 52.8 0.01 2.589 .0051 141.35 0.13 11.17 0.0196 135229

6 53.3 0.04 2.647 .0046 141.18 0.16 11.29 0.0196 139009

7 45.7 0.02 1.951 .0034 142.69 0.13 9.63 0.0197 119146

8 40.6 0.01 1.566 .0019 142.72 0.09 8.60 0.0201 105330

9 33.9 0.05 1.106 .0047 143.74 0.14 7.17 0.0203 83302

10 26.8 0.01 0.709 .0011 144.53 0.13 5.67 0.020? 69821
13

AISI Fill FRICTION TESTS

PIPt nKSIGMATIOf4 - 1.58 BATE JAN 4 30 OBSERVERS - jh 6 m

AVE. INNER DIA, - 1,6233 INCHES

TAP SEPARATION - 17,177 FEET m TARE CROSS DIVERT MANOMETER WATER STATIC FLOW DIFF, HA7.EN PIPE

NO, WT WT TINE HEIGH r SID, TEN?. TEN?, PkESS, RATE PRESS, WILLIriHS REYNOLDS (RN) (LB) (LB) (SEC) (INCH) DEO. (DEG C) (DEG C) (PS1A) (GPU) (PSD C-liEFF

NUMBER

NANO, FLUID - HATER BAROMETER - 75,75 CN OF MERCURY AIR 1EMFEkAiUre — 21.43 DEGREES CELCIUS

1 120,3 920,3 97,498 35,423 0,044 22,50 24,97 120,80 59,2 1.2705 152.53 127517.0

2 120,3 919.3 97,503 35,379 0.047 22,60 25,00 120,80 59,1 1,263? 152.49 127429,0

3 120,5 918.8 97.460 3..*,3i4 0,062 22 , !ij 25,00 121.20 59.1 1.2672 152,53 127374.0

4 120,8 918.2 97,460 35,306 0,059 22,60 25.03 120,90 59,0 1,2663 152.42 127309,0

5 120.5 919,8 97,672 35,280 0,03? 22,70 25,07 12.1,00 59,0 1,2653 152,52 127440,0

NANO. FLUID -- WATER BARONE TER - 75,74 CN OF MERCURY AIR TEMPERATURE - 21,75 DECREES CELCIUS

6 120,0 916.0 83.676 46.796 0,276 22,65 25,11 121,10 63,6 1,6783 152.1? l422o4*0

7 120.1 922,7 84.562 46,714 0.105 22,60 25.13 121.40 63.5 1,6754 151.99 147983,0

8 119,5 921,1 84,124 47,137 0.276 22,70 25,17 121,60 63.7 1,6905 151,85 148696,0

9 120.2 924.0 84,167 47,286 0,06? 22,75 25,16 121,60. 68.9 1,6958 151.93 148997,0

10 119.8 921.7 84,350 46,908 0,065 22,80 25.1? 121,70 63,6 1.6823 151.90 148414,0

NANO, FLUID -- HATER BARONE fER -- 75.67 CN OF MERCURY AIR TEMPERATURE - 2i»96 Decrees celcius

11 120,4 921.8 76,020 57,002 0,076 22.80 25,23 120.60 76.1 2,0443 151,60 164709,0

12 120,2 920.8 75.951 57,100 0.052 22.80 25,25 120,70 76,0 2,0478 151,44 164762,0

13 120.5 921.8 76,0/5 57,093 0.03? 22,90 25,26 121.30 76,0. 2,0475 151,34 164671 ,0 14 120.0 922.0 76.442 56,442 0.162 23,00 25,25 120,90 75.7 2,0241 151,6? 163990,0

15 120.3 922.2 76,737 56,257 0,059 23,0-0 25,31 120,90 75,4 2,0175 151,35 163540 »Q

NANO, FLUID - WATER BARONE FER - 75.4 ch & MERCURY AIR TEMPERATURE - 22,35 DEGREES CELCIUS

16 119,4 922.6 76.399 56,738 0,244 23.15 25.27 120,90 75,8 2,0347 151,57 164394.

C

17 120,7 922,1 75,896 57,333 0,108 23,20 25.34 119,40 76,2 2,0561 151.33 16536), 0 18 120.4 921,1 75,849 57,305 0,019 23,20 25,33 119,50. 76.2 2.0551 151,33 165444,0

19 120,6 921,3 75,933 57,193 0.079 23.20 25,40 119,50 76.1 2,0511 151,36 165313,0

20 120.6 922.5 76,018 57,137 Q.034 23,40 25,42 119,40 76,1 2,050.8 151.44 It) 645? , 0

NANO, FLUID -- WATER BAROMETER -- 75,41 CN OF MERCURY AIR TEN?'EKhTUaE — 22.52 DEGREES CF.lf.IUS 21 120.6 918.8 84,816 46,147 0,063 23,40 25.43 118,40 67,9 1.6517) 151.72 14/794,0

0*

C.A. 120.2 922,3 85.256 46,117 0,034 23,40 25,49 113,40 67,9 1 ,655? 151.72 147/30,0

23 121.0 920.4 84.349 46,820 0,094 23,40 25,51 117.70 68,4 1,6791 151,5? 148927,0

24 120.2 920.1 84,641 46,553 0.208 23,45 25,52 122.20 63.2 1.6692 151,65 148536,0 25 120.3 918,6 84,578 46.464 0,105 23,50 25,60 117,40 63,1 1,6664 151,60 143593.0

NANO. FLUID - WATER BARONE CER - 75,4 CN OF MERCURY AIR Ttr^LKAT UR£ - 22,7 degrees celcius

26 120,2 920,3 94,710 37.783 0,07/ 23,60. 25.61 117,80 61.

Q

1.3550 151,34 133106,0

27 120.4 920.2 94,945 37.553 0,0.66 23.60 25,63 118,00 60,3 1,3467 151,81 132693.0 28 120,1 920,1 93.435 33.447 0,347 23,60 25.65 121.30 61,8 1,3786 152,37 134932,0 29 120.0 920.2 94.345 33.817 0,110 23.75 25,63 121,30 61.2 1,3913 150,16 133746.0

30 120.0 920,5 93,410 33,380 0,052 23.80 25,63 12.1,30 61.8 1,3940 151,59 135135,0
14

AISI PIPE FRICTION TESTS PIPE DESIGNATION - 1.5B DATE JAN 4 80 OBSERVERS - JH i fill AVE, INNER DIA, - 1,6233 INCHES! TAP SEPARATION - 17,177 FEET

RUN TARE GROSS DIVERT MANOMETER HATER STATIC FLOW BIFF. HAZEN PIPE

NO, WT UT TIKE HEIGHT STD, TEMP. TEMP. press. RATE PRESS

,

WILLIAMS REYNOLDS (RN) (LB) (LB) (SEC) (INCH) DEV. (DEG C) (DEG C) (PSiA) (GPU) (PSD CUEFF. NUMBER

NANO. FLUID - HSC- BAROMETER -* 74,84 CH OF MERCURY AIR TEMPERATURE - 20,3 DEGREES CF1CIU3

31 121.7 1118.0 94. 948 4,557 0.026 20.35 24,38 120,00 75,7

' 2,0748 149,66 - 161091,0

32 120.8 1119.0 95,226 4,556 0,025 20,45 24,39 120,00 75,6 2,0746 149.52 160961.0

33 120.7 1117,0 95,195 4,555 0.027 20.40 24,41 120,00 75,5 2,0741 149.30 1607/3,0

34 117,1 1114,0 95,2.30 4,568 0,040 20,50 24,45 120,00 75,5 2,0798 149,11 160945,0

35 114.2 1111.0 95.171 4,553 0,031 20.70 24.46 120.00 75,5 2,0754 149.36 161Gs2.0

HAND. FLUID - HG BAROMETER -- 74,81 CH OF MERCURY AJR TEMPERATURE - 20 ,59 ltr.Gr.Ecii CELCIUS

36 113,9 1315,0 82.910 8,398 0,039 20,90 24,53 120,00 104,1 3,8239 14/ ,8s 222167.0

37 120.7 1336.0 83.442 8,560 0.028 20,95 24,56 120.00 104.9 3,8976 147,57 224163.0

33 122,8 1322,0 82,131 8,613 0.027 20,95 24,55 120,00 105.3 3,9213 147.62 224943,0

39 120.9 1327.0 82,873 8,561 0,020 21.05 24,60 120,00 105,0 3,8978 147,63 224449.0

40 121,0 1325.0 85,527 8,603 G.020 21,05 24.63 120,00 101,5 3,9172 142,42 217240,0

HANO. FLUID -- HG BAROMETER -- 74.62 CH OF MERCURY iAIR TEMPERATURE -- 21.27 DEGREES CELCIUS

41 116.0 1313,0 86,539 7,836 0,194 21,60 24,60 120.00 103.2 3,5677 147,30 214209,0

42 116,6 1326.0 87.671 7,742 0,020 21.60 24.64 120,00 99,5 3,5250 147,75 212921,0

43 118.6 1321.0 87.089 7,770 0,017 21.60 24,63 120.00 9V.

6

3,53/ 5 147,59 21 32.60,0 44 118.3 1321.0 87,165 7,777 0.022 21,70 24,69 120,0) 99,5 3,5407 147.43 213191,0

45 121,7 1320,0 36,952 7,756 0.020 21,70 24,76 120.00 99.4 3,5313 147.46 213240,0

HANO, FLUID - HG BAROMETER -- 21,42 CH OF HERCURY AIR TEMPERATURE - 21.42 DEGREESI CELCIUS 46 118.6 1118,0 93,824 4,736 0.016 21.70 24,75 120,00 76.8 2.1563 148,63 164647,0

47 118.5 1117,0 93.787 4,739 0.017 21.75 24,80 120,00 76.7 2.1575 148,56 164733,0 43 119.5 1118.0 93.765 4.734 0,019 21,80 24,82 120,00 76,7 2,1555 148,67 i64340,0

49 118.4 1119,0 94.247 4,697 0.027 21.80 24,84 120,00 76,5 2.1383 148,37 164410.0

50 118.0 1117,0 94,134 4.712 0.013 21,80 24,81 120.00 76.5 2,1454 148,54 164242,0

HANO. FLUID - WATER BAROMETER -- 75,66 CM OF HERCURY AIR TEMPERATURE -- 21,83 DEGREES CELClUS

51 0.0 200.0 30.777 24,128 0.03a 22.40 25,28 120.00 46,9 0,8654 148,72 lOlOiii , 0. 52 0,0 200.0 31,047 23,920 0.234 22,60 25,28 120,20 46,5 0,3579 143,12 100/52,0

53 0,0 200.0 31,417 23,183 0.032 22.60 25.28 120,20 45.9 0,8315 143.83 99565,1

54 0.0 200,0 30.752 24,148 Q.028 22.60 25,28 120.20 46,9 0,8661 148,78 101718.0

55 0.0 200,0 30,795 24,058 0.040 22.70 25,28 120.20 46,9 0,8628 148,83 101576,0

HANO. FLUID - WATER BAROMETER -- 75,66 CH OF HERCURY AIR TEMPERATURE -- 2i,8l DEGREES CelCIUS

56 0,0 200.0 39.526 15,045 0,049 22.80 25.28 121,20 36,5 0,5396 149.50 79)33,3

57 0,0 200,0 39.654 14.888 0,035 22,80. 25,28 121,20 36,4 0,5339 149.36 78833,

3

53 0,0 200,0 39,586 14,900 0,034 22.85 25,28 121.10 36.4 0.5344 150,05 79018,8

59 0,0 200,0 39,59V 14,892 Q.1Q1 22.90 25.28 121,20 36.4 Q.5341 150,05 78992.9

60 0,0 200.0 39,621 14.883 Q.034 22.90 25.28 121,20 36,4 0,5339 149,9? 78949.0
15

ftlSI PIPE FRICTION TESTS PIPE DESIGNATIN'! - 1 ,jB DATE JAN 4 30 OBSERVERS - JH L KH

AVE. INNER BIft, - 1,6233 INCHES* TAP SEPARATES - 17,177 FEET

RUN TAPE GROSS DIVERT HANCKteTER HATER STATIC FLOU DIFF, HAZEM PIPE

NO, HT UT TIKE HEIGH! STD. TEMP. TEMP. Press. RATE PRESS, WILLIAMS REYNOLDS (RN) (LB) (LB) (SEC) (INCH) DEV. (DEG C) (DEG C) (PSIA) <GP«) (PSD CUEFF, NUMBER

