-------
Effluent Monitoring Procedure: Calculation of the Geometric Mean of
Coliform Counts by the Use of Logarithms
An example of the calculations for operating procedure A, B, C, and D follows,
GM (23, 122, 17100) = Anti-log
log 23 + log 122 + log 17100~1
L 3 J
I
(see A5a, 5b, 5c)
GM (23, 122, 17100) = Anti-log
1.36173 + 2.08636 + 4.23300
1
(See procedure B and C)
GM (23, 122, 17100) = Anti-log 2.56036
(See D6c)
GM (23, 122, 17100) = 363.
The following practice problems should be solved to make sure that the program
of action is mastered.
1) GM (1, 4) = *L
2) GM (1, 10, 100) = 10
3) GM (10, 10, 10) = 10
Some checks for gross errors.
1) GM lies between the largest and smallest value. For the problem
GM (23, 122, 17100) = 363 the largest = 17,100 and the smallest = 23.
Since 363 lies between these two, there is no gross error.
2) GM is less than the arithmetic mean* (AM). AM = 23 + 122 + 17100 = 5748.3
3
GM = 363 is less than AM - 5748.3. Hence, there is no gross error.
*GM=AM if all coliform counts are equal as illustrated in practice problem
number 3.
Page No. 9-13
-------
-------
A PROTOTYPE FOR DEVELOPMENT OF
ROUTINE OPERATIONAL PROCEDURES
for the
MEASUREMENT OF FLOW IN AN OPEN CHANNEL BY
PARSHALL FLUME
as applied in
WASTEWATER TREATMENT FACILITIES
and in the
MONITORING OF EFFLUENT WASTEWATERS
Developed by the
Mational Training Center
Municipal Permits and Operations Division
Office of Water Program Operations
U.S. ENVIRONMENTAL PROTECTION AGENCY
EN.FM.EMP.2.4.74 Page No. 10-1
-------
-------
EFFLUENT MONITORING PROCEDURE: Flow Measurement in an Open Channel by
Parshall Flume
"his Procedure was developed by:
Name Charles E. Sponagle
Address EPA, WPO, National Training Center
Cincinnati, Ohio 45268
Position Sanitary Engineer
Education and Technical Background
B.C.E - Manhattan College, 1943
M.S. in C.E. - University of Minnesota, 1948
Professional Registration: State of New York
With Federal Water Pollution Control Program since 1948, with
various assignments at Program Headquarters, Regional Offices,
and Field Stations, including positions as
Staff Engineer, then Chief, Water Quality Section
Denver Regional Office
Staff Engineer, then Regional Construction Grants Program
Director, Denver Regional Office
Regional Construction Grants Program Director,
Cincinnati Regional Office
Director, Colorado River Basin Water Quality Control Project,
Denver Colorado
Industrial Wastes Consultant, Technical Advisory and
Investigations Branch, Cincinnati, Ohio
Participation in and Direction of numerous in-plant industrial
waste surveys and stream studies in New York, Colorado,
New Mexico, Maine, Utah
With National Training Center, September 1969 to date.
Page No. 10-3
-------
EFFLUENT MONITORING PROCEDURE: Flow Measurement in an Open Channel by
Parshall Flume
1. Objective: To enable the student to obtain the flow rate in an open
channel by means of a pre-installed Parshall Flume.
2. Description of Procedure:
The depth of liquid is measured at a stipulated point (or points) within the
Flume. This measurement is then used to obtain the rate of flow in the
channel.
a. This Procedure deals specifically with 6-inch through 8-foot flumes,
since practically all wastewater treatment plant influent and effluent
flows can be measured by flumes of this size. Operating principles of
larger and smaller size flumes are exactly the same. For these latter
however, some differences in procedures are involved, consisting of a
change of location for measurement of the downstream head, and use of
different discharge tables.
b. Flows obtained by visual observation of liquid depth are considered
herein. Use of devices which automatically provide a continuous record
of either head or flow is not included.
General Description of Equipment used in the Procedure:
1) Parshall Flume.
2) Means for visually observing depth of flow, such as a staff gage
or a float gage.
