Discharge
Characteristics
of
Triangular-notch
Thin-plate
Weirs
GEOLOGICAL
SURVEY
WATER-SUPPLY
PAPER
16I7-B
Discharge
Characteristics
of
Triangular-notch
Thin-plate
Weirs
By
JOHN
SHEN
STUDIES
OF
FLOW
OF
WATER
OVER
WEIRS
AND
DAMS
GEOLOGICAL
SURVEY
WATER-SUPPLY
PAPER
1617-B
A
comprehensive
study
of
the
discharge
characteristics
of
triangular-notch
thin-plate
weirs
UNITED
STATES
GOVERNMENT
PRINTING
OFFICE,
WASHINGTON
:
1981
UNITED
STATES
DEPARTMENT
OF
THE INTERIOR
JAMES
G.
WATT,
Secretary
GEOLOGICAL
SURVEY
Doyle
G.
Frederick,
Acting
Director
Library
of
Congress
Cataloging
in
Publication
Data
Shen,
John.
Discharge
characteristics
of
triangular-notch
thin-plate
weirs.
Geological
Survey
water-supply
paper
;
1617-B
Bibliography:
p.
Supt.
of
Docs,
no.:
I
19.13:1617-B
1.
Wiers.
2.
Stream
measurements.
I.
Title.
II.
Series:
United
States.
Geological
Survey.
Water-supply
paper;
1617-B.
TC175.S5625
551.48'3'0287
80-607045
For
sale
by
Superintendent
of
Documents,
U.S.
Government
Printing
Office
Washington,
D.C.
20402
PREFACE
An
initial
draft
of
the
report
on
the
discharge
characteristics
of
tri-
angular-notch,
thin-plate
weirs
was
prepared
in
1960.
In
draft
form
it
was
the
basis
for
the
development
of
recommended
flow-measurement
standards. In
1974,
the
discharge
equation
and
the
coefficients
of
discharge
proposed
in
the
report
were
adopted
as
part
of
an
interna-
tional
standard.
The
equation
and
coefficients
have
been
quoted
exten-
sively
in
several
foreign
national
standards,
books,
and
reports.
In
its
present
revised
form,
the
report
provides
background
and
verification
for
the
triangular-notch
weir
as
a convenient,
reliable,
and
inexpensive
device
for
measuring
small
flows
in
open
channels.
in
CONTENTS
Page
Preface
________________________________________
III
Symbols_______________________________________
VII
Abstract
_______________________________________
B1
Introduction
_____________________________________
1
Description
of
the
weir
______________________________
2
Basic
equation
of
discharge
____________________________
3
Dimensional
analysis
________________________________
4
Significance
of
the
ratios
in
equation
3
______________________
5
Coefficient
of
discharge
for
one liquid
_____________________
5
Modified
equations
for
one
liquid
_________________________
6
Review
of
the
literature
________________________________
7
Thomson's
experiments
______________________________
7
Barr's
experiments
_________________________________
8
Barr-Strickland
formula
____________________________
8
Cone's
experiments
_________________________________
9
Yarnall's
experiments
_______________________________
10
Greve's
experiments
______________________________
10
Lenz's
experiments
_______________________________
11
Experiments
of
Numachi,
Kurokawa,
and
Hutizawa
_____________
13
Other
experiments
_______________________________
13
Summary
____________________________________
15
Analysis
of
data
___________________________________
16
Evaluation
of
k
h
__________________________________________________
16
An
alternative
for
k
h
______________________________________________
19
Evaluation
of
C
e
_________________________________________________
22
Influence
of
h/P
and
PIB
___________________________________________
30
Comparison
of
formulas
______________________________
30
Basis
of
comparison
______________________________
30
90°-notch
weir
___________________________________
32
Other
notch
angles
_______________________________
32
Conclusions
_____________________________________
32
References
_____________________________________
39
Supplemental information
_____________________________
41
Requirements
for
precise
measurements
___________________
42
Specifications
for
installation
_______________________
42
Restrictions
on
the
geometric
parameters
________________
42
Restrictions
on
h
and
P
_________________________________________
42
Effect
of
neglecting
k
h
_________________________________________
42
Effect
of
approach-channel
conditions
___________________
43
Measurement
of
6
_____________________________________________
44
Measurement
of
h
_____________________________________________
44
Determination
of
gage
zero
________________________
44
VI
CONTENTS
ILLUSTRATIONS
Page
FIGURE
1.
The
triangular-notch,
thin-plate
weir
_________________
B3
2.
Evaluation
of
k
h
illustrated
with
Numachi,
Kurokawa,
and
Hutizawa
data
(v
=
90°)
_____________________________
17
3.
Evaluation
of
k
h
illustrated
with
Lenz
data
_____________
18
4-11.
Values
of:
4.
k
h
as
a
function
of
v
__________________
20
5.
k
as
a
function
of
v
_____________________-
21
6.
C
e
,
notch
angles
approximately
120°
__________
23
7.
C
e
,
notch
angles
approximately
90°
_________
24
8.
C
e
,
notch
angles
approximately
60°
________
25
9.
C
e
,
notch
angles
approximately
45°
______
26
10.
C
e
,
notch
angles
approximately
27°
_______
27
11.
C
e
,
notch
angles
of
10°
and
13°
_______________
28
12.
Coefficient
of
discharge
C
e
as
a
function
of
v
___________
29
13.
Coefficient
of
discharge
C
e
as
a
function
of
h/P
and
P/B
(v
=
90
°)
___
31
14-19.
Comparisons
of
formulas
for:
14.
90°-notch
weir
________________________
33
15.
Notch
angles
of
approximately
120°
______
34
16.
Notch
angles
of
approximately
60°
_____
35
17.
Notch
angles
of
approximately
45°
__________
36
18.
Notch
angles
of
approximately
27°
______
37
19.
Notch
angles
of
approximately
10°
_________
38
20.
Effect
of
using
h
instead
of
h
e
in
equation
6
____________
43
TABLES
TABLE
1.
Scope
of
Greve's
experiments
______________
Bll
2.
Scope
of
Lenz's
experiments
with
water
____________
12
3.
Values
ofN
and
a
for
equation
16
(Lenz)
______
13
CONVERSION
FACTORS
The
inch-pound
system
of
units
is
used
throughout
this
report.
The
following
factors
may
be
used
to
convert
inch-pound
units
to
International
System
of
Units
(SI):
Multiply
inch-pound
units
By
ft
(feet)
in
(inch)
ft
2
(square
feet)
Length
0.30480
25.4
Area
0.09290
To
obtain
SI
units
m
(meters)
mm
(millimeters)
m
2
(square
meters)
CONTENTS
VII
Multiply
inch-pound
units
By
To
obtain
SI
units
Volume
ft
3
(cubic
feet)
0.02832
m
3
(cubic
meters)
Temperature
°F
(degrees
Fahrenheit)
5/9
(°F-32)
°C
(degrees
Celsius)
SYMBOLS
a
exponent
in
equation
16
b
width
of
rectangular
notch
B
width
of
approach
channel
C
coefficient
of
discharge
C
e
coefficient
of
discharge
(based
on
effective
head)
E
relative
error
g
acceleration
due
to
gravity
h
piezometric
head
referred
to
vertex
of
notch
h
e
effective
head
j
exponent
in
equation
9
h
adjustment
quantity
h
h
head-adjustment
quantity
L
a length
M
coefficient
in
equation
12
m
exponent
in
equation
12
N
coefficient
in
equation
16
n
exponent
in
equation
12
P
height
of
weir
notch
above
bottom
of
channel
Q
discharge
R
Reynolds
number
S
slope
of
sides
of
notch
W
Weber
number
7
specific
weight
6
included
angle
between
sides
of
notch
H
dynamic
viscosity
p
density
a
surface tension
STUDIES
OF
FLOW
OF
WATER
OVER
WEIRS
AND
DAMS
DISCHARGE
CHARACTERISTICS
OF
TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
By
JOHN
SHEN
ABSTRACT
The
triangular-notch,
thin-plate
weir
is
a
convenient,
inexpensive,
and
relatively
precise
flow-measuring
instrument.
It
is
frequently
used
to
measure
the
flow
of
water
in
laboratories
and
in
small,
natural
streams.
This
report
includes
an
extensive
review
of
the
literature
and
presents
a
comprehensive
analysis
of
the
discharge
characteristics
of
triangular-notch
weirs.
Previously
published
data
are
analyzed
in
the
light
of
the
effective-head
concept,
and
a
new
discharge formula
is
proposed.
Coefficients
are
recom-
mended
and
requirements
for
precise
measurements
are
described.
Limits
of
applicabili-
ty
are
discussed.
INTRODUCTION
The
triangular-notch,thin-plate
weir
is
used
widely
for
measuring
the
flow
of
liquids
in
flumes
and
open
channels.