NANO. FLUID - HATER BAROMETER -- 75,59 CK OF MERCURY AIR TEMPERATURE. - 22,33 DEGREES CELCIUS

61 0,0 200.0 39.272 15,163 0.074 23.20 25,28 121,70 36.7 0,543/ 149,84 79650,3

62 0.0 200.0 39,266 15,150 0,119 23,25 25.28 121,70 36,7 0.5433 149,93 79662,5

63 0,0 200,0 39.253 15.252 0,054 23.30 25.28 121,70 36.8 0,5469 149,44 79688,9

64 0,0 200,0 39.271 15.226 0.103 23.35 25,28 121.70 36,7 0.5460 149,51 79652,3

65 0,0 200.0 39.272 15.236 0.090 23.40 25,28 121.70 36,7 0,5463 149.45 / Vuj’J, 3

NANO. FLUID - HATER BAROMETER --- 75,59 CH OF MERCURY AIR TEMPERATURE - 22.37 DEGREES CELCIUS

66 0.0 200.0 30.675 24,255 0,086 23.45 25,23 120,60 47,0 0.8698 143,81 101973,0

67 0,0 200.0 30.665 24.260 0.059 23.45 25,28 120.60. 47.1 0.8699 148.85 102006,0

63 0.0 200.0 30.683 24,245 0.057 23,55 25.28 120,60 47,0 0.8694 148,81 101947.0

6? 0.0 200.0 30.667 24,213 0.062 23,55 25,28 120,60 47,0 0,8682 149.00 102000.0

70 0.0 200,0 30.677 24,258 0,043 23,55 25,28 120.60 47,0 0,8698 143.30 101967.0

AISI PIPE FRICTION TESTS

PIPE DESIGNATION ~ 1.5B

DATE JAN 4 SO OBSERVERS - JH 6 HH

AVE. INNER DI A. - 1.6238 INCHES? TAP SEPARATION - 17.177 FEET

GROUP FLOtiRATE DIFF. PRESS, HAZEN-UILLIAliS VELOCITY FRICTION PIPE

NO. MEAN STD. MEAN STD. MEAN STD. FACTOR REYNOLDS

( GPU

DEV. (PSI ) DEV, DEV. (FT/SEC) NUMBER

1 59.1 0.07 1.268 .0021 152.51 0.06 9.15 0.0172 127414

2 68.7 0.16 1.684 , 0035 151.97 0.13 10.64 0.0169 148472

3 75.8 0.29 2.036 .0144 151.48 0.15 11,75 0,0167 164334

4 76.1 0.13 2,050 .0086 151,43 0.09 11.79 0.0168 165193

5 68.1 0.21 1,665 .0105 151.66 0.06 10.55 0.0170 148326

6 61.3 0.47 1.373 .0215 151,55 0.33 9.50 0.0173 133924

7 75.6 0,03 2.076 .0023 149,39 0.21 11,71 0.0172 160966

8 104.2 1.54 3,892 .0395 146.62 2.35 16,14 0.0170 222594

9 99.6 0.31 3.540 .0164 147.60 0.16 15.44 0.0169 213368

10 76.6 0.14 2.151 .0034 148.66 0.13 11.88 0.0173 164574

11 46.6 0.42 0.857 ,0145 148.68 0.32 7,22 0,0186 101049

12 36.4 0.04 0.535 ,0025 149.89 0.23 5.65 0,0191 78997

13 36.7 0.01 0.545 .0016 149.63 0.23 5.69 0.0191 79661

14 47.0 0.01 0.869 ,0007 148.35 0,03 7.29 0.0136 101979
16

AISI PIPE FRICTION TESTS

PIPE DESIGNATION - 2A DATE 12/20-31/7 OBSERVERS - JH VS

AVE. INNER DIA, - 2.0565 INCHES} TAP SEPARATION - 16,305 FEET

RUN TARE GROSS DIVERT MANOMETER WATER STATIC FLO* DIFF, HAZEN PIPE

NO, HT UT TIHE HEIGHT STD, TEMP, TEMP. PRESS. RATE PRESS

,

WILLIAMS REYNOLDS (RN) (LB) (LB) (SEC) (INCH) DEV. (DEG C) (BEG C) (PSIA) (GPU) (PSD CGSFF. NUMBER

HANO. FLUID - WATtR BAROMETER - 75,82 CK OF HEKCURY AIR TEMPERATURE - 21 DEGREES CELCIUS

1 121,1 915,7 92.728 11,479 0,115 23.15 24,46 122,40 61.8 0,4116 151.41 103545,0

2 121,0 914,9 92.530 11,481 0.065 23.00 24.53 122,20 61,9 0,4117 151,5? 103826.0

3 120,9 916,5 92.659 11,551 0.054 22.90 24,54 122,30 61,9 0,4142 151,20 103925.0

4 120,9 915,0 92.529 11,553 0.074 22,80 24,60 122,30 61,9 0.4145 151,03 104004,0

5 121,0 915,1 92,525 11,533 0,060 22, 8Q 24.63 122.40 61.9 0.4155 150.83 104073,0

HANO. FLUID - HATER BAROMETER -- 75.81 CK OF HERCURY AIR TEMPERATURE - 21.36 DEGREES CELCIUS

6 120,9 1113.0 94,960 16.974 0.049 22,90 24.70 121.10 75.4 0,6087 149.42 126871.0

7 121.2 1112,0 94.707 17.029 0,05? 22.90 24,65 121,00 75.5 0,610/ 149.36 126912,0

8 121,1 1111,0 94,605 17.0/0 0,051 22,90 24,75 121.10 75,5 0,6122 149.20 127196.0

9 120.5 1119,0 94.653 17.416 0.109 22,90 24,79 121,30 76.1 0,6246 143.7? 123336.0

10 120,9 1117.0 94.594 17,360 0.041 23,00 24,82 121,30 76,0 0,6226 143.7? 128193.0

HANO. FLUID - 1MTER BAROMETER -- 75.82 CK OF HERCURY iAIR TEMPERATURE - 21.67 DEGREES CELCIUS

11 120,4 1121.

Q

SO. 711 23,850 0.035 22.85 24,85 120.00 89.4 0,8554 147.53 151016.0

12 121.1 1115,0 80,46? 23,745 0,023 23,03 24.83 120.20 89.1 0,5516 147.34 150549.0

13 120.9 1316,0 96.812 23,784 0,05? 23.10 24,91 120.50 89.0 0,852? 147.13 150559.0

14 120,9 1314,0 96,815 23,776 0.037 23.05 24,94 120.60 88,9 0,8527 146.91 150396,0

15 121.0 1313,0 96,669 23,8v>0 0,046 23.20 24,95 120.40 83.9 0,8557 146.72 150515.0

HANO, FLUID - HATER BAROMETER -- 75.8 CK OF MERCURY AIR TEMPERAiUi\£ 21,95 DEGREES CELCIUS

16 121,1 1518.0 95.851 32,947 0,057 23.15 24.98 119,20 105.1 1.1816 145.65 178003.0

17 120,9 1513.0 95,516 33,011 0,063 23.25 25,02 119,40 105,1 1.1839 145.51 178160,0

18 121,0 1517,0 95,556 33,294 0,054 23.40 25,06 119,30 105,4 1.1940 145,1? 178732,0

19 120.7 1514.0 95.594 33,196 0.073 23.40 25,06 119.60 105.1 1,1904 145,03 178315.0

20 121.0 1516.0 95.49i 33.367 0.036 23.40 25,11 119,40 105.4 1.1966 145.01 173909,0

HANG. FLUID - HATER BAROMETER -- 75.68 CK OF HERCURY AIR TEMPERATURE - 23,02 DEGREES CELCIUS

21 120,7 1720,0 96,512 42,754 0,032 23,60 25,13 120,50 119,5 1,5331 143.87 203023,0

22 120.9 1720.0 96,674 42,716 0.049 23,75 25,15 120,30 119,3 1,5317 143.68 202741,0

23 120,8 1717.0 96,454 42,363 0,055 23.30 25,1? 120.30 119.4 1,536? 143.48 203002.0

24 120.9 1714.0 96.421 42,866 0.031 23.85 25,21 119,80 119,2 1,5370 143.25 202761,0

25 121,1 1719,0 96,485 43,146 0.166 23.85 25.24 120.80 119,5 1,54/0 143.03 203362,0

HANO. FLUID -- HATER BAROMETER - 75.67 CK OF MERCURY AIR TEMPERATURE - 23.12 DEGREES CELCIUS

26 120,9 1922,0 95,924 55,624 0,067 23.90 25,30 121.20 135,5 1,9944 141.42 230361,0

27 120.8 1930,0 96,501 55,599 0,065 23,35 25,31 121,70 135.3 1,9934 141,24 230547,0

28 121,2 1922.0 95,913 55,891 0.05? 23,85 25.33 121,40 135.4 2,003? 141.03 23096a,

0

29 120,9 1918.0 96,87? 55,883 0.055 23,90 25.33 122,30 133.8 2,0037 139.36 228440,0

30 121.1 1911.0 95.891 55,54? 0,047 23.85 25,40 121.70 134,7 1,9916 140,6? 227963,0
17

AISI PIPE FRICTION TESTS

PIPE DESIGNATION - 2A DATE 12/28-31/7 OBSERVERS - JH VB

AVE. INNER DIA, - 2,0665 INCHES. TAP SEPARATION - 16,335 FEET

RUN TARh GROSS DIVERT MANOMETER HATER STATIC FLC'J BIFF, HAZEK PIPE

NO, HT UT TIME HEIGHT SID. TEMP. TEMP

.

PRESS, RATE PRESS

i

WILLIAMS REYNOLDS

(Rft) (LB) (LB) (SEC) (INCH) DEV. (DEG C) (DEG C) ( FSI A

)

(GPH) (PSI) COEfF. NUMBER

NANO. FLUID - HATER BAROMETER - 75,03 CH OF MERCURY AIR TEMPERATURE - 20.75 DEGREES CELCIUS

31 118,7 1921,0 97,568 55.156 0,111 21.60 24,15 105.50 133.2 1,979-9 139.63 2217/3.0

32 121,0 1919,0 97,543 55,038 0,031 21.60 24.13 105,50 132,9 1,9757 139.49 221423,0

33 121.2 1919.0 97.433 55,412 0,134 21.70 24.21 1Q5.50 133.1 1.9891 139,12 221791,0. 34 121,1 1918.0 97,416 55,652 0.0/3 21,75 24.24 105,60 133.0 1,9977 133,76 221369,0

35 121,0 1911.0 97,435 55,430 Q, 107 21,85 24.28 105,60 132.5 1.9397 138,50 221157,0

HAND, FLUID -- HATER BAROMETER - 75,05 CH OF MERCURY AIR TEMPERATURE -- 21,33 degrees CELCIUS

36 121,1 1721.0 93.772 43.022 0,113 22,15 24,31 105,60 116.8 1.5442 140.05 195116,0

37 121,3 1710,0 93.531 42,908 0,036 22,15 24.35 105,70 116,3 1.5401 139.61 194335,3

38 121.2 1704.0 93,54/ 42,622 0,069 22,20 24,33 105,70 115.8 1,5293 139,53 193752.0

39 120.9 1703.0 93,415 43,038 0,156 22,30 24,41 105.70 115,9 1,5465 138.89 194047.0 40 121.0 1706.0 98,493 43,180 0,101 22,40 24,46 105,80 116,1 1,5497 133,87 194451.