Page No. 10-4
-------
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-------
EFFLUENT MONITORING PROCEDURE: Flow Measurement in an Open Channel by Parshall Flume
TRAINING GUIDE
SECTION TOPIC
I* Introduction
II* Educational Concepts - Mathematics
III* Educational Concepts - Science
IV Educational Concepts - Communications
v* Field & Laboratory Equipment
VI Field & Laboratory Reagents
VII Field & Laboratory Analysis
VIII Safety
IX Records & Reports
*Training guide materials are presented here under the headings marked*.
These standardized headings are used throughout this series of procedures
Page No. 10-9
-------
EFFLUENT MONITORING PROCEDURE: Measurement of Flow in an Open Channel by Parshall Flume
INTRODUCTION
Section I
TRAINING GUIDE NOTE
REFERENCES/RESOURCES
A.2
Flow of a liquid in an open channel can be
measured in many cases by means of a specially-
shaped section known as a Parshall Flume. The flume
can be constructed as part of the channel, or
installed later either temporarily or permanently.
The depth of the flowing liquid is determined at a
specific point, or points, in the flume. The
measured depth, or depths, can then be used to
obtain the rate of flow of the liquid in the channel.
1. Handbook of Hydraulics,
King, H. W., McGraw-Hill
NY, 3rd Ed., 1939
2. Water Measurement Manual
US Dept. of the Interior
Bureau of Reclamation,
Denver, CO, 2nd Ed., 196
3. Hydrographic Data Book,
Stevens, J. C., Leupold
& Stevens, Inc.,
Portland, OR, 8th Ed.
Page No. 10-10
-------
LFFLUENT MONITORING PROCEDURE: Measurement of Flow in an Open Channel by Parshall Flume
EDUCATIONAL CONCEPTS - MATHEMATICS
Section II
TRAINING GUIDE NOTE
REFERENCES/RESOURCES
A.I
Flows - Units of Expression
I. Flow, or Flow Rate, or Discharge.
All of these terms are commonly used to refer
to the quantity of liquid passing a point in
a certain time interval.
II. Quantity of liquid can be expressed in a number
of ways. Common units are the gallon (Gal) and
the cubic foot (cu.ft., ft.3). To change from
one of these measures to another, use the table
below:
Multiply
cu.ft.
Gal.
7.5
0.134
To obtain
Gal.
cu.ft.
III. Flow is usually expressed in these units:
Gallons per minute (GPM)
Million gallons per day (MGD)
Cubic feet per second (cfs, Sec.-ft.)
To change from one of these units to another,
use this table:
Multiply
cfs
MGD
cfs
GPM
0.646
1.55
448.8
0.0022
To obtain
MGD
cfs
GPM
cfs
IV. Flow data is needed to calculate the quantity
of constituents discharged in a plant effluent.
Formulas are--
Ib/day = MGD x mg/1 x 8.34
Kg/day = MGD x mg/1 x 3.78
Page No. 10-11
-------
EFFLUENT MONITORING PROCEDURE: Measurement of Flow 1n an Open Channel by Rarshall
EDUCATIONAL CONCEPTS - MATHEMATICS
Section II
TRAINING GUIDE NOTE
REFERENCES/RESOURCES
C.I
The head Ha is the vertical distance from the
crest of the flume (floor of the converging section)
to the liquid surface, at the stipulated point in the
converging section. Head H^ is the corresponding
distance, as measured at the stipulated point in the
throat of the flume. Both of these measurements are
referenced to the same point, i.e., the elevation of
the crest of the flume. Consequently, all equipment
and devices used to measure these heads roust also be
referenced to the crest elevation.
When a staff gage is used to obtain these heads,
it may be attached to the inside face of the flume,
or placed in a stilling well. In the former case,
only an approximate head determination is usually
possible, because of waves and rapid water level
fluctuations at the upstream gage, and turbulent
conditions at the downstream gage.
Determination of head using the staff gage is
illustrated below for the various conditions which
will be met.
Case I - Initialgage mark 0.00 ft.
The gage may be installed in either of three
positions, as shown in Fig. 1.
LIQUID
SURFACE
CREST
-0.20
///?
0.40
0.20
A. B. C.
FIG. 1 - STAFF GAGE SETTINGS
Page No. 10-12
-------
FFLUENT MONITORING PROCEDURE: Measurement of Flow in an Open Channel by Parshall Flume
EDUCATIONAL CONCEPTS - MATHEMATICS
Section II
TRAINING GUIDE NOTE
REFERENCES/RESOURCES
C.I
(cont.)