Simple
in
design
and
easily
made
from
readily
available
materials,
it
is
inexpensive,
convenient
to
use,
and
easy
to
maintain.
In
permanent
or
portable
form
it
is
frequent-
ly
used
to
measure
the
flow
of
water
in
laboratories
and
in
small,
natural
streams.
When
several
forms
of
weirs
or
flumes
might
be
used,
the
triangular-notch
weir
is
often
preferred
because
of
its
greater
ac-
curacy
at
low
flows
or
its
lesser
sensitivity
to
approach-channel
geometry
and
velocity
distribution.
Within
the
range
of
conditions
for
which
verification
data
are
adequate, and
with
reasonable
care
in
its
construction, installation,
and
use,
the
triangular-notch,
thin-plate
weir
is
a
relatively
precise
instrument.
The
triangular-notch
weir
has
been
the
subject
of
considerable
ex-
perimental
research
and
published
discussion.
Unfortunately,
however,
most
of
the
laboratory
investigations
have
been
restricted
to
a
narrow
range
of
notch
angles
and
channel
geometries.
The
90°-notch
weir
has
been
most
extensively
studied.
With
few
exceptions,
water
has
been
the
liquid
used
in
laboratory
tests.
A
large
number
of
empirical
discharge
formulas
have
been
proposed
for
triangular-notch
weirs.
Most
of
these
were
designed
to
fit
a
par-
Bl
B2
FLOW
OF
WATER
OVER
WEIRS
AND
DAMS
ticular
set
of
experimental
data.
None
provides
a
comprehensive
solu-
tion,
even
for
a
single
liquid.
Deficiencies
in
these
formulas
are
con-
cealed
with
numerous
limits
of applicability
which
greatly
restrict
their
usefulness.
This
report
presents
a
comprehensive
analysis
of
the
discharge
characteristics
of
triangular-notch,
thin-plated
weirs.
Previously
published
data
from
various
sources
have
been
reanalyzed,
and
some
of
the
traditional
discharge
formulas
are
compared
with
an
original
solu-
tion.
The
report
is
based
on
one
of
a
series
of
studies
of
weirs
and
spillways
which
was
undertaken
by
the
U.S.
Geological
Survey
under
the
direction
of
C.
E.
Kindsvater.
Previously
published
reports
in
the
series
are
concerned
with
broad-crested
weirs
(Tracy,
1957),
rec-
tangular,
thin-plate
weirs
(Kindsvater
and
Carter,
1959),
and
embankment-shaped
weirs
(Kindsvater,
1964).
Portions
of
this
report
are
adapted
from
unpublished
reports
and
drafts
of
weir
standards
prepared
by
C.
E.
Kindsvater.
DESCRIPTION
OF
THE
WEIR
The
weir
which
is
the
subject
of
this
study
is
a
symmetrical,
V-shaped
notch
in
a
vertical
thin
plate.
The
line
which
bisects
the
angle
of
the
notch
is
vertical
and
equidistant
from
the
sides
of
the
approach
chan-
nel.
The
weir
plate
is
smooth,
plane,
and
perpendicular
to
the
sides
as
well
as
the
bottom
of
the
approach
channel.
Figure
1
shows
a
triangular-notch,
thin-plate
weir
installed
at
the
end
of
a
rectangular
channel.
The
crest
surfaces
of
the
weir
notch
are
plane
surfaces
which
form
sharp,
right-angle
corners
at
their
intersection
with
the
upstream
face
of
the
weir
plate.
The
width
of
the
crest
surface
varies,
but
it
is
general-
ly
between
1/32
and
1/16
inch.
If
the
weir
plate
is
thicker
than
1/16
inch,
the
downstream
edges
of
the
notch
are
chamfered
to
make
an
angle
of
not
less
than
45°
with
the
surface
of
the
crest.
Ideally,
the
channel
upstream
from
the
weir
is
straight,
smooth,
horizontal,
rec-
tangular,
and
of
sufficient
length
to
develop
the
normal
(uniform
flow)
turbulence
and
velocity
distribution
for
all
discharges.
Usually,
however,
it
is
less
than
ideal,
and
baffles
or
screens
are
provided
in
order
to
simulate
a
normal
velocity
distribution.
Channel
and
tailwater
conditions
downstream
from the
weir
are
such
as
to
permit
a
free,
fully
ventilated
flow
from
the
notch.
Provisions
for
ventilation
ensure
that
pressure
on
the
nappe
surfaces
is
atmospheric.
The
tailwater
is
low
enough
that
it
does
not
interfere
with
the
ventilation
of
the
nappe
or
free
flow
from the
notch.
The
head
on
the
weir
is
the
measured
vertical
distance
from
the
water
surface
to
the
vertex
of
the
notch.
The
head-measuring
section
is
located
a
sufficient
distance
upstream
from
the
weir
to
avoid
the
region
of
surface
draw-down,
and
it
is
sufficiently
close
to
the
weir
that
the
DISCHARGE
OVER
TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
B3
Upstream
face
of
weir
plate
^45°
FIGURE
l.-The
triangular-notch,
thin-plate
weir.
energy
loss
between
the
measuring
section
and
the
weir
is
negligible.
A
distance
of
4
to
5
h
is
recommended.
BASIC
EQUATION
OF
DISCHARGE
The
traditional
equation
of
discharge
for
triangular-notch
weirs
is
derived
on
the
basis
of
an
assumed
analogy
between
the
weir
and
the
B4
FLOW
OF
WATER
OVER
WEIRS
AND
DAMS
orifice.
In
the
derivation,
an
approximate
velocity
equation
is
in-
tegrated
over
assumed
area
limits
of
the
nappe
in
the
plane
of
the
weir.
The
result
is
an
equation
which
is
useful
mainly
because
it
is
dimen-
sionally
correct
and
because
it
is
used
almost
universally
as
the
basis
for
the
analysis
of
experimental
data.
It
is
used
herein
as
the
basic
equation
of
discharge.
In
its
traditional
form,
the
basic
discharge
equation
is
Q=CV20
tan
*60
(1)
lo
£
in
which
Q
is
the
volume
rate
of
flow
or
discharge
in
cubic
feet
per
sec-
ond;
C is
the
nondimensional
coefficient
of
discharge;
g
is
the
accelera-
tion
due
to
gravity
in
feet
per
second
per
second;
0
is
the
angle
included
between
the
sides
of
the
notch,
usually
measured
in
degrees;
and
h
is
the
potentiometric
head
or
height
of
the
upstream
liquid
surface
measured
with
respect
to
the
vertex
of
the
notch,
in
feet
(in
metric
units,
discharge
would
be
stated
in
cubic
meters
per
second,
head
in
meters,
and
g
in
meters
per
second
per
second;
C,
being
nondimen-
sional,
would
remain
unchanged
in
numerical
value).
Whereas
C is
assumed
to
be
a
coefficient
of
contraction
in
the
tradi-
tional
derivation,
in
actuality
it
is
an
experimentally
determined
coeffi-
cient
which
is
dependent
upon
all
the
variables
needed
to
describe
the
channel,
the
weir,
and
the
discharging
liquid.
Thus,
in
the
absence
of
a
rigorous
theoretical
solution,
dimensional
relations
must
be
used to
guide
the
analysis
of
experimental
data
on
triangular-notch
weirs.
DIMENSIONAL
ANALYSIS
The
principal
variables
needed
to
define
the
discharge
characteristics
of
a
triangular-notch,
thin-plate
weir
in
a
rectangular
channel
(fig.
1)
are:
Q,
the
discharge;
B,
the
width
of
the
approach
channel;
P,
the
height
of
the
notch
vertex
with
respect
to
the
floor
of
the
approach
channel;
h,
the
head
on
the
weir,
referred
to
the
vertex
of
the
notch;
6,
the
angle
included
between
the
sides of
the
notch;
p,
the
density
of
the
liquid;
n,
the
viscosity
of
the
liquid;
a,
the
surface
tension
of
the
liquid;
and
7,
the
specific
weight
of
the
liquid.
If
the
discharge
is
selected
as
the
dependent
variable,
a
complete
statement
of
the
discharge
function
is
Q-f<jB,P,h>9
t
p
9
p
t
o,y).
(2)
From
this
equation
a
nondimensional
discharge
ratio
can
be
expressed
as
a
function
of
five
nondimensional
ratios,
g
DISCHARGE
OVER
TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
B5
in
which
g=ylp.
The
dependent
ratio
in
equation
3
is
proportional
to
the
coefficient
of
discharge.
The
first
three
ratios
on
the right-hand
side
describe
the
geometry
of
the
weir,
approach
channel,
and
flow
pattern;
the
last
two
ratios
are
the
Reynolds
number
(R)
and
the
Weber number
(W).
SIGNIFICANCE
OF
THE
RATIOS
IN
EQUATION
3
The
first
independent
ratio
in
equation
3,
h/P,
is
a
measure
of
the
depth-contraction
characteristic.