Q

NANO. FLUID - 1HATER BAROMETER - 75.05 CH OF MERCURY AIR TEMPERATURE - 21,72 DECREES CeLCIUS

41 120.3 1517.0 99,040 33,420 0,092 22,60 24,49 105,70 101.7 1,1994 139.78 170509,0

42 120.9 1521.0 99.469 33,470 0,033 22,60 24,51 105.80 101,5 1,2012 139,41 170257,0

43 121.1 1495.0 99.478 32,330 0.056 22.60 24,52 105.80 99,6 1,1621 139,26 167091.0

44 121.1 1515.0 99.487 33.650 0.144 22.70 24.53 105.80 101.1 1,2076 133.37 169543.0

45 121.0 1518.0 99,502 33.866 0.122 22.90 24,56 105.90 101.3 1.2153 138.13 170000.0

HAND. FLUID - HATER BAROMETER - 75.05 CH OF MERCURY AIR TEMPERATURE - 22,02 DEGREES CELCIUS 46 120,7 1316.0 100,550 24.420 0.033 22.95 24.62 105.90 85,7 0,8763 139,62 144113,0

47 121.2 1322.0 100.510 24.734 0.162 23.05 24,64 105.90 86.2 0,3376 139.35 144399,0

48 121.1 1322.0 100.454 25,022 0.135 23,20 24,63 106.00 86.2 0.8979 133.58 145112.0

49 121.1 1306,0 100.433 24,510 0,068 23,25 24,69 106,00 85.1 0,8795 133,2? 143231.0 50 121.2 1306,0 100.424 24.644 0.043 23,40 24,72 106,00 85,1 0,8343 137,90 143327 ,

0

HAND. FLUID - HATER BAROMETER - 75,03, CH OF HERCURY AIR TEMPERATURE - 22,3 DEGREES CclCIUS

51 120.8 1115.0 101.371 17.283 0.060 23.50 24,74 106. QO 70,7 0,6203 133,85 119196,0

52 121.0 1119,0 101,506 17,503 Q.066 23,55 24.75 106.00 70,9 0.6280 133.26 119517,0

53 120.8 1121.0 101,405 17,577 Q.099 23.55 24,79 106.00 71.1 0,6307 133.40 119999,0

54 121,0 1118.0 101.433 17,564 0,096 23.75 24,79 106.00 70.9 0,63-02 137.97 119576,0 55 121.0 1115,0 101,460 17,637 Q.C96 23.75 24,81 106,00 70.7 0.6328 137.21 119240.0

HAND. FLUID - HATER BAROMETER - 74,98 CN OF MERCURY AIR TEMPERATURE - 22,54 DEGREES CELCIUS

56 120.8 915.5 105,592 10,697 0,128 23.80 24.82 106.00 54,3 0,3333 133,12 91620.0

57 121.1 916.4 105,472 10,698 Q.196 23,30 24,85 106, QO 54.4 0,3838 133,38 913j0.3

53 120.9 920,8 105.504 10,772 0,113 23.80 24,86 106.00 54.7 0 , 33c>j 133,62 92372.6

59 120.9 920.7 105. 4S6 10,888 0.098 23.90 24,87 106,00 54.7 0,3906 137,83 92395.9

60 121.0 918,4 105.482 10,840 0.034 24.00 24,88 106.00 54.5 0,333? 137.75 92141.2
18

AISI PIPE FRICTION TESTS

PIPE DESIGNATION — 2A

DATE 12/23-31/7 OBSERVERS - JH VB

AVE. INNER DIA. - 2.0665 inches; TAP SEPARATION - 16 .335 FEET

GROUP FLOWRATE DIFF. PRESS

.

HAZEN-U ILL IANS VELOCITY FRICTION PIPE

NO* MEAN STD. MEAN STD. MEAN STD. FACTOR REYNOLDS

(GPtt) DEV. (PSI ) DEV. DEV. (FT/SEC) NUMBER

1 61*9 0.05 0.414 .0013 151.23 0.28 5.92 0.0180 103374

9 75.7 0.33 0.616 .0073 149.11 0.31 7.24 0.0179 127502

3 89.1 0.21 0.854 .0013 147.13 0.33 3.52 0.0179 150607

4 105.2 0.14 1.189 .0064 145.28 0.28 10.07 0,0179 178424

5 119.4 0.13 1.537 .0060 143.47 0.32 11.42 0.0179 202978

6 134.9 0.70 1.997 .005? 140.75 0.82 12.91 0.0182 230i55

7 133.0 0.27 1.986 .0037 139.10 0.47 12.72 0.0137 221604

8 116.2 0.39 1.542 ,0077 139.40 0.51 11.11 0.0190 194350

9 101.0 0.33 1.197 ,0206 139.00 0.69 9.66 0,0195 169480

10 85.7 0.55 0,385 .0033 133.75 0.72 8.19 0.0201 144137

11 70.9 0.18 0.628 .0043 133,14 0.61 6.78 0,0203 119505

12 54.5 0.13 0.387 . 0030 138.14 0.37 5.22 0.0216 92076
19

AISI PIPE FRICTION TESTS

PIPE DESIGNATION - 2B DATE 1/2/80 OBSERVER3 - Jll VB Pul AVE. INNER DIA, - 2,0919 inches; TA? SEPARATION - 16,125 FEET

RUN tare GROSS DIVERT — MANOMETER WATER STATIC FLOW DIFF, HAZEM PIPE

NO, ut WT TIME HEIGHT STD. TEMP. TEH?, PRESS. RATE PRESS, LULL IANS REYNOLDS (RN) (LB) (LB) (SEC) (INCH) DEV. (DEG C) (DEG C) (PSIA) (GPU) (F'SI

)

COEFF. NUMBER

NANO. FLUID - WATER BAROMETER -- 75.96 CM OF MERCURY AIR TEMPERATURE - 21,63 DEGREES CELCIUS

1 120. S 1933.0 89,037 55,044 0,040 22,90 24,05 121.60 146.8 1,9740 147,93 240790,0

0

i. 119,7 1932.0 89,197 54,937 0,044 22,95 24,03 121,50 146,5 1,9701 147.83

' 240622.0

3 120.5 1927,0 83.784 55,11? 0,036 22,95 24,11 121.60 146.7 1,9766 147.79 241118,0

4 119.9 1930.0 89,114 55,051 0.062 22,90. 24,15 121,50 146,5 1.9743 147.63 240905.0

5 120.6 1928,0 83.90/ 55.129 0.025 22.95 24.13 121,60 146,6 1,9770 147.64 241256.0

HAND. FLUID - WATER BAROMETER -- 74,96 CM OF HERCURY AIR TEMPERATURE - 21.76 DEGREES CELCIUS

6 120.3 1926.0 102.426 41,916 0.051 23,00 24,23 119,90 127,1 1,5052 143,47 209430,0

7 120.5 19t4»0 102,373 41,850 0.065 22,95 24,24 119.50 127,1 1,500? 142,49 209327,0

8 120,5 1926,0 102,434 41.9/8 0,047 23.05 24,23 119,60 127,1 1,5055 143.32 209609.0

9 120.2 1927.0 102.616 41,361 0,034 23,05 24,33 119.40 127.0 1.5013 148,39 20960j.O

10 120,3 1922,0 102.274 42.023 0,042 23,05 24,34 119,40 127,1 1,5071 143,16 209756,0

KANO. FLUID - WATER BAROMETER --- 74.92 CM OF MERCURY AIR TEMP ERATURE - 22,01 DEGREES CELCIUS

11 120,3 1522.0 90,295 32,890 0,045 23,15 24,26 121,30 111,9 1,1794 149,00 184464,0

12 120,7 1526.0 90,493 32.980 0.0/6 23.20 24,30. 121,30. 112.0 1,1827 148,89 184752.0

13 120,8 1523.0 90.471 32,926 0,060 23,25 24,30. 121,20 111.8 1,1807 148.73 184389,0

14 120.5 1524,0 90,411 33,060 0,063 23.35 24,33 121,30 112,0 1,1355 143,65 184990.0

15 120,7 1523,0 90,527 32.960 0,035 23,35 24,42 121,30. 111.7 1,1319 143,57 184743,0

HAND* FLUID - WATER BAROMETER - 74,92 CM OF MERCURY AIR TEMPERATURE - 22, OS DEGREES CELCIUS

16 320,3 1513.0 91,053 24,159 0,127 23,25 24,45 115,60 94,9 0,3665 149,21 156979,0

17 320.8 1532,0 91.463 24,365 0,161 23.40 24,43 113.30 95.5 0,8733 149.54 153135.0

18 325,9 1530,0 91.442 24,409 0,0/2 23,40 24,49 118,30 95.0 0,8754 143,55 157277.0

19 321.9 1532.0 91,451 24,413 0.026 23.45 24,51 118,30 95,4 0.8755 149.27 153110,0

20 321.2 1532,0 91.441 24,473 0.023 23,45 24,55 118.30 95.5 0,8776 149.18 153350,0

HANG, FLUID -- HATER BAROMETER -- 74.93 CM OF MERCURY AIR TEMPERATURE - 22.13 DEGREES CELCIUS

21 321.5 1317.0 91,0/7 16,981 0,037 23.60 24,57 120.00 78.8 0,6089 150.04 130768,0. 22 321.4 1319,0 91,461 16,931 0.030 23,60 24,58 120. CO 78,7 0,6071 149.97 130520.0

23 321.8 1322.0 91,436 17,058 0,031 23,60 24,59 120,00 73.9 0,6117 149.80 130923.0

24 321.1 1311.0 91,417 16.784 0.263 23,60 24.62 120,00 78.1 0.601? 149,59 129632,0 25 321.4 1316,0 91.433 16,863 Q.046 23,60 24,63 120. CO 78.5 0,6047 149,39 130302.0

HAND. FLUID - HATER BAROMETER - - 74.94 CM OF MERCURY AliR TEMP"EkAT ure 22.12 DEGREES CELCIUS

26 321.7 1115,0 90.765 11.123 0.041 23.65 24,65 121.50 63.0 0,3983 150,82 104738.0

27 321,0 1105.0 90.459 11,030 0.038 23,70 24,67 121.60 62.5 0,3955 150,24 103904.0

28 320,4 1103,0 90.547 10,931 0.032 23,75 24.67 121,60 62.3 0,3919 150.55 10.4617,0 29 321,4 1104,0 90.419 10,988 0,016 23.75 24,69 121,70 62,4 0,3940 150.35 103807.0

30 322.4 1103,0 90.483 10,932 0,044 23.70 24,71 121.60 62,2 0,3920 150.27 103511,0
20

AISI PIPE FRICTION TESTS

FIFE DESIGNATION - 28 DATE 1/2/SO OBSERVERS - JH VB r,H AVE, INNER BIA, - 2,091? INCHES} TAP SEPARATION - 16*125 FEET

RUN TARE GROSS DIVERT MANOMETER: —- WATER STATIC FLOW DIFF, HAZEN Plr'E NO. HT UT TIME HEIGHT STD, TEMP, TEMP'. F‘KESS, RATE PRESS

WILLIAMS REYNOLDS (RH) (LB) (LB) (SEE) (INCH) DEV, (DEG C) (DEG C) (PSIA) (GPii) (PSD COZFF, NUMBER

KANO. FLUID - WATER BAROMETER -• 75,53 CM OF MERCURY AIR TEMPERATURE - 21,52 DEGREES CELCIUS

31 120.4 1529.0 90.104 34,047 0,055 22.80 24,31 122,40 112,8 1.2210 147,33 186026,0

32 120,1 1519,0 89.592 34,011 0,028 22,80 24,35 122.30 112,6 1,2197 147.23 185955.