In "A", the bottom of the gage is set at crest
elevation. The intersection of the liquid surface
with the gage gives a direct reading of the head.
Here, the head is 0.30 ft.
In "B" the bottom of the gage is set some dis-
tance "d" above crest elevation. To obtain the
head, "d" must be added to the gage reading. For
example, if "d" in the Figure equals 0.25 ft., then
the head is 0.25 + 0.20, equals 0.45 ft.
In"C" the bottom of the gage is set some dis-
tance (say 0.20 ft) below crest elevation. This
must be subtracted from the gage reading to obtain
the head. Thus, 0.40-0.20 = 0.20 ft., which is the
head.
Case II - Initial gage mark other than 0_.0_0 ft.
The mark at which the gage divisions start must
be taken into account in determining the head. For
example, if a gage section starting at 3.33 ft.
instead of 0.00 ft. is used, the calculations are
as follows for the three conditions shown in
Fig. 2 (which correspond to tho.se of Fig. 1):
LIQUID
SURFACE
CREST
3.63
3.33 j:
A. B. C.
FIG. 2 - STAFF GAGE SETTINGS
In "A", head = 3.63-3.33 = 0.30 ft.
In "B", assuming that "d" = 0.25 ft., head =
(3.53 + 0.25)-3.33 = 0.45 ft.
In "C", head = 3.73-3.53 = 0.20 ft.
Page No. 10-13
-------
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-------
EFFLUENT MONITORING PROCEDURE: Measurement of Flow in an Qpen Channel by Rarshall Flume
EDUCATIONAL CONCEPTS - MATHEMATICS
Section II
TRAINING GUIDE NOTE
REFERENCES/RESOURCES
C.2
With Ha determined, the flow can be obtained
from a Table such as that shown in Table 1. (This
shows the head-discharge relationships for flumes
ranging in size from 6 to 24 inches. Similar tables
for larger and smaller flumes will be found in
References 1,2, and 3).
The flow is obtained from this Table as follows
1. Go vertically downward in the column titled
"Head" until you reach the value for the Ha
measured. Note that values of Head in this
column are given both in feet, and in inches
corresponding to the foot values.
2. Proceed horizontally to the right until you
reach the columns for the throat width of
flume in use.
3. Read the flow in the units to be reported.
The flow is given in three units in this
Table: sec.-ft. (cubic feet per second);
GPM (gallons per minute), and MGD (million
gallons per day). Example:
For a 12" flume, with Ha = 0.86 ft.
1. Locate 0.86 ft. in the "Head" column.
2. Go over horizontally to the right to the
columns under the "12" throat width.
3. Read flow: 3.18 sec.-ft., or
1427 GPM, or
2.06 MGD
4. Water and Sewage Works,
Reference & Data Section,
1954, p. R-277
Page No. 10-15
-------
EFFLUENT MONITORING PROCEDURE: Measurement of Flow in an Qpen channel by parsha]1
EDUCATIONAL CONCEPTS - MATHEMATICS
Section II
TRAINING GUIDE MOTE
REFERENCES/RESOURCES
D.I
A float gage is shown in Fig. 3, installed in a
stilling well for measurement of HL. To illustrate
the calculation of Ha it "is assumed that the floor
of the stilling well is at the same elevation as the
PULLEY
FLOAT
INDEX
1 FOOT
FIG .3 - FLOAT GAGE INSTALLATION
crest of the flume, and that the liquid is flowing
in the flume with a depth of one foot. The float
will, of course, be resting on the surface of the
liquid in the well, and it is also assumed that for
the condition illustrated the tape division opposite
the float index reads 8-1/2 feet.
With the specific relations established for
this one condition, the gage can now be "zeroed" so
that Ha can be obtained for any other condition, as
follows:
(a) A reading of 8-1/2 feet on the tape corre-
sponds to an Ha of one foot. Consequently,
a reading of 7-1/2 feet on the tape corre-
sponds to an Ha of zero feet, or to the
crest elevation.
(b) Therefore Ha can be obtained for any depth
of flow by subtracting 7-1/2 feet from the
observed tape division opposite the index.
The following points should be noted in connec-
tion with this procedure:
(a) If the elevation of the index is changed,
the gage must be re-zeroed.