Because
velocities
in
the
channel
upstream
from
the
weir
are
proportional
to
the
head,
the
h/P
ratio,
in
combination
with
h/B
and
0,
is
also
a
measure
of
the
relative
magnitude
of
the
velocity
in
the
approach
channel.
The
hIB
ratio,
in
combination
with
6,
is
a
measure
of
the
width-
contraction
characteristic
(resembling
bIB
for
rectangular-notch
weirs;
see
Kindsvater
and
Carter,
1959).
A
more
convenient
ratio
to
serve
the
same
purpose
is
P/B,
which
is
the
quotient
of
h/B
divided
by h/P.
Thus,
as
a
width-contraction ratio,
P/B
depends
on
h/P
as
well
as
0.
The
notch
angle,
0,
is
a
nondimensional
measure
of
the
shape
of
the
weir
notch.
It
is
also
a
measure
of
the
cross-sectional
shape
of
the
discharging
liquid
stream
in
the
plane
of
the
weir.
In
contrast
with
the
discharge
from
most
other
forms
of
weirs,
the
shape
of
the
stream
from
a
triangular-notch
weir
is
geometrically
similar
at
all
values
of
head,
except
as
it
is
influenced
by
h/P
and
hIB.
The
Reynolds
number,
R,
is
a
measure
of
the
relative
influence
of
fluid
viscosity.
It
is
usually
expressed
as
R
=
VLp//t,
in
which
V
is
a
typical
velocity,
L
is
a
significant length,
p
is
the
mass
density,
and
/A
is
the
dynamic
viscosity
of
the
liquid.
In
this
instance
the
head,
h,
is
the
dominant
length
parameter.
As
the
velocity
is
also
a
function
of
h,
the
influence
represented
by
the
Reynolds
number
can
be
expressed
in
terms
of
h,
p,
and
p.
The
Weber
number,
W, is
a
measure
of
the
relative
influence
of
sur-
face
tension.
It
is
usually
expressed
as
W
=
VVx/v/o/p
in
which
a
is
the
coefficient
of
surface
tension
of
the
liquid.
As
in
the
Reynolds
number,
h
is
the
most
significant
length
parameter
for
use
in
the
Weber
number.
Because
V
is
also
a
function
of
h,
the
influence
represented
by
the
Weber
number
can
be
expressed
in
terms
of
h,
a,
and
p.
COEFFICIENT
OF
DISCHARGE
FOR
ONE
LIQUID
In
equation
3
the
dependent
variable
is
proportional
to
the
coefficient
of
discharge.
The
independent
variables
include
three
geometric
ratios
and
two
fluid-property
ratios.
As
explained
in
the
preceding
section,
one
of
the
geometric
ratios,
hIB,
can
be
replaced
with
P/B,
which
is
more
convenient
because
it
is
a
constant
for
a
given
weir
installation.
B6
FLOW
OF
WATER
OVER
WEIRS
AND
DAMS
For
one
liquid
over
a
limited
temperature
range,
/A,
a,
and
p
can
be
assumed
to
be
constants.
Under
these
circumstances,
the
effects
of
viscosity
and
surface
tension
are
related
to
the
absolute
magnitude
of
h
alone. Thus,
both
R
and
W
in
equation
3
can
be
replaced
with
the
quan-
tity
h.
It
follows
that,
for
one
liquid
and
a
limited
range
of
temperatures,
(4)
In
this
report
the
only
liquid
of
interest
is
water
at
normal
atmospheric
temperatures.
MODIFIED
EQUATIONS
FOR
ONE
LIQUID
The
separate
quantity
h
in
equation
4
represents
the
combined
and
inseparable
effects
of
viscosity
and surface
tension
on
the
coefficient
of
discharge.
The
principal
effects of
viscosity
are
those
which
are
associated
with
flow
pattern
modifications
due
to
boundary
resistance
and
separation.
The
principal
effects
of
surface
tension
are
associated
with
the
curvature
of
the
nappe
and
"clinging"
on
the
crest
surfaces
of
the
notch.
A
detailed
discussion
of
these
effects
is
contained
in
the
paper
by
Kindsvater
and
Carter
(1959)
on
rectangular,
thin-plate
weirs.
The
following
pertinent
conclusions
are
drawn
from
that
paper:
1.
The
combined
effects
of
viscosity
and
surface
tension
on
a
notch
weir
are
commensurate
with fictitious
increases
in
head
and
notch
width.
2.
The
coefficient
of
discharge
can
be
expressed
in
terms
of
the
geometric
ratios
alone
if
the
effects
of
viscosity
and
surface
tension
are
accounted
for
by
an
adjustment
of
the
measured
values
of
head
and
notch
width
(for
triangular-notch
weirs,
for
which
notch
width
is
a
function
of
h,
only
the
measured
values
of
head
need
be
adjusted.)
3.
The
adjustment
of
measured
values
of
h
can
be
accomplished
very
simply,
as
indicated
by
the
equation
h
e
=
h+kh,
(5)
in
which
h
e
is
the
effective
(adjusted)
head,
h
is
the
measured
head,
and
kfr
is
a
quantity
which
must
be
determined
by
experiment.
1
4.
Use
of
the
effective
head,
h
e
,
in
place
of
h,
results
in
the
following
modifications
of
equations
1
and
4
for
one
liquid:
1
Subsequent
to
the
initial
exposition of
the
"effective-head
concept"
by
Kindsvater
in
1956,
it
was
applied
successful-
ly
to
several
kinds
of
weirs
by
others
(Carter,
1956;
Schlag,
1962a;
Schlag,
1962b;
John
Shen,
written
commun.,
1962;
Burgess
and
White,
1966,
among
others).
DISCHARGE
OVER
TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
B7
W
(6)
and
Equation
6,
in
combination
with
experimentally
derived
values
of
C
e
and
kh,
is
proposed
as
a
new,
comprehensive
discharge formula
for
tri-
angular-notch,
thin-plate
weirs.
2
Equation
7
defines
C
e
as
a
function
of
geometry
alone;
i.e.,
independent
of
fluid-property
effects
represented
by
h.
The
adequacy
and
validity
of
these
equations
must
be
examined
in
the light
of
experimental
data.
The
data
used
for
this
purpose
have
been
abstracted
from
the
literature.
REVIEW
OF
THE
LITERATURE
THOMSON'S
EXPERIMENTS
James
Thomson,
Professor
of
Civil
Engineering
at
Queen's
College,
Belfast,
Ireland,
was
among
the
earliest
experimental
investigators
of
the
triangular-notch
weir
(Thomson,
1858,
1861).
Thomson's
ex-
periments
were
made
at
a
pond
in
an
open
field
near
Belfast.
His
pur-
pose
in
making
the
tests
was
to
acquire
experimental
evidence
to
sup-
port
his
proposal
that
triangular-notch
weirs
be
used
instead
of
rec-
tangular
weirs
when
the
range
of
discharges
to
be
measured
included
very
small
flows.
Professor
Thomson's
experimental
equipment
was
crude
by
modern
standards,
and
the
range
of
conditions
covered
by
his
experiments
was
small.
Nevertheless,
some
of
his conclusions
are
pertinent
here.
Two
notch
angles,
90°
and
127°,
were
investigated.
For
the
90°
notch,
Thomson
recommended
a
constant
value
of
C
(eq
1)
=
0.593.
For
the
127°
notch,
he
recommended
C-
0.617.
Experiments
made
with
the
vertex
of
the
notch
at
the
level
of
the
channel
(P=0),
with
the
channel
wide
enough
to
provide
negligible
approach
velocities,
showed
no
ap-
preciable
influence
which
could
be
attributed
directly
to
the
value
of
P.
With
reference
to the
127°
notch,
Thomson
noted
an
instability
which
he
associated
with
the
nappe's
tendency
to
cling
to
the
upper
portions
of
the
wetted
crest
surfaces.
This
led
him
to
recommend
for
larger
discharges
that
two
or
more
90°
notches
(located
side-by-side)
be
used
instead
of
a
single,
large-angle
notch.
2
Equation
6
is
described
as
the
Kindsvater-Shen
equation
in
the
international
standard
(International
Standards
Organization,
1975)
which
was
based
in
part
on
the
1960
draft
of
this
report.
B8
FLOW
OF
WATER
OVER
WEIRS
AND
DAMS
BARR'S
EXPERIMENTS
One
of
the
most
extensive
among
the
early
investigations
began
as
an
effort
to
check
Thomson's
conclusions
(Barr,
1910).
James
Barr,
then
a
Carnegie
Research
Scholar
at
Glasgow
University,
Scotland,
performed
his
experiments
in
the
James
Watt
Engineering
Laboratories.
Many
of
the
traditional
formulas
for
90°-notch
weirs
are
based
on
the
results
of
Barr's
experiments.