Q

33 121,0 1514,0 89.318 33,98? 0,057 22.70 24,37 122.30 112.5 1.2139 147,11 135316,0

34 120,4 1527,0 90,334 33,983 0,043 22.70 24,41 122,30 112.3 1,2137 146,3? IcIjo/ 4*0

35 120.4 1526,0 90,316 33,991 0.031 22.70 24,44 122,30 112,3 1,2190 146,80 i3jS95»0

KANO. FLUID -- HATER BAROMETER - 75.52 CM OF MERCURY AIR TEMPERATURE - 21,6? DEGREES CELCIUS

36 120,1 1921.0 102.715 43,036 0.036 22.80 24,52 120,80 126,5 1,5452 145,4? i.v / J t J* v 37 120,7 1927.0 103.097 43,0/0 Q.056 22,80. 24,54 121,10 126.4 1,5446 145.41 209432,0

38 120.4 1928,0 103,158 43,126 0.100 22,80 24.56 121,20 126,4 1,5467 145,33 209595.0

39 119,7 1928.0 103,154 43,196 0,063 o*/ oa

LL.k 24,65 121,20 126.4 1,5492 145,27 210076,0

40 120,5 1922,0 102.953 43,135 G.Q47 22.80 24,66 121,10 1 Ti T

14.UI L. 1.5470 145,11 209728,0

HAND. FLUID - 1rlATEft BAROMETER - - 75.43 CM OF MERCURY AIR TEMPERATURE - 22,66 DEGREES CELCIUS

41 120,5 1923.0 89,915 56,150 0,035 23,20 24,64 121.90 144.4 2.0135 144,01 239917,0

42 119,4 1925.0 90,093 56,323 0.047 23,30 24,67 121,70 144.6 2,0197 143,90 240270,0

43 120,5 1915.0 89.675 56,216 0,032 23,35 24,72 121,80. 144,3 2,0153 143 , 83 240554.0

44 120,3 1923.0 90.395 53.321 0.044 23,45 24.76 121.70 144,2 2,0195 143.59 240192,0

45 120,7 1925,0 90.147 56.310 0,076 23,50 24.73 121,80. 144.4 2,0191 143.74 240499,0

KANO. FLUID - HATER BAROMETER - - 75.42 CK OF MERCURY AIR TEMPIlRATUrE -* 22,69 DlGFxt.ES CELCIUS

43 120.6 1517,0 103,503 24,451 0.074 23,75 24,86 119,20 94.6 0.8768 147.30 157798,0

47 120.7 1521.0 10/, 023 24.440 0,031 23.80 24.39 119.50 94,4 0.8764 147,53 157575,0

43 120,3 1525,0 107,177 24,533 0,051 24.00 24,33 119.20 94.5 0.8797 147.48 157810.0

49 120.6 1524,0 107,294 24,533 0.062 e4» 05 24,96 119.20 94.4 0.8797 147.1? 157752,0

50 120.6 1524,0 107,129 24,619 0,038 24,05 24,93 119,20 94,5 0,8327 147,14 158060.0

KANO, FLUID - HATER BAROMETER -- 75,44 CK OF MERCURY AIR TEMPERATURE — 23.07 DEGREES CELCIUS

51 120,5 13.20,0 110.053 17,260 0,124 24,20 25, Od 117,50 78,6 0,618? 148.33 131696,0

52 120,6 1320,0 110.232 17,22.2 0,05j 24,20 25.07 113,80 78,5 0,6175 143,26 131526.0

53 120.3 1320.0 110,584 17.142 0.032 24.30 25,10. 119.00 78,3 0.6146 148,20 131221.0

54 120,9 1320.0 110.400 17,269 0.043 24,30 25.12 113.90 78.4 0,6192 147.78 131428,0

55 120.4 1318,0 110.450 17,30/ 0.057 24,35 25,13 119.00 78,2 0.620s 147.36 131231,0

KANO. FLUID - HATER BAROMETER •-- 75,5 CM OF MERCURY iUR TEMPERATURE — 23,01 DEGREES CELCIUS

53 320,7 1116,0 117,124 10,793 0,081 24.35 25,17 120,70 61,3 0.386? 149,07 102933.0

57 119.9 1118,0 120,95? 10,152 0.094 24,25 25,13 119,60 59.5 0,3640 . 149.62 99970,8 53 120.6 1121,0 119,290 10,614 0,079 24,25 25,1? 119,60 60.5 0,3806 148,45 101624,0

59 120.7 1117.0 118,443 10,693 0,053 24.25 25,25 119.30 60.7 0,3834 143.30 102013,0

30 120.5 1118,0 113.437 10,805 0.030 24.20 25,24 119,50 60.7 0.3873 147.63 102138.0
21

AISI PIPE FRICTION TESTS

PIPE DESIGNATION — 2B

DATE 1/ 2/80 OBSERVERS - JH VB HH

AVE. INNER 1 <t

h*H 2.0919 INCHES? TAP SEPARATION - 16 .125 FEET

ROUP FLOURATE DIFF* PRESS* HAZEN-U ILL IANS VELOCITY FRICTION PIPE

NO. MEAN STD * NEAN STD* NEAN STD. FACTOR REYNOLDS

( GPfiDEO, ( PSI > DEO* DEV* (FT/SEC) NUMBER

1

.L 146*6 0*13 1,974 ,0027 147*77 0.13 13*69 0*0165 240933

9 127*1 0*06 1.504 .0027 143*37 0*13 11*86 0.0167 209545

3 111*9 0*12 1.182 .0023 143.77 0*13 10.44 0.0170 184669

4

. VCi * «1 0*31 0*374 * 0043 149.15 0*36 8*89 0.0173 157770

5 78*6 0*32 0*607 • 00>j3 149.86 0.13 7*34 0.0177 130439

6 62*5 0*32 0.394 .0029 150.44 0.24 5*84 0.0181 103915

/7 112*5 0*21 1.219 .0009 147.07 K) * f-Z 10*50 0.0173 135333

8 126*4 0*10 1*547 .0018 145.32 0*14 11*80 0.0174 209686

9 144*4 0*12 2.018 . 0028 143*82 0*16 13*43 0.0174 240206

10 Of c! T * J 0*10 0*879 .0026 147.43 0*27 8*82 0.0177 157799

1

73*4 0*17 0*613 *0022 147.98 0*41 7*32 0,0181 131420

1 9 60*5 0 * £) J 0,330 ,0096 148,61 0.76 5.65 0.0186 101736
22

AISI PIPE FRICTIOM TESTS PIPE DESIGNATION - 2.5A DATE 12/19/79 OBSERVERS - JH VB

A'vL* IilffcR DJA. - 2.474 INCHES* TAP SEPARATION - 15*552 FEF.T

R’J.N Tare gross DIVERT —- HALS,ALTER; —- WATER STATIC FLOW BIFF. HAZF.fI PIPE

fin. HT HI TIME HEIGHT STB, TEH?. TEH?, PRESS. RATE PRESS. WILLIAMS REYNOLDS

(RN

)

(LB) (LB) (SEC) (INCH) DEV. (DEG C) (DEG C) (PSIA) (GPU) (PSD CGEFF, NUMBER

FANS. FLIilfi - HATER BAROMETER - 75,26 m of MERCURY AIR TEMPERATURE - 21,2 DEGREES CELCIUS

1 140.5 2123*0 172.701 7,706 0,162 22.65 24,25 121,20 82,8 0,2764 152,28 115358,0

»»i. 152.4 2133.0 165,862 8,263 0,094 22,65 Oi 07

L

l1 1 LJ 119,90 86,1 0,2965 152,48 120049,0

3 142.0 2122.0 164,063 8,314 0,140 22,55 24,30 121,00 86,2 0,2987. 152,10 1201.75,0 4 141.5 2122.0 169.164 8,013 0.145 22,65 24,32 120,9-0 84,4 0,2874 152,06 117872,0

5 347,6 2122.0 171,333 7,823 0.117 o-i Oft LL * 0V 24,35 121,00 83,1 0,2806 151.63 116045.0 Km FLUID - HATER BAROMETER - 75.28 CM OF MERCURY AIR TEHPERATiiSh - 21.35 DECREES CELCIUS 6 150.7 2140,0 128.101 13,939 0.217 22,70 24,43 118,80. 112,0 0,4999 149,53 156639.0

1 14?,. 2 2124,0 129,636 13,821 0,133 22,70. 24.44 113,70 110.8 0,4957 143.57 154961.0 8 354,8 2126,0 131,755 13,094 0.160 22,80 24,47 119.20 107,8 0,4696 148,86 150878,0

9 145.8 2124.0 131.352 13,317 0,165 22,80 24,51 119.10 103,7 0,4776 148.75 152281,0

10 147,2 2126.0 133.365 13,03] 0,360. 22,80 24,53 119,30 107,0 0,4674 148,17 149973,0

KAMI* FLUID - lLATER BAROMETER - - 75,32 CH OF MERCURY 1AIR TEMPERATURE - 21.5 DEGREES CELCIUS

11 142,5 2131.0 109,932 18,876 0.164 22.80 i.7, Ji> 120,50 130.5 0,6770. 147.85 182946.0

12 145,0 2156,0 110.161 19.222 0,104 22,80 24,58 120.30 131,7 0.6894 147,76 184703,0

13 153,5 214?,

0

110,470 13,922 0,0/3 o-l Oft Li.IWW 24,59 120,60 130,3 0,6786 147,46 182810,0

14 145,7 21.33,0 110,5.99. 19,251 0*203

•“>•» OA

Li. Vix/ 24,62 120.60 131.2 0,6904 14/, 16 184265.0

15 143,3 2U?,0 111.157 19,196 0,090 22,80 24,63 120.40 131,1 ft, 6885 147,25 184138,0

MANS. FLUID - IHATER BAROMETER - - 76.18 CH OF MERCURY AIR TEMPERATURE - i?,7i degrees celcius

16 143.9 3140,0 141.798 25.533 0.077 20,40 24,19 120,20 152.4 0,9162 146,64 212072.0

17 154.7 3139,0 143,131 24,931 0,0.49 20,55 24,20 120,70 153.3 0.S946 146.53 209243,0

18 146,8 3140,0 141,131 25.811 0.077 20.65 24,21. 120.20 153.0 0.9261 146,33 212956.0

19 144.8 3139.0 139,332 26,503 0,337 20,80 24.24 120,20 155.0 0,9510 146.17 21.5913,0

Oft

L\t 146,4 3137,0 140,377 26,445 0.282 2.1,00 24,31 120.60 153.7 0.9488 145.09 214359,0

HAN?.. FLUID - HATER BAROMETER -- 76.26* CH GF HEkCURY AIR TEMPERATURE - 20,13 DEGREE:s CELCIUS

21 141.5 3H8.0 10/. 933 44,245 0,160 20,85 24,39 119,20 200.8 1,5876 143.55 280599.0

22 146,9 3144,0 10/. 876 44,119 0,0.31 21.00 24,41 119.30 200.4 1.5830 143,48 280129.0

23 146.0 3133,0 10/, 903 43,949 0,135 21.15 24,47 119,60 203.0 1.5763 143.50 279917,0

24 147,2 3150,0 10/. 997 44,275 ft. 038 21.10 24,48 119,30 203,5 1.5886 143,32 280/54,0

25 145,2 3141.0 109.597 43,700 ft, 069 21,25 24,49 119.50 199.0 1.5679 143,21 278610. ft

HA,NO, FLUID -- HATER BAROMETER --- 76,32 CM OF MERCURY AIR TEMPERATURE - 20.43 DEGREES CEIXIUS

24 144,2 3146.0 123.214 34,669 0,029 21.35 24,56 119,50 175.7 1.2433 143,34 24640/.