Page No. 10-16
-------
'.FFLUENT MONITORING PROCEDURE: Measurement of Flow in an Open Channel by Parshall Flume
EDUCATIONAL CONCEPTS - MATHEMATICS
Section II
TRAINING GUIDE NOTE
REFERENCES/RESOURCES
D.I
(cont.)
E.3.2
(b) If the position of the tape on the pulley is
changed, the gage must be re-zeroed.
(c) The tape must be installed so that the
numerical value of the tape reading
increases as the depth of flow increases.
Hfj can be obtained with the float gage in the
same manner as described above for Ha.
Discharge through the flume is not reduced from
the free-flow value until the percent submergence
equals or exceeds the following values:
60% for 6- inch and 9- inch flumes
70% for 1 foot to 8-foot flumes
When the submergence reaches these values, a
corrected flow must be calculated in the following
manner:
For 6-inch and 9-inch Flumes
The corrected flow can be obtained directly
from Fig. 4 for a 6-inch flume, and from Fig. 5 for
a 9-inch flume. Example: For a 6-inch flume,
= 0.8 ft.
x 100 = 80%
Ha = 1.0 ft. ,
% Submergence =
Refer to Fig. 4. On "Percent of submergence"
scale on left-hand side, go up to the "80"
value.* Move to the right along the "80" line to
where it intersects the "Ha = 1.0 feet" curve.
Drop vertically from the point of intersection
to the "Discharge, Second-feet" scale along the
bottom of the chart.
Read 1.7 - this is the discharge in cubic feet
per second through the flume. Convert flow to
other units if desired.
Exactly the same procedure would be followed for a
9-inch flume, using Fig. 5.
Ref. 1
Page No. 10-17
-------
EFFLUENT MONITORING PROCEDURE: Measurement of Flow in an Open Channel by Parshall Flume
UPSTREAM HEAD Ho, FEET
0 02 04 06 08 1.0 12 14 16 18 20 2.2 24 26 2.8 1.0 J.Z 34 5.6 3.8 4.O
DISCHARGE, SECOND-FEET
FIG. 4 — Diagram for determining rate of submerged flow for a 6-inch Parshall flume. 103-D-897. (Courtesy U.S.
Soil Conservation Service.)
UPSTREAM hE-AD Ha, FEET
•a 9 t
96
/r
/4 i-
-yU
t
f___onjp_
*y
10 1.5 20 25 30 35
DISCHARGE, SECOND-FEET
40 45
55 60
FIG. 5 — Diagram for determining rate of submersed flow for a 9-inch Parshall flume. 103-D-898. (Courtesy U.S.
Soil Conservation Service.)
Page No. 10-18
-------
EFFLUENT MONITORING PROCEDURE: Measurement of Flow in an Open channel by Rarshall F]ume
EDUCATIONAL CONCEPTS - MATHEMATICS
Section II
TRAINING GUIDE NOTE
REFERENCES/RESOURCES
E.3.2
(cont.)
For Flumes 1 foot to 8 feet wide
Use Fig. 6. This provides a correction factor
to be applied to the discharge obtained using Ha
and Table 1, the free-flow discharge table. For
flumes larger than 1 foot a second correction, using
a "multiplying factor" is necessary. Example 1.
For a 1-foot flume,
Hh = 0.8 ft., Ha = 1.0 ft.
Submergence =
x 100 = 80%
1.0
Refer to Fig. 6. On "Upstream Head Hfl" scale
at left-hand side, go up to 1.0 ft. Move to
the right along the "1.0 ft." line to where
it intersects the "80% Submergence" curve.
Drop vertically from the point of intersection
to the "Correction, second-feet" scale at the
bottom of the chart. Read "0.35 sec.-ft."
Refer to Table 1. For a 12-inch flume with
Ha = 1.0 ft., discharge is 4.00 sec.-ft. But
the actual discharge will be less than this,
since submergence exceeds 70%. To get actual
discharge, subtract correction obtained from
Fig. 6. Then the discharge is 4.00-0.35
= 3.65 sec.-ft.
Note that "Multiplying Factor" is 1.0, so the
correction factor obtained from Fig. 6 is
used directly.
Example 2
For a 24- inch flume,
Hb = 1.23 ft., Ha = 1.30 ft.
Submergence =
1.30
x 100 = 95%
Refer to Fig. 6. On left-hand scale go up to
1.30 ft., which is the Upstream Head Ha.