Because
his
instrumenta-
tion
and
technique
were
good,
his
data
are
among
those
selected
for
analysis
in
this
report.
Barr's
experiments
were
performed
primarily
with
three
different
90°
notches.
One
weir
was
made
of
brass
and
two of
iron
plate.
The
upstream
edges
of
the
crest
surfaces
were
square
and
sharp,
and
the
width
of
the
crest
surfaces
varied
from
1/16
inch
to
1/12
inch.
A
54°
notch
was
also
tested.
The
weirs
were
placed
at
the
end
of
a
channel
which
was
4
feet
wide
and
22
feet
long.
The
vertex
of
the
notches
was
about
2
feet
above
the
floor
of
the
approach
channel
for
most
of
Barr's
tests.
To
investigate
the
effect
of
channel
width
and
weir
height,
Barr
used
false
walls
and
floors
in
the
approach
channel.
The
false
walls
extended
3
feet
upstream,
and
the
floor
extended
3.5
feet
upstream
from
the
weir
plate.
Tests
were
also
made
to
investigate
the
effects
of
roughness
and
projections
on
the
upstream
face
of
the
weir.
For
this
purpose,
roughness
was
produced with
a
mixture
of
varnish
and
emery
particles.
Projections
consisted
of
narrow
metal
strips
which
were
bolted
to
the
weir
bulkhead.
On
the
basis
of
his
experiments,
Barr
disagreed
with
Thomson's
con-
clusion
that
the
coefficient
of
discharge
was
a
constant.
His
results
in-
dicated
that
the
coefficient
varied
with
the
head.
He
concluded
that
the
coefficient
was
increased
by
roughness
and
projections
on
the
upstream
face
of
the
weir.
He
also concluded
that
the
coefficient
was
independent
of
channel
width
if
the
width
was
at
least
eight
times
the
head.
For
channel
widths
less
than
Sh,
the
coefficient
increased
as
the
width
decreased.
He
also
found
that
the
coefficient
decreased
slightly
with
decreasing
values
of
P
when
P
was
less
than
Kh,
where
K
is
a
coefficient
equal
in
value
to
the
head
in
inches.
BARR-STRICKLAND
FORMULA
A
widely
quoted
formula
for
90°-notch
weirs
was
derived
by
T.
P.
Strickland
(1910)
on
the
basis
of
Barr's
experiments.
As
an
equation
for
C,
the
Barr-Strickland
formula
is
C=
0.566+^^-
(8)
DISCHARGE
OVER
TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
B9
CONE'S
EXPERIMENTS
Subsequent
to
the
work
of
Thomson
and
Barr,
the
triangular-notch
weir
was
widely
used
and
extensively
investigated
in
the
United
States
as
well
as
Europe.
One
of
the
earliest
investigators
in
this
country
was
V.
M.
Cone
(1916),
whose
work
on
rectangular,
trapezoidal,
circular,
and
triangular
thin-plate
weirs
was
performed
in
the
laboratory
of
the
Colorado
Agricultural
Experiment
Station
at
Fort
Collins,
Colorado,
under
the
sponsorship
of
the
U.S.
Department
of
Agriculture.
The
channel
used
for
Cone's
experiments
was
20
feet
long,
10
feet
wide,
and
6
feet
deep.
The
vertex
of
the
weir
notch
was
4.5
feet
above
the
channel
floor.
Cone
tested
five
triangular-notch
weirs,
with
notch
angles
equal
to
120°,
90°, 60°,
30°,
and
28°4'.
All
weirs
were
made
of
V4-inch
brass
plate,
with
sharp
upstream
edges
and
crest-surface
widths
of
1/16
inch
(except
the
120°
notch,
for
which
the
crest
surface
was
1/32-inch
wide).
A
total
of
98
tests
was
made,
covering
a
range
of
heads
from
0.20
to
1.35
feet.
Cone,
like
Thomson,
observed
that
notch
angles
of
120°
or
larger
were
impractical
because
of
the
tendency
for
the
nappe
to
cling
to
the
upper
portion
of
the
wetted
crest
surfaces.
On
the
basis
of
his
ex-
periments,
he
proposed
a
general
formula
for
all
notch
angles
between
28°
and
109°.
As
an
equation
for
C,
Cone's
formula
is
r
0.576
0.00584
,
Q
.
u
=
+
'
(y
)
in
which
S
is
the
slope
of
the
sides
of
the
notch,
expressed
decimally,
and
50.75
Cone
also
made
a
limited
number
of
tests
on
the
90°
notch
with
the
floor
of
the approach
channel
at
the
vertex
of
the
notch.
He
concluded
that
the
coefficient
of
discharge
was
slightly
greater
for
P=0
than
for
P=4.5
feet.
Thus,
the
results
of
tests
made
by
Thomson,
Barr,
and
Cone
give
conflicting
indications
of
the
influence
of
P.
With
regard
to
crest-surface
width,
Cone
concluded
that
"thin
edge"
and
"sharp
edge"
need
not
imply
that
the
weir
notches
are
knife-edged.
He
observed
that
the
allowable
width
depends
on
the
head.
Ex-
periments
indicated
that
"edges
V4-inch
thick
showed
that
while
water
would
adhere
to
the
notch
edges
with
a
head
of
0.15
foot,
there
was
no
adherence
with
heads
of
0.2
foot
and
over."
He
recommended
that
head
measurements
"be
made
either
at
a
distance
of
at
least
4/&
upstream
from
the
notch
or
at
a
distance
of
at
least
2h
sidewise
from
the
end
of
the
crest
of
the
notch"
(Cone,
1916, p.
1089-1090).
BIO
FLOW
OF
WATER
OVER
WEIRS
AND
DAMS
YARNALL'S
EXPERIMENTS
D.
R.
Yarnall's
principal
work
on
triangular-notch
weirs
was
based
on
research
performed
at
the
University
of
Pennsylvania
(Yarnall,
1912,
1926).
His
tests
were
made
in
a
channel
6
feet
wide
and
9
feet
long,
with
only
4
feet
8
inches
between
baffles
and
weir
plate.
The
ver-
tical
distance
from
the
vertex
of
the
notch
to
the
floor
of
the
approach
channel
was
3.6
feet.
The
notch
angles
tested
by
Yarnall
were
90°,
53°8',
27°,
and
13°8',
and the
width
of
the
weir-crest
surfaces
was
1/32
inch.
A
total
of
61
tests
were
made
on
the
four
weirs,
with
a
range
of
heads
from
0.35
to
1.26
feet.
A
notable
feature
of
Yarnall's
experiments
was
the
short
channel,
which
he
had
equipped
with
simple
but
effective
baffles
in
order
to
pro-
duce
a
uniform
velocity
distribution
upstream
from
the
weir.
Such
demonstrations
of
the
practicality
of
short
weir
"boxes"
led
to
their
widespread
use
as
portable
flow-meters
in
hydraulics
laboratories,
in-
dustrial
plants,
and
field
applications.
GREVE'S
EXPERIMENTS
The
most extensive
investigation
of
different
notch
angles
is
represented
by
the
work
of
Professor
F.
W.
Greve
at
Purdue
Universi-
ty
(Greve,
1932).
A
total
of
16
different
weirs,
with
notch
angles
vary-
ing
from
25°03'
to
118°11',
were
investigated.
All
of
the
weirs
were
tested
in
a
channel
which
was
5
feet
wide
and
16
feet
long
from
baffles
to
weir
plate.
The
distance
from
notch
vertex
to
channel
floor
varied
from
4.5
to
5
feet.
The
weir
plates
were
cut
from
3
/s-inch
soft
steel
plates,
with
the
downstream
edges
of
the
notches
beveled
to form
a
crest
which
was
sharp
on
the
upstream
edge
and
1/32-inch
wide.
The
report
stated
that
the
plates
were
coated
with
asphalt
paint,
but
not
specifically
that
the
paint
was
applied to
the
surfaces
in
the
immediate
vicinity
of
the
crest.
Thus,
there
is
some
uncertainty regarding
the
smoothness of
the upstream
face
and
the
sharpness
and
width
of
the
crest
during
the
tests.
Table
1
shows
a
summary
of
the
scope
of
Greve's
experiments.
In
summarizing
the
results
of
his
tests,
Greve
presented
a
com-
prehensive
discharge
formula
for
all
notch
angles
between
20°
and
120°.
His
formula
for
C
is
C=
(11)
(tan
|)0.004^0.03
Referring
to
supplementary
tests
on
a
10°
notch,
Greve
observed
that
the
small
notch
exhibited
characteristics
of
"excessive
clinging"
and
gave
"results
which
were
not
in
harmony"
with
his
general
formula.