0

27 146.4 3167.0 123.803 34,760 ft. 036 21,40 24,59 119.30 176.0 1,2471 143,34 246914,0

28 145.2 3145,0 123,274 34 , 16^3 0.0 .^S 21.45 24,63 119,50 175.5 1,2436 143.19 246480.

Q

29 145.5 3159,0 123,697 34,736 0,031 21.45 24,65 119,40 175.7 1.2462 143,15 246799,0

30 145.2 3151,0 123.606 3* , 697 Q.Q67 2.1.50 24.69 119,50 175.4 1,2444 143,04 246616.0
23

AISI PIPE FRICTION TESTS

PIPE DSSISMATIUM - 2.5A DATE 12/19/79 OBSERVERS - JH VB

AWE. INNER BIA. - 2.474 INCHES? TAP SEPARATION - 15.552 FEET

RUN TAlRh GROSS DIVERT —- MANOMETER WATER STATIC FLOW BIFF, HA7.EN PIPE

NIK HT WT TIME HEIGHT STD, TEMP . TEMP* Press, RATE PRESS, WILLIAMS REYNOLDS (RN) (LB) (LB) (SEC) (INCH) DEV, (DEG C) (DEG C) (PSIA) (GPfi) (PSD CUEFF

,

NUMBER

HAND. FLUID - WATER BARONETER - 75,37 CK OF MERCURY AIR TEMPERATURE - 21,48 DEGREES CELCIUS

31 143.2 314S.0 103,714 44,210 0,131 22.75 24.29 119.50 208,6 1,5857 149,22 290896.0

32 149.4 3142.0 103.411 44,171 0,043 22.80 24,32 119,50 203.3 1,5842 149,09 2906/2,0

33 143.2 3155.0 103,574 44.664 0*033 n-i zc; O J 24,36 119.40 209,4 1.6020 143.95 292399,0

34 147.3 31.49.0 104.134 43*869 Q.086 22,75 24,3? 119,50 207,9 1.5734 149.34 290503,0

35 141,9 3149.0 103.910. 44.376 0*0.34 22.80 24,42 119.50 208.7 1,5916 149,01 291846,0

KANO. FLUID - HATER BAROMETER -- 75,35 CM OF MERCURY AIR TEMPERATURE - 21.68 DEGREES CELCIUB

34 149.4 3153.0 117.270 35.242 0,104 22,75 24.42 118,30 184,8 1.2641 149.41 258365,0

37 145,9 3153,0 117*890 34,787 0.051 22,80 24,46 118.50 184.0 1,2477 149,81 257450,0

38 142,8 3140.0 117,089 35,273 0,09V 22.90 24,49 118.40 184,6 1,2651 149,22 258519.0

39 147,7 3143.0 117.414 34.873 0.149 22.90 24.50 118.50 184,0 1.2508 149.63 257639.0

40 347,4 3143,0 117,0:11 35,280 0,094 22,90 24,51 118,50 134,6 1 , 2tij4 149,17 258572,0

HAND. FLUID - 1;!ATER BARONE TER - - 75,31 CM OF MERCURY iAIR TEMPERATURE - 22.49 DEGREES CELCIUS

41 122.3 1924,0 84,921. 25,093 0,044 23,25 24,60 120,40 153,2 0.9000 148.84 214996.0

42 122.0 1912.0 84,484 24,936 0,016 23.40 24,64 120,20 152,8 0,8960 143,83 214639,0

43 121.1 1911.0 84.494 25,0.48 0,041 23,40 24,67 120.40 152,8 0,8982 148.61 21.4735,0 44 121,2 1912.0 84,444 25,141 0,0.44 23.60 24,70 120,30 152,9 0.9015 148,45 215057,0

45 121.4 1910.0 84,433 25,130 0,030 23,70. 24,75 120,30 152,8 0,9011 143.35 215032,0

KANO, FLUID - HATER BAROMETER -- 75,32 CK OF MERCURY AIR TEMPERATURE - 22,83 DEGREES CELCtUS

44 121,0 1722.0 87 » ^44 19 * 0?o 0,045 23.80 24,77 119.20 132,2 0,6347 148,91 186189,0

47 121.5 1725,0 87,452 19.153 0.027 23.80 24,81 119.50 132.3 0.6868 143.72 186408.0

43 121.0 1724.0 87.390 19.233 0,047 23,85 24,83 119.30 132.3 0,6896 148.45 136559,0

49 121,2 1724.0 87.445 19,276 0,049 24,00 24,37 119.80 132,4 0.6911 148.35 186805,0 50 121.1 1722,0 87.351 19.250 0.034 24,00 24,88 119,20 132,2 0.6902 148,25 186591,0

KANO. FLUID -- HATER BAROMETER -- 75,33 CH OF MERCURY AIR TEMPERATURE - 23,04 DEGREES CELCIUS

f.t 120.7 1522.0 91,093 13.823 0.026 24.00 24,92 121.10 111.0 0,4958 148.83 156764.0

52 121.3 1522,0 91,033 13,873 0.015 24,00 24,97 120,80 11Q.9 0,4974 148,50 156853.0

53 121.3 1517,0 90,729 13,887 G.02H 24,15 25.00 12.1,20 111.0 0,4979 148.48 157005,0

54 121.3 1518,

0

90.777 13,920 0,035 24,15 25.01 121,10 111.0 Q .4991 148,31 157067,0

55 i21.2 1517.0 90,739 13, V56 0*027 24.20 25.04 121.30 111.0 0.5003 148,08 157129,0

KANO. FLUID - HATER BAROMETER •- 75,35 CH OF MERCURY AIR TEMPERATURE -- 23.08 DEGREES CELCIUS

54 120,9 1317.0 104,504 7,982 0.024 24.20 25,04 119.40 82.6 0,2362 149,02 116912,0

57 120,9 1324,0 104.507 8,065 0,0.37 24.20 25,10 119.40 83.0 0,2892 149.05 117739,0

50 120.7 1324.0 104,443 8,100 0,034 24,15 25.11 120,10. 83,1 0,2904 148,75 . 117802,0

59 121,0 1334,0 104.534 8.170 6,600 24.10 25,13 119,30 83,7 0,2929 149.19 11 3750.

Q

40 119,1 1325.0 104,474 8,131 0,012 24,10 25,15 119.90 83,3 0,2933 143,29 118169,0
24

AISI PIPE FRICTION TESTS

PIPE DESIGNATION -- 2.5A

DATE 12/19/79 OBSERVERS - JH VB

AVE INNER DIA. - 2.474 INCHES} TAP SEPARATION - 15. 552 FEET

GROUP FLOtIRATE DIFF, PRESS, HAZEN-WILLIAM3 VELOCITY FRICTION PIPE

NO* MEAN STD. MEAN STB. MEAN STD. FACTOR REYNOLDS

( GPM ) DEO, (PSI) DEO, DEV. (FT/SEC) NUMBER

1 84,5 1.60 0.28S ,0096 152.11 0.32 5.64 0.0174 117890

9 109,3 2.03 0.482 .0150 143.78 0.50 7.29 0.0175 152946

"2 131,0 0,57 0.685 .0064 147.50 0.30 3.74 0.0173 183774

T 152,9 1,72 0.927 .0236 146.15 0.62 10.20 0,0172 212909

C"

vJ 200,1 0.72 1.531 0036 143.41 0.14 13.36 0.0171 280002

6 175.7 0,22 1.245 .0015 143.21 0.13 11.72 0,0174 246643

T 208 .

0,55 1,537 .0105 149.13 0,16 13,92 0,0153 291264

8 184,4 0.33 1.259 .0036 149.45 0.27 12.31 0.0160 258119

9 152,9 0.17 0,899 .0023 143.62 0.22 10.21 0.0166 214902

1C 132,3 0,07 0.689 .0027 143.54 0.27 8.83 0,0170 186511

11 111.0 0,02 0.493 .0017 148,44 0.28 7.41 0.0175 156964

i

*j L 4. 83,1 0,41 0,290 .0029 148,86 0.35 5.55 0,0132 117375
25

AlSI PIPE FRICTION TESTS PIPE DESIGNATION - 3A DATE 12/21/7? OBSERVERS - VB i JH

AVE, INNER DIA. - 3.0738 inches; TAP SEPARATION - 14,469 FET

RUN TARE GROSS DIVERT MANOMETER WATER STATIC noy DIFF. HAZEM PIPE

NO, VT UT TIME HEIGHT STD. TEMP. TEMP. PRESS. RATE PRESS, WILLIAMS REYNOLDS

(RN) (LB) (LB) (SEC) (INCH) DEV, (DEG C) (DEG C) (PSIA) ( GPH > (PSI) COEFF. NUMBER

NANO, FLUID - HG BAROMETER -- 75, 7E1 CM OF MERCURY AIR TEMP'ERATURE ~ 21.5 DEGRES CELCIUS

1 173,2 4070.0 56.427 7,171 0,021 22.50

rn oq 116,00 497,9 3,2646 130.93 542758,0

2 183.2 4099.0 56.517 7.197 0.025 22.60 22.93 116,00 498,9 3,2766 130,93 544416,0

3 175.6 4090.0 56.414 7.229 0.031 22.70 22.96 116.00 500,3 3,2912 130.97 546253.0

4 179.1 4075.0 56.260 7.185 0.022 22.70 23.00 116.00 499.3 3,2710 131.15 545625,0

5 180.0 4079.0 56,173 7.214 0,028 22.80 23,03 116.00 500.4 3.2844 131,15 547202,0

NANO. EUID - WATER BAROMETER -- 75,781 CM a

r MERCURY AIR TEMPERATURE - 21,5 DEGRES CECIliS

6 179,7 4114.0 94.860 34,295 0,093 24,00 23.4S 122,00 299,1 1.2295 133.32 330109,0

7 160.2 4060.0 93.561 34,505 0.108 24.00 23.50 121.50 300,6 1,2371 133,54 331897.0

8 184.5 4037,0 93.186 35,057 0.066 24,10 23.52 120.80 302.0 1.2569 133,02 333603,0

9 185,7 4062.0 93,390 34.380 0.062 24.25 23,54 122,20 299,3 1.2325 133,25 330778,0

10 178.4 4070.0 93.418 34.816 0.100 24,10 23.56 122.20 300.4 1.2482 132,82 332123.0

HAND. EUID - WATER BAROMETER -- 75,78 CH OF MERCURY AIR TEMPERATURE - 21,5 DEGRES CECIL’S

11 178.8 4060.0 102.443 29,484 0,045 22,80 22,83 120.00 273.2 1.0575 132,10 297447,0

12 177.4 4061.0 102.550 29,468 0.059 22,80 22,86 120.00 273.0 1,0569 132.09 297509.0

13 179.0 4060.0 102.454 29.462 0.076 22.80 22,89 120.00 273,1 1,0567 132,14 297777.0

14 177.8 4118.0 102.505 30.122 0.340 22.80 22.93 120.00 277,1 1.0303 132,49 302425,0

15 178.4 4221.0 102.448 31.872 0.087 22.80 22.95 119.30 284.5 1,1431 131.92 310533,0

KANO. EUID - WATER BAROMETER -- 75.76 CM OF MERCURY AIR TEMPERATURE - 21.95 DEGREES CECILIS

16 177.7 4086.0 117,408 22,433 0.070 22.85 23.05 120,00 240.0 0.8047 134,54 262563.0