Page No. 10-19
-------
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-------
EFFLUENT MONITORING PROCEDURE: Measurement of Flow in an Open Channel by Parshall Flume
EDUCATIONAL CONCEPTS - MATHEMATICS
TRAINING GUIDE NOTE
REFERENCES/RESOURCES
E.3.2
(cont.)
Proceed horizontally to the right along the
"1.30 ft." line. The-point of intersection of
this line with the "95% Submergence" curve is to
be located. Since no curve is drawn on Fig. 6
for this value of submergence, mentally locate a
point on the "1.30 ft." line which is midway
between the "94% submergence" and the "96% sub-
mergence" curves.
Drop vertically from this point to intersect the
"Correction, second-feet" scale at the bottom of
the chart. Read "2.7".
From the Table at right side of chart on Fig. 6,
read the "Multiplying Factor" for a 24-inch
flume. This factor is 1.8.
Multiply. 2.7 x 1.8 = 4.9 sec.-ft. This is the.
correction factor to be used in this case.
From Table 1 obtain free-flow discharge of 12.0
sec.-ft. for a 2-foot flume with Ha = 1.30 ft.
Subtract correction factor from this free-flow
value to obtain discharge with this degree of
submergence.
Discharge = 12.0 - 4.9 = 7.1 sec.-ft.
Page No. 10-21
-------
EFFLUENT MONITORING PROCEDURE: Measurement of Flow in an Open Channel by Parshall Flume
EDUCATIONAL CONCEPTS - SCIENCE
Section III
TRAINING GUIDE NOTE
REFERENCES/RESOURCES
B.I.I
B.I.3
B.I.4
The Parshall Flume is intended for use- as an
in-line structure in an open channel where reason-
ably smooth flow, uniformly distributed across the
cross-section-, is the normal condition.
A good degree of accuracy cannot be maintained
if poor approach conditions exist in the approach
channel. Experience has shown that Parshall Flumes
should not be placed at right angles to flowing
streams unless the flow is effectively straightened
and uniformly redistributed before it enters the
flume. Surges and waves of any appreciable size
should be eliminated.
The liquid should enter the converging section
reasonably well distributed across the entrance
width, and the flowlines should be essentially
parallel to the flume centerline. Flow at the flume
entrance should be free of "white" water and free
from turbulence in the form of visible surface
boils. Only then can the flume measure flow as
intended.
The velocity of flow through the flume will
generally be sufficiently great to virtually
eliminate any deposition of sediment within the
structure. If any such build-up is observed,
however, it should be eliminated. Deposits should
also be removed from the channel upstream and down-
stream of the flume.
The flow condition can be determined from
measurements of Ha and Hu. Generally, however,
these heads do not have to be measured—the condition
of flow through the flume can usually be determined
by visual observation.
Three flow conditions through the flume are
shown in Fig. 7.
Ha
FIG. 7 - FLOW CONDITIONS
Page No. 10-22
-------
EFFLUENT MONITORING PROCEDURE: Measurement of Flow in an Qpen Channel by Rarshall
EDUCATIONAL CONCEPTS - SCIENCE
Section III
TRAINING GUIDE NOTE
REFERENCES/RESOURCES
B.I.4
(cont.)
B.I.5
In flow condition 2, there is a drop in the
elevation of the liquid surface, followed by an
abrupt rise in the throat-. This phenomenon is
referred to as a hydraulic jump or standing wave.
When the hydraulic jump is present, free-flow
conditions exist.
In flow condition 1, there is a substantial and
smooth drop in the elevation of the liquid surface
as it passes through the throat and the diverging
section of the flume. Free-flow conditions exist.
A hydraulic jump will be observed downstream of
the flume.
Flow condition 3 illustrates the configuration
of the liquid surface for submerged-flow conditions.
Sometimes a series of waves or ripples will be noted
in the transition area between the upstream and
downstream liquid elevations. These also indicate
that submerged-flow conditions exist.
Flumes used in treatment plants are selected
to operate under free-flow conditions over the
range of flows handled at the plant. The existence
of a submerged-flow condition would therefore be
most unusual, and might be due either to the flume
being too small, or to some obstruction in the
channel downstream of the flume which is raising the
water level. In any case, it is important to
determine the reason for a submerged flow condition,
and take the appropriate steps to return the flume
to free-flow operation.