DISCHARGE
OVER
TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
Bll
TABLE
1.-Scope
ofGreve's experiments
Series
W-3.3
W-3.4
______
W-3.0
W-3.1
W-3.5
W-3.6
W-3.6A
_____
W-3.7
W-3.8
_
W-3.9
______
W-3.10
______
W-3.11
_______
W-3.12
W-3.13
W-3.14
W-3.15
Notch
angle
25°03'
36°53'
40°00'
44°
24'
45°23'
45°23'
53°
55'
53°55'
59°07'
69°38'
81°
52'
94°39'
98°47.5'
102°2(y
110°00'
118°H'
Number
of
tests
37
30
27
46
27
13
32
17
31
43
33
46
22
31
36
30
Range
of
head
(ft)
From
0.167
.146
.282
.201
.153
.251
.241
.190
.217
.243
.342
.219
.318
.257
.217
.251
To
0.991
1.090
.854
1.025
1.178
1.128
1.211
1.199
1.254
1.216
1.199
1.111
.988
1.047
.945
.725
Range
of
temperature
(°F)
From
62
63
69
69
65
71
72
71
77
71
74
74
69
72
74
80
To
69
71
73
79
67
73
73
72
84
75
77
77
74
76
81
82
A
final
statement,
based
on
attempts
to
correlate
his
results
with
the
results
of
others,
is
noteworthy:
"it
is
unwise
to
formulate
a
general
ex-
pression
for
discharge
from
data
compiled
from
different
sources
unless
such
expression
incorporates
certain
factors
which
correlate
variation
in
the
physical
characteristics
of
the
testing
plants"
(Greve,
1932,
p.
33).
LENZ'S
EXPERIMENTS
The
effect
of
viscosity
and
surface
tension
were
objectives
of
the
ex-
periments
made
by
Professor
Arno
T.
Lenz
at
the
University
of
Wisconsin
(Lenz,
1943).
Using
water
and
two
different
oils
at
temperatures
ranging
from
51°
to
102°
F,
Lenz's
tests
covered
a
range
of
viscosities
from
1
to
150
times
that
of
water,
surface
tensions
from
1
to
0.41
times
that
of
water,
and densities
from
1
to
0.85
times
that
of
water.
Six
different
weirs,
with
notch
angles
ranging
from
10°
to
90°,
were
investigated.
The
tests
were
made
in
a
steel
tank
3.5
feet
wide
and
7
feet
9
inches
long
from
baffles
to
weir
plate.
The
vertex
of
the
notch
was
3
feet
above
the
floor
of
the
tank.
The
weir
plates
were
made
of
Vs-inch
brass,
sharp-edged
on
the
upstream
side
and
beveled
on
the
downstream
side
to
form
a
sharp-edged
crest
1/32-inch
wide.
Table
2
shows
a
summary
of
the
scope
of
Lenz's
tests
which,
for
the
purpose
of
this
report,
includes
only
those
experiments
using
water.
B12
FLOW
OF
WATER
OVER
WEIRS
AND
DAMS
TABLE
2.
-Scope
ofLenz's
experiments
with
water
Series
90
D_
_
__
60D_
_
__
45D
__
_ _
28D
_
20
D_
_
__
20
D
_
__
10
D
__ _ _
Notch
angle
89°53.2
;
59°51.0'
44°40.0'
27°55.0'
l$°55.ff
20°
2.5'
10°20.1'
Number
of
tests
14
33
18
18
24
19
33
Range
of
head
(ft)
From
0.23
.16
.20
.26
.18
.24
.24
To
0.50
.60
.55
.70
.70
.70
.88
Range of
temperatures
From
61
54
56
51
54
54
52
To
63
62
60
59
67
65
54
On
the
basis
of
his
experiments,
Lenz
derived
a
general
formula
for
the
coefficient
of discharge
M
C=0.560+
'
(12)
in
which
R=
N
/g^3
/Gi/p)
is
the
Reynolds
number;
W=(pgh
2
)/a,
is
the
Weber
number;
and
M,
n,
and
m
are
empirically
determined
functions
of
the
notch
angle,
M=0.475+
°'
225
>
(13)
-
\0.80
/
0
\0-09
(14)
n~
0.165
(tan
-^
,
and
«
0.170
,
1(
.v
m-
(15)
-
'
0.035
That
the
formula
is
not
truly
general
is
indicated
by
the
fact
that
strict
limits
of
applicability
were
placed
on
R,
W,
C,
and
6.
For
water
at
one
temperature
(70°
F),
limits
on
R
and
W
are
re-
moved,
and
C
can
be
computed
with
the
equation
C=0.560+
>
(16)
h
a
in
which
AT
and
a,
like
M,
n,
and
m,
are
functions
of
0
alone.
In
equation
16,
R
and
W
are
functions
of
the
quantity
h,
because,
for
one
liquid
at
a
constant temperature,
the
fluid
properties
are
constant
(See
the
discus-
sion
leading
to
eq
4).
Lenz
gives
experimentally
determined
values
of
AT
and
a
in
table
3.
DISCHARGE
OVER
TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
B13
TABLE
3.
-
Values
o/N
and
a/or
equation
16
(Lenz)
Notch
angle,
9
Constant
N
__
a
_
90°
.
0.0159
.588
60°
0.0203
.582
45°
0.0238
.579
28°04'
0.0315
.575
20°
0.0390
.573
10°
0.0624
.569
Basing
his
comparison
on
the
tests
of
Barr,
Yarnall,
Greve,
Ho
and
Wu
(Ho
and
Wu,
1931),
Lenz
concluded
that
equation
16
would
give
results
accurate
to
within
1
percent
for
all
notch
angles
between
28°
and
90°.
He
observed
that
increasing
the
temperature
of
water
from
40°
F
to
165°
F
decreases
the
computed
value
of
C
about
1
percent.
EXPERIMENTS
OF
NUMACHI,
KUROKAWA,
AND
HUTIZAWA
The
most extensive
investigation
of
a
single
notch
angle
and
a
single
liquid
is
represented
by
the
experiments
performed
by
Numachi,
Kurokawa,
and
Hutizawa
(1940)
at
Tohoku
Imperial University
in
Japan.
These
tests,
all
of
which
were
made
with
water
and a
90°
triangular-notch
weir,
covered
a
range
of
values
of
h
from
0.16
to
0.85
feet,
P
from
0.31
to
2.16
feet,
and
B
from
1.44
to
3.87
feet.
The
channel
in
which
the
tests
were
made
was
26
feet
long
and
3.87
feet
wide.
False
walls
and
a
false
floor,
extending
15
feet
upstream
from
the
weir,
were
used
to
produce
30
different
values
of
PIE.
The
weir
was
made
of
bronze,
and
the
weir
crest
surface
was
5/64
inches
wide.
Subsequently,
12
additional
series
of
tests
were
made
by
Numachi,
Kurokawa,
and
Hutizawa
(1943).
Made
with
the
same
weir,
these
sup-
plementary
tests
covered
a
lower
range
of
values
of
P,
from
0.01
to
0.164
feet.
Values
Of
B
varied
from
0.985
to
2.10
feet.
On
the
basis
of
their
data,
Numachi
and
Hutizawa
proposed
a
general
equation
for
the
coefficient
C,
(17)
0=0.574^(0.055.^)
£-
(M-
Within
the
range
of
conditions
covered
by
the
tests,
equation
17
gives
results
which
are
within
1
percent
of
the
experimental
data.
OTHER
EXPERIMENTS
Among
the
many
published
accounts
of
experiments
on
triangular-
notch
weirs,
some
are
of
interest
because
they
were
especially
con-
cerned
with
certain
details
of
the
discharge
characteristics.
For
exam-
ple,
Switzer
(1915),
Cozzens
(1915),
and
Smith
(1934,
1935)
made
tests
B14
FLOW
OF
WATER
OVER
WEIRS
AND
DAMS
to
determine
the
influence
of
temperature
on
the
discharge
of
water.
On
the
basis
of
tests
on
90°
and
54°
notches,
with
temperatures
rang-
ing
from
39°
F
to
165°
F,
Switzer
concluded
that
the
effect
on
the
coefficient
of
discharge
was
less
than
2
percent
and
"inappreciable
com-
pared
with
other
factors
present".
Cozzens,
on
the
other
hand,
presented
a curve
to
be
used
to
make
a
small
correction
over
a
range
of
temperatures
from
60°
F
to
220°
F.
Smith
developed
an
empirical
for-
mula
which
incorporated
the
kinematic
viscosity
in
a
correction
coeffi-
cient.
Professor
H.
W.
King
(1916,
1954)
made
tests
on
90°,
60°,
and
22.5°
notches
at
the
University
of
Michigan.
His
weirs
were
made
of
steel,
with
a
sharp
upstream
crest
edge
and
a
crest-surface
width
of
Vs
inch.
The
vertex
of
the
notch
was
2
feet
above
the
floor
of
the
experimental
channel.