17 179.3 4077.0 117.183 22,477 0.078 22.95 23,07 120.00 239.8 0.8061 134.30 262453.0

18 179,8 4030.0 117.243 22.431 0.061 23.00 23.11 120.00 239,8 0.8044 134,47 262709.0

19 179.9 4087.0 117.203 22,502 0.061 23. LO 23,15 121.00 240,4 0.8069 134.54 263496,0

20 179.2 4077.0 117.157 22.567 0.107 23.05 23,16 120,80 239.9 0.8093 134.06 263028,0

KANO. FLUID - HATER BAROMETER -- 75.74 CH OF MERCURY AIR TEMPERATURE - 22,34 DEGRES ELCIUS

21 179.0 3157,0 106.219 16.227 0,250 23.15 23.41- 121.10 202.2 0,5319 135.03 222821,0

22 178,7 3151,0 106.260 16.222 0.123 23.15 23.44 120.90 201.7 0,5817 134,74 222449.0

23 179.3 3164.0 106.310 16.141 0.086 23.40 23.46 120.80 202.4 0.5788 135,61 223365.0

24 177,1 3167.0 106,427 16,156 0.159 23.45 23.50 120.70 202.6 0,5793 135.63 223696,0

25 177,6 3161.0 106.310 16,282 0.060 23.50 23,51 120.80 202.4 0.5333 134.92 223502.0

MANQ. 1EUID - WATER BAROMETER -- 75.75 CH OF MERCURY AIR TEMPERATURE - 22.52 DEGREES CECIUS

26 162,9 3166,0 135,348 10,009 0.042 23,40 23,59 118,60 160.0 0,3590 138,76 177007.0

27 128,6 3144,0 135.283 10,176 0,039 23.40 23,63 118.60 160,7 0.3649 138. L6 177966.Q

28 166,7 3189.0 135.426 10.295 0,071 23,45 23.66 118.80 160.9 0,3692 137.46 173297.

Q

29 177,0 3175,0 135.308 10.114 0.081 23.60 07 LO

d-O t uu 118.30 159,8 0,3627 137.79 177092.0

30 173.8 3166,0 135,203 10,175 0.071 23.60 23.69 119.10 159.6 0,3649 137.18 176924.

Q

i
26

AISI PIPE FRICTION TESTS PIPE DESIGNATION - 3A DATE 127 21/79 OBSERVERS - VB 6 JH

AVE, INNER DIA, - 3,0738 :inches; TAP SEPARATION - 14,469 FEET

RIJN TAKE GROSS DIVERT MANOMETER HATER STATIC FLOW DIEF, HA2EN PIPE

NO. WT UT TIKE HEIGHT STD, TEMP,

'TEMP, PRESS, RATE PRESS, WILLIAMS REYNOLDS

(rn:I (LB) (LB) (SEC) (INCH) DEV. (DEG C) (DEG C) (PSIA) (GPM) (PSI) COEFF. NUMBER

KANO. FLUID - WATER

* BAROMETER -- 75.8 CM OF MERCURY AIR TEMPERATURE 22.47 DEGREES CELCIU3

31 178.5 2200.0 120,363 5.686 0,105 23.60 23.74 118.20 121.1 0,2039 142,59 134406.0

77 161.1 2181,0 120,293 5,729 0,089 23,60 23,79 118,40 121,1 0,2055 141,97 134512,0

33 165.1 2186,0 120.283 5,393 0,072 23.70 23.79 118.30 121.2 0,2113 139,92 134596,0

34 175.4 2196,0 120.312 5,834 0.089 23.65 23.81 118,20 121.1 0,2110 139.93 134600.0

35 109.5 2134,0 120.485 5.939 0,105 23.60 23.84 118.20 121.2 0.2130 139,34 134750.0

NANO. FLUID - WATER BAROMETER -- 75,83 CM OF MERCURY AIR TEMPERATURE - 22.39 DEGREES CELCIUS

36 169.5 2155,0 144,357 3.79S 0,074 23.70 23,83 120,20 99.2 0,1362 145,25 110392.0

37 153.3 2142.0 14-4.521 3.905 0.054 23.75 23.92 120,10 99,2 0,1400 143.15 110537.0

10

*JV 146,2 2132,0 144,363 3,943 0,071 23.80 23.94 120,00 99.2 0,1414 142.35 110539,0

3? 169.7 2156,0 144, 39S 3,833 0.065 23.65 23,95 119.30 99,2 0,1393 143,53 110567,0

40 146,8 2134.0 144,453 4.003 0,07? 23.55 23,95 119,30 99.2 0,1435 141.21 110575.0

KANO. FLUID - WATER BAROMETER -- 76,32 CH OF MERCURY AIR TEMPERATURE - 21.18 DEGREES CELCIUS

41 157.3 2131.0 117.307 5.775 0,034 22.85 24.73 113.50 121.4 0,2071. 141.67 137443.0 42 149.3 2157,0 117,030 5.997 0,055 22,80 24,78 113,40 123.7 0,2151 141.54 140292.0

43 146,2 2116,0 118,171 5,635 0.035 00 OA iX»UV 24,79 118,80 120.2 0,2021 142.24 136343.0

44 149.6 2147.0 117.920 5.811 0,026 22,80 24.79 113.30 122.2 0,2034 142.16 133547.0

45 145,7 2164,0 117,540 5.999 0,060 77 7c; i-J-H J 24.31 118,90 123.9 0,2152 141,65 140503.0

KANO, FLUID - WATER BAROMETER -- 76.34 CM OF MERCURY AIR TEMPERATURE - 21.33 DECREES CELCIUS

46 164.3 3156,0 137.161 10.067 0.028 22. SO 24,86 120.00 157.3 0.3611 136,02 17S663.0

47 144.3 3140,0 137.275 10,052 0.028 22.75 24,39 121,20 157.4 0,3605 136.13 173334.0

48 153.2 3176.0 137.430 10.132 0.042 22.80 24.93 119.30 158.3 0,3634 136.41 180064.0

4? 147.2 3173.0 137.365 10.203 0.034 22,75 24,94 119,30 153.9 0.3661 136,33 130729.0

50 146.6 3160.0 137.221 10.133 0.023 22.30 24.96 119.30 153.4 0,3652 136.10 130252.0

KANO. FLUID - WATER BAROMETER -- 76.44 CM OF MERCURY AIR TEMPERATURE - 21.35 DEGREES CELCIUS

51 149,0 3142.0 112.445 15.832 0.043 22.70 24.92- 118,20 .192.0 0,5697 129.73 218299.0

52 134,3 3143.0 112.077 16,169 0.051 22,75 24,94 118,00 193.6 0,5300 129.53 220256.0

53 146.7 3157,0 111,819 16,346 0.253 22,80 24.96 118.40 194.2 0,5363 129.19 220972.0

54 146.3 3146,0 112,239 16,113 0.033 22,85 24.99 118,0-0 192.8 0.5779 129.23 219469.0

55 145.5 3165.0 112.444 16,309 0.052 22,90 25,01 117.90 193.7 0,5350 129.02 220643.0

KANO, FLUID - WATER BAROMETER -- 76.45 CM OF MERCURY AIR TEMPERATURE - 22 DEGREES CELCIUS

56 160,0 4150,0 128.030 22,403 0,125 23.00 25,09 113,20 224,8 0,3035 126.13 2564S9.0

57 139.1 4166.0 128,579 22,710 0.175 23.10 25.15 119,60 225,9 0.8145 125.83 253074,0

58 144,7 4119,0 123.372 22.180 0.046 23.15 25,19 119.50 223,3 0.7954 125,98 255324.0

5? 155,4 4185.0 128.434 22,303 0,067 25.20 25,20 119.40 226.3 0,8176 125.80 253304.0

60 145,0 4126.0 128.644 22,153 0,033 23,20 25.21 119,60 007 7

i-i. O » 0,7946 126,00 255313,0
27

AIS1 PIPE FRICTION TESTS

PIPE DESIGNATION - 3A DATE 12/21 m OBSERVERS - VB L JH

AVE. INNER DIA. - 3.0733 inches; TAP SEPARATION - 14,469 FEET

RUN TARE GROSS DIVERT NANOMETER WATER STATIC FLOW DIFF. KAZEN PIPE

NO. VT IT TIKE HEIGHT STD. TEMP, TEMP, PRESS. RATE PRESS, WILLIAMS REYNOLDS

(RN) (LB) (LB) (SEC) (INCH) DEV, (DEG C) (DEG C) (PSIA) (GPM) (PSD COEFF, NUMBER

KANO. FLUID. -- WATER BAROMETER -- 76,4 2 CM OF MERCURY AIR TEMF'ERAIURE - 22.2 DEGREES CELSIUS

61 149.5 4150.0 121.635 25.426 0.122 23,15 25.28 117.20 237.3 0,9119 124,34 271811,0

62 143.1 4139.0 121.442 25,456 0.043 23.25 25.31 115.70 237,4 0,9130 124,23 272030,0

63 148.4 4156.0 121.444 25.643 0,053 23.25 25.33 115,4-0 238.1 0,9193 124,15 272934,0

64 159.8 4129.0 121.418 25,196 0.04S 23.40 25,34 118,50 235,8 0,9036 124,17 270432.0

65 150.1 4149.0 121.695 25.519 0.111 23.40 25.36 119.80 237,1 0,9151 123.97 271947.0

HANQ. FLUID - WATER BAROMETER - 76.37 CM OF MERCURY AIR TEMPERATURE -- 22,5 DEGREES CELSIUS

66 147.6 4155.0 112.621 30.124 0.096 23.40 25.39 119.90 256.7 1 ,0803 in 77 294664.0

67 149.2 4154.0 112.960 29.933 0.026 23.50 25.42 120.20 255,8 1,0734 122.70 293770,0

6S 147.0 4170.0 112.475 30.543 0,063 23.60 25.46 119,40 253,0 1.0953 122.45 • 296621.0

6? 147.3 4139.0 112.636 30.003 0,046 23.60 25.51 121.00 255,7 1.0760 122.50 294194,0

70 145.8 4151.0 112.666 30.199 0.045 23.70 25.52 119.70 256.5 1.0329 122.45 295170,0

AISI PIPE FRICTION TESTS

PIPE DESIGNATION — 3A

DATE 121/21/79 OBSERVERS - VB & JH

AVE. INNER DIA. - 3.0738 INCHES; TAP SEPARATION - 14 .469 FEET

GROUP FLOURATE DIFF. PRESS. HAZEN-UILLIAMS VELOCITY FRICTION PIPE

NO. MEAN STD. MEAN STD. MEAN STD. FACTOR REYNOLDS

(GPM) DEV. (PSI ) DEV. DEV. ( FT/SEC

)

NUMBER

1 499.4 1.03 3.278 .0106 131.03 0.12 21.59 0.0182 545252

9 300.3 1.16 1.241 .0114 133.19 0.28 12.98 0.0190 331702

3 276.2 4.97 1.079 .0373 132.15 .. 0.21 11.94 0.0195 301149

4 240.0 0.23 0.806 .0020 134.38 0.21 10.33 0,0194 262850

5 202.3 0.34 0.581 .0021 1.35,19 0.41 8.74 0,0196 223167

6 160.2 0.59 0.364 .0037 137.87 0.62 6.93 0.0196 177457

7 121.1 0.04 0.209 .0040 140.76 1.43 5.24 0,0197 134573

8 99.2 0.02 0.140 .0027 143.10 1.50 4.29 0.0197 110522

9 122.3 1.55 0.210 .0056 141.85 0.32 5.29 0.0194 138627

10 158.1 0.68 0.363 .0025 136.21 0.16 6.83 0.0201 179709

11 193.3 0.87 0.580 .0066 129.35 0.29 8.36 0,0215 219928

12 224.7 1.43 0.805 ,0106 125.95 0.14 9.72 0.0220 256802

13 237.1 0.81 0.913 .0059 124,18 0.14 10.25 0.0224 271831

14 256.5 0.95 1,082 .0085 122.57 0.14 11.09 0,0227 294884

i
28

A1SI PIPE FRICTION TESTS

PIPE DESIGNATION - 3D DATE DEC 19 l 2 OBSERVERS - JH VB HH

AVE, INNER DI A. - 3,0994 INCHES! TAD SEPARATION - 13,635 FEET

RUN TARE GROSS DIVERT HANOHETEF: WATER STATIC FLOW DIFF, HAZEM PIPE

NO, UT UT TINE HEIGHT STD, TEMP. TEMP, PRESS. RATE

nriror

r PvLoO WILLIAMS REYNOLDS

(RN)' < LB) .(LB) (SEC) (INCH) DEV. (DEG C) (DEG C) (PSIA) (GPM) (F’SI

)