For a stilling well to function properly, the
opening or pipe between the well and the flume must
be kept free of deposits or materials which would
interfere with the free movement of liquid. This
should be checked occasionally, and any such inter-
ferences removed by flushing with clean water, or
by some other suitable procedure. Deposits or
floating materials in the well should also be
removed to maintain accurate head measurement.
Page No. 10-23
-------
EFFLUENT MONITORING PROCEDURE:
Measurement of Flow in an Open Channel by Parshall Flume
FIELD & LABORATORY EQUIPMENT
Section V
TRAINING GUIDE NOTE
REFERENCES/RESOURCES
A.3
Two drawings of a Parshall Flume are shown in
Fig. 8. The top (Plan) drawing shows the appear-
ance of the flume when viewed from above. The
drawing labeled "Section L-L" is the way the flume
looks when viewed from the side, along the line
marked "L-L" in the top drawing.
CONVERGING DIVERGING
SECTION SECTION//-
THROAT SECTION ://
Ha,
>
L*L
I
WING WALL
PLAN
STILLING WELL
FLOW CREST
ASLOPE '/4-t sIL-^gp
WATER SURFACE, S
SECTION L-L
FIG. 8 - PARSHALL FLUME
The flume structure proper consists of three
sections:
1. A converging section
2. A throat section having parallel walls
3. A diverging section
Wingwalls are shown in Figure 8 immediately
upstream and downstream of the flume. The function
of these is to provide a gradual width transition
between the channel and the flume. The flume can be
made of concrete, galvanized steel, or other suitable
material. Flumes must be built to specific dimen-
sions and close tolerances governed by throat width,
for satisfactory performance. The floor of the
converging section must be level if the flume is to
operate properly.
Page No. 10-24
-------
EFFLUENT MONITORING PROCEDURE: Measurement of Flow in an Open Channel by Parshall Flume
FIELD & LABORATORY EQUIPMENT
Section V
TRAINING GUIDE NOTE
REFERENCES/RESOURCES
A.4
Throat Width
Distance between the walls of the throat section.
Flume Size
Flumes are designated as to size by the throat width,
as a "6-inch flume", a "10-foot flume", etc.
Flume Crest
Floor of the converging section. Sometimes indicated
as the junction point of the floor of the converging
section with the throat section.
Crest Elevation
Elevation of the floor of the converging section.
Upstream Head (Ha)
Depth of liquid over the flume crest, measured back
from the crest of the flume at a distance equal to
two-thirds of the length of the converging section. •
Downstream Head
Depth of liquid over the flume crest, measured at a
stipulated distance upstream of the beginning of the
diverging section. Varies with size of flume. For
flumes considered in this guide (i.e. 6-inch to-
8-foot flumes), the point of measurement is two
inches upstream of the beginning of the diverging
section (dimension "x", Fig. 8).
Stilling Well (Float Well)
A chamber connected by a small inlet to the liquid
flowing in an open channel, which provides quiescent
conditions so as to secure good records of water
levels. Waves and surges occuring in the flowing
liquid do not appear in the well. Liquid level in
the well does, however, follow all the steady
fluctuations of the flowing liquid.
Free Flow
A condition of flow through the flume which occurs
when the depth of liquid downstream of the crest is
insufficient to reduce the discharge rate.
Submerged Flow
A condition of flow through the flume which occurs
when the depth of liquid downstream of the crest is
sufficient to reduce the discharge.
Submergence
The ratio Hb
usually expressed as a percentage.
Page No. 10-25
-------
EFFLUENT MONITORING PROCEDURE: Measurement of Flow In an Open Channel by Parshall Flume
FIELD & LABORATORY EQUIPMENT
Section V
TRAINING GUIDE MOTE
REFERENCES/RESOURCES
A.5
A.6
The Parshall Flume is a specially-shaped flow
section, so constructed and installed that the rate
of flow through it depends only on its size (throat
width), and the depth of liquid over the crest.
Discharge through the flume can occur for two condi-
tions of flow:
1. Free Flow, in which the discharge depends
only on the upstream head Ha. When free-flow
conditions exist, discharge through the
flume can be obtained by measuring the
upstream head only.