On
the
basis
of
his
experiments,
Professor
King
developed
the
following
formulas:
(90°
notch)
C--'
(18)
(60°
notch)
C=
0.595
ft
0
-
01
,
(19)
(22.5°
notch)
C=9L,
(20
)
An
investigation
performed
at
Cornell
University
by
Ho
and
Wu
(1931)
is
notable
for
the
large
range
of
heads
(from
0.129
to
3.43)
covered
by
the
tests.
All
of
these
tests
were
made
in
a
channel
6
feet
wide,
12
feet
deep,
and
30
feet
long
from
baffles
to
weir
plate. Weirs
tested
included
notch
angles
of
90°, 60°, 37°,
28°,
and
19°.
The
ver-
tices
of
notches
were
a
minimum
distance
of
8
feet
above
the
channel
floor.
The
weir
plates
were
made
of
galvanized
sheet
metal
or
brass,
with
sharp,
square,
upstream
edges.
Lenz
(1943)
observed
that
his
general
formula
for
water
(eq
16)
was
confirmed
within
1
percent
by
the
Ho
and
Wu
data.
From
1931
to
1934,
four
investigations
were
made
at
Princeton
University
by
senior
students
under
the
direction
of
Professor
L.
F.
Moody.
Most
pertinent
of
these
is
the
investigation
by
Allerton
(1932),
which
involved
tests
with
notch
angles
of
90°, 60°,
54°,
and
30°.
Of
particular
interest
is
the
fact
that
Allerton
analyzed
his
data
on
the
basis
of
a
formula
which
involved
a
head
adjustment
similar
to
that
used
in
equation
5.
The
formula
was
attributed
to
Moody,
but
no
men-
tion
of
the
formula
is
made
in
reports
of
two
subsequent
investigations
made
at
Princeton.
Investigations
which
placed
emphasis
on
the
influence
of
viscosity
were
made by
Mawson
(1927),
Thornton
(1929),
and
Smith
(1934,
1935).
Because
they
ignored
the
equal
or
larger
influence
of
surface
tension,
however,
the
results
of
the
studies
were
inconclusive.
DISCHARGE
OVER
TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
B15
Hertzler
(1938)
was
especially
concerned
with
120°
notches.
On
the
basis
of
his
tests
on
six
different
weirs,
all
with
6
=
120°,
he
proposed
the
formula
SUMMARY
Published
accounts
of
experimental investigations
agree
on
very
few
details
of
the
discharge
characteristics
of
triangular-notch
weirs.
Some
of
the
disagreements
are
doubtless
the
result
of
differences
in
equip-
ment
and
technique.
More
significantly,
however,
conclusions
drawn
from
the
experiments
are
believed
to
differ
because
of
certain
inade-
quacies
in
traditional
methods
of
analyzing
the
data.
It
is
reasonable
to
assume
that
experimental
equipment
was
ade-
quate
and
that
the
work
was
done
with
skill
and
care.
Nevertheless,
there
are
indications
that
some
of
the
weirs
were
neither
sharp-edged,
thin-crested,
nor
smooth-faced.
Crude
equipment
and
technique
in
other
instances
resulted
in
systematic
errors
related
to
the
measure-
ment
of
Q,
h,
and
6.
The
effect
of
these
deviations
cannot
be
determined
from
the
information
available.
There
is
some
agreement
that
weirs
with
notch
angles
less
than
about
20°
or
greater
than
about
100°
exhibit
characteristics
of
in-
stability
which
are
related
to the
intermittent
clinging
of
the
nappe
to
the
surface
of
the
crest.
Similar
behavior
was
observed
at
extremely
low
heads
on
all
notch
angles.
Most
investigators
found
that
C
varied with
notch
angle.
This
is
a
clear
indication
of
a
shortcoming
in
the
traditional,
so-called
theoretical
equation
of
discharge
(eq
1).
Only
one
of
the
many
investigations
(by
F.
Numachi
and
others)
included
a
systematic study
of
the
influence
of
weir
placement
and
channel
geometry.
However,
this
study
was
made
with
only
one
notch
angle
and
one
liquid.
Several
investigators
demonstrated
the
practicality
of
using
short
approach
channels
if
they
are
effectively
equipped
with
baffles.
No
comprehensive
studies
have
been
made
of
the
influence
of
velocity
distribution
and turbulence
in
the
approach
channel.
Few
investigators
attempted
to
isolate
and
evaluate
the
influence
of
the
physical
properties
of
the
liquid,
although
several
attempted
to
determine
the
effect
of
temperature
on
the
discharge
of
one
liquid
(water).
Their
conclusions
are
remarkable
for
their
disagreement.
Lenz
made considerable
progress
in
isolating
the
separate
effects
of
viscosity
and
surface
tension,
but
the
range
of
conditions
covered
in
the
in-
vestigation
was
quite
limited.
For
this reason,
his
proposed
general
for-
mulas
are
restricted
in
applicability.
They
are
also
inconvenient
to
use.
B16
FLOW
OF
WATER
OVER
WEIRS
AND
DAMS
Most
investigators
working with
water
at
normal
temperatures
reported
a
correlation
between
C
and
h.
Empirical
formulas
were
evolved
to account for
this
correlation,
but
no
explicit
recognition
was
given
to
the
fact
that
the
h
correlation
is
evidence
of
the
combined
effects
of
viscosity
and surface
tension.
Thus,
the
"scale
effect"
implica-
tions
of
the
phenomenon
were
ignored.
It
is
believed
that
the
effective-
head
concept
(eq
5)
provides
a
reasonable
and
practical
method
of
ac-
counting
for
the
effects
related
to
the
absolute
magnitude
of
h.
No
additional
experiments
were
made
for
this
investigation.
Instead,
experimental
data
obtained
from
some
of
the
sources
reviewed
above
are
used
in
the
following
analysis.
ANALYSIS
OF
DATA
EVALUATION
OF
k
h
The
coefficient
C
e
in
equations
6
and
7
is
described
as
a
function
of
geometric
ratios
(hIP,
PIE,
and
6)
when
h
e
,
the
"effective
head,"
is
deter-
mined
from
equation
5,
h
e
=h+kh.
(5)
In
this
equation,
h
is
the
measured
head
on
the
notch and
k^
is
an
ex-
perimentally
determined quantity
that
accounts
for
the
combined
effects
of
viscosity
and
surface
tension.
Comparison
of
equations
4
and
7
shows
that
the
effect
of
the
effective-head
adjustment
is
to
relieve
the
coefficient
of
discharge
of
dependency
on
h.
This
criterion
is
used
to
determine
the
value
of
kh
which
is
applicable
to
a
specific
set
of
ex-
perimental
data.
For
one
liquid
over
a
small
temperature
range,
and
for
one
notch
angle,
k^
is
assumed
to
be
a
constant.
The
validity
of
the
several
basic
assumptions
related
to
the
effective
head
concept
has
been
demonstrated
in
a
previous
study
of
rectangular
weirs.
Nevertheless,
the practicality
of
the
concept
as
applied
specifically
to
triangular-notch
weirs
must
be
established
on
the
basis
of
experimental
data
for
triangular-notch
weirs.
The
results
of
ex-
periments
by
Barr,
Cone,
Yarnall,
Greve, Lenz,
and
Numachi,
Kurokawa,
and
Hutizawa
are
selected
for
this
purpose.
Because
the
flow
of
water
at
ordinary
atmospheric
temperatures
is
of
principal
in-
terest
to
the
Geological
Survey,
and
because
data
on
other
liquids
are
limited
in
many
ways,
the
data
used
are
only
those
which
involve
water
in
the
temperature
range
from
40°
F
to
85°
F.
In
the
validation
process,
the
quantity
k^
is
evaluated
from
ex-
perimental
data
by
a
trial
procedure.
For
a
series
of
tests
in
which
h
is
the
principal
variable,
k^
is
determined
by
successive
approximations
as
the
quantity
which
will
remove
the
correlation
between
C
and
h.
The
DISCHARGE
OVER TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
B17
U.DJ
0.62
0.61
0.60
0.59
0.58
0.57
0.63
0.62
0.61
0.60
0.59
0.58
0.57
n
RR
\
A
A
*;
^
^^
£--
a»
A
L
^
A
A
f
i
r*-
~~^
C as
a
A-
B Ce
as
A
A A
|
A
^
4
~x
functk
A
x
a
func
L_
_
_
_
x
>n
of
/j
-x
-x.
~x
Q
/P
zir
^
eM^i-c
X
p=
-A
-
X
-A
>o^
EXPLANATION
Symbol
Head,
in
feet
A
O.K
h
<0.3
X
0.3<
h
<0.5
0
0.5<
/?