CQEFF. NUMBER

HAND. FLUID - CATER BAROMETER -- 75.74 CM OF MERCURY AIR TEMPERATURE - 21,84 DEGREES CELSIUS

1 141.7 2122,0 144,890 2.681 0.076 22.90 23.78 118.70 98.6 0,0961 165.07 103565,0

0 173,1 2203.0 144.672 2,791 0.070 23.00 23.81 118,60 101,2 0,1001 165,82 111522,0

3 166,3 2193.0 144.533 2.835 0,096 23.00 23,85 118.30 101.1 0,1017 164.32 111542.0

4 151.8 2149.0 144,550 2,720 0.093 23.20 23.87 118.40 99.6 0.0976 165,49 109901.0

5 146.6 2115,0 144.721 2,701 0.036 23.30 23,90 118.40 93.1 0.0969 163,63 103310,0

NANO, FLUID -- CATER BAROMETER -- 75,7 CM OF MERCURY AIR TEMPERATURE - 21.96 DEGREES CELCIU3

6 160.1 2095.0 120,574 3,733 0,040 23,30 23.92 120.00 115,7 0.1341 161.95 127842.0

7 166.4 2117.0 120.767 3.774 0,061 23.35 23.96 119.90 116,5 0,1353 162,18 128731,0

8 159.4 2098,0 120,712 3.796 0,051 23,40 23,98 119.90 115.8 0,1361 160.74 iooiaa a liUiVuW

9 154.4 2142.0 120,633 3,922 0.050 23,40 24,00 120.00 118.8 0,1407 161.95 131424,0

10 159.2 2135,0 120.044 3,965 0.123 23,40 23.9? 119,80 118,7 0,1422 160,91 131312,0

KANO. FLUID - CATER BAROMETER -- 75.63 CM OF MERCURY AIR TEMPERATURE - 21,96 DEGREES CELCIUS

11 151.5 3187,0 135.514 7,417 0.037 23,05 24,13 118,40 161,5 0.2660 156.0? 179232.0

12 142.2 3205.0 135.686 7,446 0.045 23.00 24,15 118.30 162,8 0,2671 156,96 180690.0

13 140,8 3185.0 135,629 7,418 0.041 23,00 24.17 118.10 161,9 0.2661 156,39 179743.0

14 152,0 3164.0 135.735 7.227 0,048 23.00 24.18 113.20 160.0 0.2592 156,81 177739,0

15 142.6 3156,0 135.757 7.280 0.087 23,10 24.20 113.20 160.1 0.2611 156,24 177867.0

HAND. FLUID - CATER BAROMETER -- 75.66 CM OF MERCURY AIR TEMPERATURE - 22,02 DEGREES CELCIUS

16 142,6 3203.0 106.552 12.10S 0.050 23.05 24,26 120.00 207.2 0.4342 153,57 230441,0

17 139.7 3196.0 106.579 12.007 0,103 23,10 24.27 119.90 206,8 0,43-06 154.03 00 A

18 136.6 3169,0 106.673 11.834 0.039 23.10 24.28 120.30 205.0 0,4244 153,89 223168.0

19 139,9 3174.0 106,643 11.903 0.035 23,15 24.30 120.50 205,2 0,4270 153.50 223455,0

20 140.6 3199,0 106,734 11.992 0,071 23.20 24.31 120,00 206.7 0,4300 154.02 230136,0

NANO, FLUID - CATER BAROMETER -- 75,46 CM OF MERCURY AIR TEMPERATURE - 19.56 DEGREES CELCIUS

21 141.9 4151.0 124.633 15,145 0,079 21.25 23.85 ,.. 121.60 232.0 0,5433 152.36 255383.0

OO

L-i. 144,0 4147,0 125,274 14.918 0.063 21.25 23.89 121.40 230.4 0.5352 152,59 254404,0

07

i-O 143.6 4140.0 124.061 15.233 0.113 21,00 23.94 121.60 232.3 0,5465 152,0? 256736,0

24 148,0 4147,0 124,634 15,101 0.091 21,05 24,00 121.50 231.3 0,5418 152,15 255939.0

25 128.5 4135,0 125,835 14.892 0,031 21.05 24.04 121.50 229.5 0,5343 152.12 254184.0

NANO. FLUID - CATER BAROMETER •- 75,47 CM OF MERCURY AIR TEMPERATURE - 19.8? DECREES CELCIUS 26 140,9 4166.0 102,331 22,683 0,095 21,05 24.06 121,50 283,7 0,8133 149.76 314273,0

27 145,2 4152.0 102,554 22.406 0,043 21.15 24.03 120,60 281,8 0,303? 149.74 312294.0

28 157,8 4150.0 103,199 21,999 0,049 21,20 24,03 120.90 279,0 0.7892 149.75 309212,0

29 142.7 4154,0 101.978 22,803 0,155 21.25 24,10 120.80 283.7 0,8183 149,32 314542.0

30 146.3 4142,0 102,396 22,354 0,052 21.25 24.11 120,70 281,4. 0,8020 149,75 312105,0
29

AISI PIPE FRICTION TESTS PIPE DESIGNATION -- 3B DATE DEC 19 i 2 OBSERVERS - JH VB HH

AVE, INNER DIA, - 3.0994 :inches; TAD SEPARATION - 13,635 FEET

RUN TARE GROSS DIVERT NANOMETER 1-JATER STATIC FLOU DIFF. HAZEH PIPE

NO, «T UT TINE HEIGHT STD. TEMP.

‘TEMP. PRESS. RATE PRESS, WILLIAMS REYNOLDS

(Rn;i (LB) (LB) (SEC) (INCH) DEV. (DEG C) (DEG C) (PSIA) (GPM) (PSI) CQEFF, NUMBER

NANO, FLUID - HATER BAROMETER -- 74,73 CM OF MERCURY AIR TEMPERATURE — 21,62 DEGREES llLCi Uc* 31 150,8 4151.0 101.074 22,131 0,01? 22.80 23,66 120,30 235.4 0,7937 152.71 313577,0

32 147,0 4152.0 101.049 22,132 0.034 22.85 23.74 120,40 285.8 0.7937 152,94 314557,0

33 148,2 4153.0 101,139 22.154 0,020 23.00 23,75 120.30 235.9 0.7945 152,90 314720,0

34 142,3 4153.0 10L.216 22.116 0.047 23.00 23.78 120.40 235,7 0.7931 152,96 314743.0

35 148.5 4150.0 101.039 22.105 0.041 23.00 23.80 120.40 235,6 0.7923 152.92 314711,0

NANO. FLUID - HATER BAROMETER -- 74.75 CH OF MERCURY AIR TEMPERATURE - 22,1 DEGREES CELCIUS

33 143,0 4149.0 107 OOOlji.O » L. 7u 15,033 0.036 23,40 23.87 120.10 234,0 0,5391 154,34 258233,0

37 148.6 4143.0 123.204 15,056 0.035 23,40 23.89 120,10 233.8 0,539? 154,03 2531 17.0 3S 148.3 4147.0 123.23? 15.090 0.05S 23,55 23.91 120.20 233.9 0,5411 153.95 253324.0

39 148.8 4144.0 123.091 15,107 0.037 23,55 23,95 120.20 234,1 0,5417 153,93 253729,0

40 147,3 4133.0 123,078 15,053 0,043 23.60 23,98 120.10 233. S 0,5400 154.09 258627,0

NANO. FLUID - HATER BAROMETER -- 74.75 CM OF MERCURY AIR TEMPERATURE - 22,35 DEGREES CELCIUS

41 143.5 3147.0 103,946 12,06? 0.063' 23.60 24,01 120,80 203,2 0.4328 154,61 230339.0

42 143.4 3145.0 103.496 12,166 0.066 23.75 24,04 120.10 209,2 0,4362 154,63 231620,0

43 148.2 3144.0 103.930 11,996 0.035 23,30 24.05 121.10 207,8 0,4301 154.83 07f|1 l r

44 147,5 3143.0 103.395 12,163 0,036 23,85 24,08 121.30 203.9 0.4363 154.51 (\ A.J1UU U» V 45 147.5 3149.0 103.551 12.144 0.034 23.95 24,10 121.10 209,0 0,4354 154*75 071770 A

i-sJX./ i / » \J

NANO. FLUID - HATER BAROMETER -- 74.77 CM OF MERCURY AIR TEMPERATURE - 23 DEGREES CELCIUS 43 143.1 3139.0 133.543 7.342 0,033 23,75 24,14 121,60 161.6 0.2632 157.06 179359.0

47 145.9 3137.0 132,666 7.453 0.092 23.90 24.13 121.90 162.6 0.2674 156,66 130536,0

48 147,0 3139,0 134.632 7.245 0.021 24,20 24,21 121.60 160.3 0.2597 156,87 178113.0

49 147,9 3139,0 134.554 7.242 0.053 24.20 24,23 121,70 160.3 0.2596 156,94 178237,0

50 144.5 3135.0 133.179 7,414 0.046 24.35 24.25 121,70 161.9 0.2653 156,54

V 180116,0

NANO, FLUID - HATER BAROMETER -- 74.82 CH OF MERCURY AIR TEMPERATURE ~ 23,18 DEGREES CELCIUS

51 143.5 2123.0 126.261 3.668 0.032 24.25 24.40 119.50 113,1 0.1315 159,83 126149.0 52 151.6 2129.0 125.444 3,703 0,033 24,30 24, 119,00 113.7 0,1328 159.93 126339,0

53 147,9 2127.0 125.442 3.735 0.025 24.30 24.44 119.50 113.8 0.133? 159.32 127052.0

54 143.8 2126.0 124.318 3,796 0.042 24.55 24,45 119.40 114.8 0.1361 159.37 128234.0

55 147.0 2123.0 126.09-3 3.682 0.031 24.55 24.47 119.40 113.3 0.1320 159.89 126591.0

NANO. aUID - HATER BAROMETER -- 74,85 CH OF MERCURY AIR TEMPERATURE - 23.05 DEGREES CELCIUS

53 155.0 2129.0 143.425 2.601 0,045 24.70 24.50 118,80 95,9 0.0932 163,34 107236,0

57 140.1 2126.0 153.333 2.490 0.030 24.55 24,52 119.20 93.4 0,033? 163,15 104435.0 58 148,2 2126.0 149.512 2.622 0.044 24.60 24.54 119.20 95.4 0.0940 161.77 106749,0

59 147,9 2123,0 149.054 2,612 0,016 24.65 24.56 119.20 95.6 0,0936 162.33 106975,0

30 146,2 2123.0 150.575 • 2,56? 0.017 24.65 24.53 119.30 94.7 0,0921 162.32 106030.0
30

AISI PIPE FRICTION TESTS

PIPE DESIGNATION — 3B

DATE DEC 19 & 2 OBSERVERS - JH VB MH

AYE. INNER DIA. - 3.0994 inches; taf' SEPARATION - 13 .635 FEET

GROUP FLOWRATE DIFF. PRESS. hazen-uilliams VELOCITY FRICTION PIPE

NO. MEAN STD. MEAN STD. MEAN STD. FACTOR REYNOLDS

( GPM ) DEO. ( F’SI

)

DEO

.