2. Submerged Flow, in which the discharge is
reduced due to the effect of the depth of
liquid downstream of the flume. Irt this
case it is necessary to measure both the
upstream head Ha and the downstream head H&
in order to obtain the discharge.
A staff gage (Fig. 9) is a graduated scale,
usually installed vertically, for obtaining liquid
depth, or head. An observer notes the scale
division at which the liquid surface intersects the
7-=
B-i
5-f
4-f
3-5
8-j
FIG. 9 - STAFF
GAGE SECTION
The head and discharge can then
gage (gage height).
be calculated.
Commercially-available gages are made of 18-gage
metal coated with a substantial thickness of porce-
lain enamel. The face of the gage is white;
numerals and graduations are black. Gages are avail-
able in several styles; in widths from 2-1/2 to 4
inches, in lengths from 1 to 5 feet, and with gradua-
tions of 0.1, 0.01, or 0.02 feet. A gage divided in
metric units is also commercially available.
Page No. 10-26
-------
IFFLUENT MONITORING PROCEDURE: Measurement of Flow in an Open Channel by Parshall Flume
FIELD & LABORATORY EQUIPMENT
Section V
TRAINING GUIDE NOTE
REFERENCES/RESOURCES
A.7
A float gage (Fig. 10) is a means of continu-
ously indicating liquid levels. It consists of a
metal float, a pulley mounted on a standard, and a
counterweight. A graduated stainless steel tape is
Fig. 10 - Float Gage
attached to the float and connected at the other
end to the counterweight. The float follows the
rise and fall of the liquid surface and the level
can be read from the tape and a pointer or reference
mark. Tapes are available in selected lengths, and
are graduated either in feet, tenths and hundredths
for English measurements, or meters, decimeters and
centimeters for metric measurements.
The float gage is used extensively as a refer-
ence gage in stilling wells to check the accuracy
of automatic head or flow recording devices.
Page No. 10-27
-------
-------
A PROTOTYPE FOR DEVELOPMENT OF
ROUTINE OPERATIONAL PROCEDURES
for the
MEASUREMENT OF FLOW IN AN OPEN CHANNEL BY
SHARP-CRESTED WEIR
as applied in
WASTEWATER TREATMENT FACILITIES
and in the
MONITORING OF EFFLUENT WASTEWATERS
Developed by the
National Training Center
Municipal Permits and Operations Division
Office of Water Program Operations
U.S. Environmental Protection Agency
EN.FM.EMP.1.11.74 Page No. 11-1
-------
-------
Effluent Monitoring Procedure: Measurement of Flow in an Open Channel by
Sharp-Crested Weir
This Procedure was developed by:
NAME Charles E. Sponagle
ADDRESS EPA, WPO, National Training Center, Cincinnati, OH 45268
POSITION Sanitary Engineer
EDUCATION AND TECHNICAL BACKGROUND
B.C.E. - Manhattan College, 1943
M.S. in C.E. - University of Minnesota, 1948
Professional registration, New York State
With Federal Water Pollution Control Program since
1948, with various assignments at Program Headquarters,
Regional Offices, and Field Stations, including positions
as
Staff Engineer, then Chief, Water Quality Section,
Denver Regional Office
Staff Engineer, then Regional Construction Grants
Program Director, Denver Regional Office
Regional Construction Grants Program Director,
Cincinnati Regional Office
Director, Colorado River Basin Water Quality
Control Project, Denver, Colorado
Industrial Wastes Consultant, Technical Advisory
and Investigations Branch, Cincinnati, Ohio
Participation in and Direction of numerous in-plant
industrial waste surveys and stream studies in New
York, Colorado, New Mexico, Maine, Utah
With National Training Center September 1969 to date.
Page No. 11-3
-------
Effluent Monitoring Procedure: Measurement of Flow in an Open Channel by
Sharp-Crested Weir
1. Objective:
The student will be able to make an acceptable measurement of flow rate
in an open channel by means of a preinstalled sharp-crested weir and
vertical staff gage or a float gage.
2. Brief Description of Procedure:
The depth of liquid producing flow over a weir is measured. This measure-
ment is used to obtain the rate of flow in the channel at the time the
observation was made.
General Description of Equipment used in the Procedure:
1. A Weir over which the liquid flows.
2. Means for visually observing depth of liquid flow, such as a staff gage or
a float gage.
Page No. 11-4
-------
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