<0.7
Notes:
fi=3.87
ft,
*/7=0.003
ft,
P=0.64-2.16
ft
-x
x
tion
o:
.^x^
/7/P
T38^
6^>^<
X
r-o-
^T
0.06
0.08
0.10
0.12
0.14
0.16
0.18 0.20
0.22
0.24 0.26
0.28
0.30
0.32
VALUE
OF
h/P
FIGURE
2.-Evaluation
of
k
h
illustrated
with
Numachi,
Kurokawa,
and
Hutizawa
data
(0
=
90°).
procedure
is
illustrated
in
figure
2
by
its
application
to
some
of
the
data
reported
by
Numachi,
Kurokawa,
and
Hutizawa.
3
These
data
were
selected
because
they
were
obtained
with
different
values
of
P.
Thus,
the
influence
of
h
can
be
isolated from
the
influence
on
hIP.
The
tests
shown
in
figure
2
are
for
a constant, large
value
of
B
and
5
different
values
of
P,
all
with
a
90°-notch
weir.
Figure
2A
shows
C
plotted
as
a
function
of
hIP.
Ranges
of
values
of
h
are
indicated
by
the
symbols
shown
in
the
legend.
The
scatter
in
values
of
C
is
systematically
related
3
The
procedure
is
illustrated
and
discussed
in
greater
detail
in
the
paper
by
Kindsvater
and
Carter
(1959,
p.
783-787,
figs.
3,
4,
5,
6)
on
rectangular weirs.
B18
FLOW
OF
WATER
OVER
WEIRS
AND
DAMS
to
the
magnitude
of
h
as
shown
by
the
dashed
curves.
There
is
no
clear-
ly
defined
correlation
with
P.
Figure
25
shows
C
e
plotted
as
a
function
of
hIP.
The
value
of
k^
which
was
used
in
the
computations
of
C
e
for
this
figure
was
0.003
foot.
Evidence
of
the
lack
of
correlation
between
C
e
and
h
is
shown
by
the
fact
that
one
curve
drawn
through
all
the
points
is
horizontal,
and
the
scatter
is
greatly
reduced.
Thus,
the
validity
of
the
effective-head
concept
is
demonstrated,
and
the
value
k^=
0.003
foot
is
shown
to
be
appropriate
for
the
tests
by
Numachi
and others.
Another
demonstration
of
the
validation
procedure
is
shown
in
figure
3,
which
is
based
on
the
results
of
Lenz's
tests
on
weirs
with
three
0.64
0.63
0.62
0.61
0.60
0.59
0.58
0.57
0.63
0.62
0.61
0.60
0.59
0.58
0.57
0.56
-*-&-*
EXPLANATION
Symbol
0
(degrees)
k^
feet
0
89°53'
0.003
X
59°5V
0.004
A
44°40'
0.005
Notes:
P=3.0
ft,
P/B=0.86
B Ce
as
a
function
of
h/P
0
0.02
0.04
0.06
0.08
0.10
0.12
0.14
0.16
0.18
0.20 0.22
0.24
0.26
VALUE
OF
h/P
FIGURE
3.-Evaluation
of
k
h
illustrated
with
Lenz
data.
DISCHARGE
OVER
TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
B19
different
notch
angles.
Values
of
the
notch
angles
are
shown
in
the
legend.
In
the
top
part
of
figure
3,
C
is
plotted
as
a
function
of
hIP,
but
because
P
is
constant
for
each
weir,
the
separation
and
curvature
of
the
lines
drawn
through
the plotted
points
show
the
influence
related
to
h
and
6.
The
lower
part
of
figure
3
shows
C
e
plotted
as
a
function
of
hIP
for
the
Lenz
data.
In
this
instance,
different
values
of k^
were
derived
for
each value of
6,
as
shown
in
the
legend.
Here
again
the
effectiveness
of
kh
in
eliminating
h
as
an
independent
variable
is
demonstrated
by
the
fact
that
curves
drawn
through
the
points
are
essentially
horizontal.
Coincidentally,
a
single
curve
fits
the
three
sets
of
points
reasonably
well,
showing
that
6
has
a
minimal
effect
on
C
e
for
notch
angles
be-
tween
45°
and
90°.
Values
of
PIB
and
h/P
represented
by
the
tests
shown
in
figures
2
and
3
are
in
the
range
in
which
these
variables
also
have
negligible
influence
on
C
e
.
This
fact
is
demonstrated
subsequently.
Values
of
k^
for
values
of
6
between
10°
and
120°
were
determined
from
the
tests
made
by
Barr,
Cone,
Yarnall,
Greve,
Lenz,
and
Numachi
and
others.
The
results
are
shown
on
figure
4.
Values
of
k^
for
those
few
tests
which
were
made
for
very
small
or
very
large
notch
angles
are
not
well
defined.
Deviations
from
the
smooth
curve
drawn
through
the
points
can
be
attributed
to
differences
in
physical
characteristics
of
weirs
and
test
channels.
AN
ALTERNATIVE
FOR
k
h
The
quantity
k^
is
added
to
the
measured
head
as
an
adjustment
for
the
combined
effects
of
viscosity
and
surface
tension.
The
procedure
is
justified
with
the
observation
that,
in
general, the
effects
of
the
two
fluid
properties
are
commensurate
with
a
fictitious
increase
in
head
and
notch
width.
Because
the
width
is
a
function of
the
head
for
triangular-
notch
weirs,
a
quantity
added
to
the
head
is
simultaneously
an
adjust-
ment
of
the
width.
However,
because
the
width
is
a
function
of
6
as
well
as
h,
it
is
not
unreasonable
that
figure
4
shows
k^
to
be
a
function
of
6.
As
an
alternative
to
k^,
a
factor
k
is
proposed,
where
k
is
measured
perpendicularly
to the
sides
of
the
notch.
Thus,
fc-Afcsin-!--
(22)
z
Values
of
k
were
computed
for
the
data
shown
in
figure
4
to
determine
whether
k
might
be
constant
for
all
notch
angles.
The
results
are
shown
in
figure
5.
The
figure
shows
that
a
value
of
k=
0.002
foot
could
be
used
for
values
of
0
between
40°
and
90°.
Somewhat
smaller
values
of
k
are
indicated
for
values
of
6
less
than
40°.
The
quantity
k
is
not
well
defined
for
values
of
6
greater
than
90°.
w
CO
o
0.024
50
60
70
80
VALUE
OF
0,
IN
DEGREES
FIGURE
4.
-Value
of
k
h
as
a
function
of
0.
90
100
110
120
s
o
Sd
so
DISCHARGE
OVER
TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
B21
»
To
<o
E
.-
c
>
N
CO
1=
fc
P
C
3
1-
-s
D
O
8
w
.
in
^
HI
C4H
DC
°
O
C!
ill
O
O
-«
UJ
*0
i
3
<
13
l
U3
H
05
O
133d
Nl
'*
dO
3mVA
B22
FLOW
OF
WATER
OVER
WEIRS
AND
DAMS
It
is
apparent
that
the
effective
head
in
the
modified
basic
equation
of
discharge
(eq
6)
can
be
evaluated
in
terms
of
either
k
or
k^.
If
k^
is
used,
values
of k^
are
read
from
figure
4.
If
k
is
used,
values
of
k
can
be
read
from
figure
5,
or,
in
the
range
from
40°
to
90°,
h
e
can
be
computed
as
(23)
sn
Which
of
these
alternatives
is
the
more
convenient
is
conjectural.
Hereafter
in
this
report,
h
e
is
computed
with
values
of k^ from
figure
4.
EVALUATION
OF
C
e
Figures
6
to
11,
inclusive, show
values
of
C
e
computed
from
results
of
the
tests
by
Barr,
Cone,
Yarnall,
Greve,
Lenz,
and
Numachi,
Kurokawa,
and
Hutizawa.
In
the
figures,
C
e
is
plotted
as
a
function
of
h/P.
The
data
cover
a
long
range
of
notch
angles
from
120°
to
10°.
In-
cluded
on
each figure
is
a
legend
which
identifies
the
investigators
and
gives
corresponding
values
of
6,
P/B, and
k^
Values
of
kh
used
in
com-
puting
C
e
for
each
set
of
tests
are
the
values
plotted
in
figure
4.
The
average
values
of
C
e
were
determined
visually
by
fitting
a
line
to
the
plotted
points.
The
average
value
and
the
limits
representing
1
percent
deviations
from
the
average
are
shown
as
horizontal
lines
in
each
figure.
The
experimental
data
plotted
in
figures
6
through
11
show
a
range
of
values
of
h/P
from
0.03
to
0.35
and
a
range
of
values
of
PIE
from
0.
15
to
1.5.
In
this
range,
which
includes
the
most
common
limits
for
prac-
tical
applications,
it
is
apparent
that
C
e
is
virtually
independent
of
h/P
and
PIE.
Thus,
within
this
range
C
e
is
remarkably
well
defined
as
a
function
of
6
alone.
Scatter
in
the
test
points
at
smaller
values
of
h/P
is
attributed
to
the
influence
of
intermittent
nappe-clinging
at
small
values
of
h.