DEV, ( FT/SEC) NUMBER

1 99,7 1,43 0,098 .0023 164.87 0.89 4.24 0,0151 109968

njC. 117.1 . 1.52 0,138 ,0035 161 .54 0.67 4.98 0 .0153 129492

3 161.3 1,19 0.264 .0035 156.50 0.37 6.86 0.0155 179054

4 206.2 0.99 0.429 .0037 153.80 0,25 8.77 0,0154 229464

5 231.1 1.14 0.540 .0053 152,26 0.21 9.83 0.0155 255430

6 281 .

9

1.94 0,805 .0113 149.66 0.19 11.99 0.0155 312485

7 285.7 0.20 0.794 .0007 .152.89 0.10 12.15 0.0149 314463

8 233.9 0.11 0.540 .0011 154.09 0.16 9.95 0,0151 258407

9 208.6 0.61 0,434 ,0027 154.68 0,13 8.87 0.0153 231100

10 161.4 1.03 0,263 .0035 156.81 0.21 6 . 86 0.0155 179282

11 113.7 0,67 0,133 .0018 159.68 0.30 4.84 0.0158 126983

12 95.0 1.01 0.092 .0021 162.59 0.65 4.04 . 0.0157 106285
29

AISI PIPE FRICTION TESTS PIPE DESIGNATION - 3B BATE ICC 19 & 2 OBSERVERS - JH VB HH

AVE, INNER DIA. - 3.0994 1inches; TAD SEPARATION - 13.635 FEET

RUN TARE GROSS DIVERT MANOMETER HATER STATIC FLOU BIFF. HAZEN PIPE

NO. HT HT TIKE HEIGHT STD. TEMP.

'TEMP. PRESS. RATE PRESS, WILLIAMS REYNOLDS

(RN)' (LB) (LB) (SEC) (INCH) DEV. (DEG C) (DEG C) (PSIA) (GPM) (PSI) COEFF. NUMBER

KANO. FLUID -- HATER BAROMETER -- 74.73 CM OF MERCURY AIR TEMPERATURE - 21.62 DEGREES LlLCIU:.

31 150.8 4151.0 101.074 22.131 0.019 22.80 23,66 120.30 285.4 0,7937 152,71 313577,0

32 147.0 4152.0 101.049 22.132 0.034 22,85 23.74 120.40 285.8 0.7937 152,94 314557,0

33 148.2 4153.0 101,139 22.154 0.020 23.00 23.75 120.30 235.9 0.7945 152,90 314720.0

34 142.3 4153.0 10L.216 22.116 0.047 23.00 23.78 120.40 233.0.7931 152,96 314743.0

35 148.5 4150.0 101.033 22.105 0.041 23.00 23.80 120.40 235.6 0.7928 152,92 314711.0

KANO. FLUID - HATER BAROMETER -- 74.75 CM OF MERCURY AIR TEMPERATURE - oo i nee c*rrc rpi ryjiq

35 143.0 4149.0 p7 noo IjLO » iL7u 15.033 0.036 23.40 23.87 120.10 234.0 0.5391 154,34 258233.0

37 143.6 4143.0 123.204 15.056 0.035 23.40 23.89 120,10 077 0 0.539? 154,03 258117.0

3S 148.3 4147.0 123.28? 15.090 0.05S 23.55 23.91 120.20 233.9 0,5411 153,95 or. 07';.; n

3? 148.8 4144.0 123.091 15.107 0.037 23.55 23.95 120.20 234.1 0.5417 153,93 253729,0

40 147.3 4133.0 123.078 15.053 0.043 23.60 23.98 120.10 233. S 0,5400 154.09 258627.0

KANO; FLUID - HATER BAROMETER -- 74.75 CM OF MERCURY AIR TEMPERATURE - 22,35 DEGREES CELCIUS

41 146.5 3147.0 103.946 12.069 0.063' 23.60 24.01 120,80 203.2 0.4328 154,61 230339.0

42 143.4 3145.0 103.496 12,166 0,066 23,75 24.04 120.10 209.2 0,4362 154,63 ii-iiuZO.O 43 148.2 3144.0 103.930 11,996 0,035 23.80 24.05 121.10 207.8 0,4301 154,83 230145.0

44 147.5 3143.0 103.395 12.163 0.036 23,85 24.03 121.30 203.9 0.4363 154.51 Tiicrzo r\ 4.Jlw>UU» V 45 147.5 3149.0 103.551 12,144 0.034 23.95 24.10 121,10 209.0 0,4354 154.75 071770 A

jlox/ i / \

KANO. FLUID - HATER BAROMETER -- 74.77 CM OF MERCURY AIR TEMPERATURE - 23 DEGREES CELCI'JS 45 146.1 3139.0 133.543 7.342 0.033 23,75 24.14 121.60 161.6 0.2632 157.06 179359.0

47 145.9 3137.0 132.666 7,453 0.092 23.90 24.13 121.90 162,6 0.2674 156,66 130536,0

43 147.0 3139.0 134.632 7.245 0.021 24.20 24.21 121.60 160.3 0.2597 156,87 178113.0

49 147.9 3139.0 134.554 7.242 0.053 24.20 24,23 121,70 160.3 0.2596 156,94 178237,0

50 144.5 3135.0 133.17? 7.414 0.046 24.35 24.25 121.70 161.9 0.2653 156.54

v 180116.0

KANO. FLUID - HATER BAROMETER -- 74.82 CM OF MERCURY AIR TEMPERATURE - 23,18 DEGREES CELCIUS

51 143.5 2128.0 126.261 3.668 0.032 24,25 24,40 119,50 113,1 0.1315 159,83 126149.0 52 151.6 2129.0 125.444 3.703 0.033 24,30 24, 42 119,00 113.7 0.1328 159.93 126339,0

53 147.9 2127.0 125.442 3.735 0,025 24.30 24.44 119.50 113.8 0.133? 159.32 127052.0

54 146.8 2126.0 124.3LS 3.796 0.042 24.55 24,45 119.40 114.8 0.1361 159.37 128234,0

55 147.0 2128.0 126.098 3.682 0.031 24.55 24.47 119.40 113.3 0.1320 159.8? 126591.0

KANO. FLUID - HATER BAROMETER - 74,85 CM OF MERCURY AIR TEMPERATURE - 23,05 DEGREES CELCIUS

55 155.0 2129.0 143.425 2.601 0.045 24.70 24,50 118.80 95.9 0.0932 163.34 107236,0

57 140.1 2126.0 153.333 2.430 0.030 24.55 • 24,52 119.20 93.4 0.033? 163,15 104435.0

58 143.2 2126.0 149.512 2.622 0.044 24.60 24.54 119.20 95.4 0.0940 161.77 106749,0

59 147.9 2123.0 149.054 2.612 0,016 24.65 24.56 119.20 95.6 0.0936 162.33 106975,0

60 146.2 2123.0 150.575 ' 2.569 0.017 24.65 24.53 119.30 94.7 0,0921 162,32 106030,0
30

AISI PIPE FRICTION TESTS

PIPE DESIGNATION — 3B

DATE DEC 19 & 2 OBSERVERS - JH OB MH

AVE

.

INNER DIA. - 3.0994 inches; taf SEPARATION - 13 .635 FEET

GROUP FLOURATE DIFF. PRESS. HAZEN-UILLIAMS VELOCITY FRICTION PIPE

NO. MEAN STD. MEAN STD. MEAN STD. FACTOR REYNOLDS

( GPU ) DEO. ( PSI ) DEO

.

DEO. (FT/SEC) NUMBER

1 99.7 1.43 0.098 .0023 164.87 0.89 4.24 0,0151 109968

OjL. 117.1 . 1.52 0.138 .0035 161 .54 0.67 4.98 0.0153 129492

3 161.3 1.19 0.264 .0035 156.50 0.37 6.86 0.0155 179054

4 206.2 0.99 0.429 .0037 153.80 0.25 8.77 0,0154 229464

5 231.1 1.14 0.540 .0053 152.26 0.21 9.83 0.0155 255430

6 281.9 1.94 0.805 .0113 149.66 0.19 11.99 0.0155 312485

7 285.7 0.20 .0,794 .0007 152.89 0.10 12.15 0.0149 314463

8 233.9 0.11 0.540 .0011 154.09 0.16 9.95 0.0151 258407

9 208.6 0.61 0.434 .0027 154.68 0.13 8.87 0.0153 231100

10 161.4 1.03 0.263 .0035 156.81 0.21 6,86 0.0155 179282

11 113.7 0.67 0.133 .0018 159.68 0.30 4.84 0.0158 126983

12 95.0 1.01 0.092 .0021 162.59 0.65 4.04 . 0.0157 106285
NBS-114A (Rev. »-78)

U.S. DEPT. OF COMM.

BIBLIOGRAPHIC DATA

SHEET

1. PUBLICATION OR REPORT NO. NBSIR 80-2041

»- No.| 3. Reciplfen'r's ' Ac

:c*$s1<m No.

4. TITLE AND SUBTITLE

Friction Losses in Two Sets of Black Steel Pipe of Recent

Manufacture

5. Publication Date May 1980

6. Performing Orgamzation Coa,

7. AUTHOR(S)

J. R. Whetstone

8. Performing Organ. Report No.

9. PERFORMING ORGANIZATION NAME AND ADDRESS

NATIONAL BUREAU OF STANDARDS

DEPARTMENT OF COMMERCE

WASHINGTON, DC 20234

16. Project/Task/Wor

11. Contract/Grant No. 7320577

12. SPONSORING ORGANIZATION NAME AND COMPLETE ADDRESS (Street, City, state, ZIP)

American Iron and Steel Institute

1000 16th Street, N.W.

Washington, DC 20036

13. Type of Report & Period Covered Final

15. SUPPLEMENTARY NOTES

I I Document describes a computer program; SF-185, FIPS Software Summary, is attached.

16. ABSTRACT (A 200-word or leas factual summary of most significant information. If document includes a significant bibliography or

literature survey, mention it here.) Two sets of black steel pipes have been tested at the National Bureau of Standards

(NBS) to determine their frictional loss characteristics. Twenty foot lengths of

pipe furnished by the American Iron and Steel Institute ranging from one to three

inches nominal pipe size were tested using water in the primary flow measurement

facilities at NBS. These facilities use static gravimetric techniques with

precision timing to determine flow rates to within + 0.13% based upon three

standard deviations. Pipe pressure losses were measured using water and mercury

manometers for pipe flow velocities ranging from 4 to 16 feet per second.

Frictional loss characteristics of each pipe characterized using the conventional

Hazen-Williams formulation at each flowrate.

17. KEY WORDS (six to twelve entries; alphabetical order; capitalize only the first letter of the first key word unless a proper name;

separated by semicolons)

Friction factor; Hazen-Williams coefficient.

18. AVAILABILITY : Unlimited

I I For Official Distribution. Do Not Release to NTIS

I I Order From Sup. of Doc., U.S. Government Printing Office, Washington, DC

20402, SD Stock No. SN003-003-

Ixl Order From National Technical Information Service (NTIS), Springfield,

VA. 22161

19. SECURITY CLASS

(THIS REPORT)

UNCLASSIFIED

20. SECURITY CLASS

(THIS PAGE)

UNCLASSIFIED

21. NO. OF

PRINTED PAGES

51

22. Price

$7.00

USCOMM-DC
*