The
influence
of
PIE
at
higher
values
of
hIP
is
discussed
in
the next
section.
Figure
12
shows
the
relationship
between
6
and
the
average
values
of
C
e
determined
from
figures
6
through
11.
The
dashed
portions
of
the
summary
curves for
C
e
(fig.
12)
and
kh
(fig.
4)
indicate
that
there
is
some
uncertainty regarding
the
practicality
of
weirs
with
notch
angles
less
than
20°
or
greater
than
100°.
0.62
0.61
o
u_
0.60
O
HI
D
t
0.59
0.58
X
o
o
o
0 0
o
x
o-
X
X
o o o
o
O
<B>
O|
0
0
O
1
8
1
O
^
1
0
o
0
0
EXPLANATION
Symbol
Name
6
PIB
AT,
(ft)
degrees
X
Cone's
120°
0.45
0.003
formula
O
Greve
118°11'
0.95
0.005
X X
+
1
-1
Pet.
.588
(avg)
Pet.
0.05
0.10
0.15
0.20
VALUE
OF
hIP
FIGURE
6.-Value
of
C
e
,
notch
angle
approximately
120°.
0.25
0.30
CO
O
0.35
a
o
K
f
w
to
oo
W
to
LL
O
0.62
0.61
0.60
0.59
0.58
0.57
o
o
0
o
X
o
o
8
°
0
o o
-
Y^
X
7
7
O
0
1
<0>07O
Q
OI
O
--X
-O*B>-
O-A
-0
1L
-
f
!
*
2
Q
AD
a
a
EXPLANATION
Symbol
Name
0
PIB
*y,(ft)
degrees
V
Barr
90°00'
0.50
0.003
x
Cone
90°00'
0.45
0.0035
n
Yarnall
90°00'
0.60
0.003
0
Greve
94°39'
0.95 0,003
+
Numachi
90°00'
0.16-1.04
0.003
and
others
A
Lenz
89°53'
0.86
0.003
4
v
o
+
*
;^,r!7.t
f
-
r
4
^r
7^
Q
-fD
I
+1
Pet.
-
0.578
(avg)
-1
Pet.
0.05
0.10
0.15
0.25
0.20
VALUE
OF
hIP
FIGURE
7.-Value
of
C
e
,
notch
angle
approximately
90
c
0.30
0.35
0.40
DISCHARGE
OVER
TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
B25
Is
**
o
Oq
in
^
0
O
Q3
-
_
<D
0
z-g
§
^
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CL
UJ
E
*
(0
£
z
c
"o
n
E
X
to
o
o o
000
o o o
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in
co
o
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in
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CO
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in in in
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(0 0)
C
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^
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c
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n
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100
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0-
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<
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Ll-
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Pu
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to
0.60
0.59
0.58
0.57
O
o
o
<n>
o
o
o
X
0
O
'
X
"
'
"
X
X
X
X
K
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X
X
3
Symbol
Name
O
Greve
X
Lenz
O
O
0
<
X
<
x x
X
EXPLANATION
6
degrees
45°23'
44°40'
0
0
©
£
°
O
PIB
k
h
(ft)
0.95
0.005
0.86
0.005
-
+
1
Pet.
-
-
-0.580
(avg)
-1
Pet.
0.05 0.10
0.15
VALUE
OF
h/P
FIGURE
9.-Value
of
C
e
,
notch
angle
approximately
45°.
0.20
0.25
0.30
O
3
O
^
1
O
O
DISCHARGE
OVER
TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
B27
If
£
°£
coo
*
0
0
QQ
LO
c
^
d
o
w
z
£
*
c
2
8*
g
S=
I-
§
S
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5
w
<N
c\
z
*
^
a.
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t
x
1
S
£
m
J°
o
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z
o
>
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x
c
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w
to
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0
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CD
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CO
d
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LO
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CM
CN
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1
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c
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2
i
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e
j_
«
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^*
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o
0
5
X
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a
X
O
OC
o
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1
3
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5
1
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1
8
c
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t-
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1
1
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1
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X
a
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1
a
|
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X
1
3
1
1
X
|
4
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i
1
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1
D
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!
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1-1
i
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I
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0
1
a
1
1
1
1
O
O
|
1
-
x
o o
oj
o
0
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CO
0
LO
CM
O
O
CM
O
LO
0
0
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LO
0
o
o
i
£
.2
O
"ho
ui
i
3
_e
O
*^
o
a>
13
CO
o
6
a
o do
0.62
0.61
0.60
0.59
0.58
0.
O
0
°
0
^o
0
cb
0
o
0
EX
PLAN
AT
8
Symbol
Name
degr
Q
Yarnall
13°C
©
Lenz
10°;
o
o
a
a
O
o
<o>
o
a>
o
a
ON
ees
P/B
k
h
(ft)
)8'
0.60
0.022
>0'
0.86 0.017
+
1
Pet.
o
a
-1
Pet.
Q
05
0.10 0.15
0.20
0.25 0.30
0.597
(avg)
0.35
Q.i
VALUE
OF
hIP
FIGURE
11.-Value
of
C
e
,
notch
angles
of
10°
and
13°.
DISCHARGE
OVER
TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
B29
T3
s
O
O
I
cj
T I
a
M
g
B30
FLOW
OF
WATER
OVER
WEIRS
AND
DAMS
INFLUENCE
OF
h/P
AND
P/B
A
few
tests
involving
different
values
of
P
and
B
were
made
by
Barr,
and
some
tests
withP=0
were
reported
by
Thomson
and
Cone.
Among
the
experimental
data
available
to
the
writer,
however,
the
only
data
covering an
extensive
range
of
values
of
hJP
and
PIE
were
those
ob-
tained
from
the
experiments
on
90°
notches
made
by
Numachi,
Kurokawa,
and
Hutizawa.
Values
of
C
e
were
computed
from
the
results
of
the
Numachi-
Kurokawa-Hutizawa
tests,
using
kh=
0.003
foot.
Smooth
curves
inter-
polated
from
the
plotted
data
were cross-plotted
to
obtain
the
family
of
curves
showing
C
e
as
a
function
of
hIP
and
PIE
on
figure
13.
The
results
are
a
comprehensive
solution
for
90°
-notch
weirs
that,
because
of
the
degree
of
extrapolation
from
the
data,
must
be
regarded
as
unsubstan-
tiated.
The
h/P
limit
lines
at
the
lower
left
corner
of
figure
13
illustrate
the
limited
hIP
range
of
the
Numachi-Kurokawa-Hutizawa
tests,
and
the
C
e
values
from
those
tests,
plotted
in
figure
7,
are
all
within
1
per-
cent
of
the
average
value
(0.578).
COMPARISON
OF
FORMULAS
BASIS
OF COMPARISON
Derived
from
tests
in
which
hIP
and
PIE
were
of
negligible
significance,
the
traditional
formulas
for
triangular-notch
weirs
are
generally
of
the
form
C=/«U),
(24)
in
which
an
empirically
derived
term
involving
h
accounts
for
the
com-
bined
effects
of
viscosity
and
surface
tension
for
water
at
ordinary
temperatures.
Unfortunately,
the
significance
of
h
was
not
understood
by
the
originators
of
most
of
these
formulas.
Consequently,
the
more
conservative
investigators
specified
a
range
of applicability
which
was
based
on
the
limits
of
their
test
conditions.
In
order
to
compare
the
proposed
new
formula
(eq
6)
with
the
classic
formulas,
values
of
C
were
computed
from
the
classic
formulas
and
from
the
equation,
_h+kh
2
-
obtained
from
the
solution
of
equations
1
and
6.
Values
of
C
e
and
kh
were
obtained
from
figures
10
and
4,
respectively.
The
comparisons
are
shown
in
figures
14-19,
inclusive,
in
which
C is
shown
as
a
function
of
h
for
selected
values
of
6.
DISCHARGE
OVER
TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
B31
&
I
I
o
I
8
S
5
6
c>
o
o
CO
d d
dO
3niVA
B32
FLOW
OF
WATER
OVER
WEIRS
AND
DAMS
gO'-NOTCH
WEIR
The
most
frequently
used
triangular-notch
weir
is
one
with
a
notch
angle
of
90°
.
Some
of
the
classic
formulas
are
intended
for
use
with
this
weir
alone.
Figure
14
shows
a
comparison
of
values
of
C
computed
from
the
well-known
formulas
of
Thomson,
Barr-Strickland
(eq
8),
Cone
(eq
9,
10),
Greve
(eq
11),
Lenz
(eq
16),
and
King
(eq
18)
and
the
formula
determined
from
equation
25
in
combination
with
figures
12
and
4.
The
Thomson
"formula"
is
actually
just
C=
0.593,
because
Thom-
son
did
not
propose
a correlation
with
h.
It
is
emphasized
that
figure
14
is
a
comparison
of
formulas,
whereas
figure
7
is
a
comparison
of
the
data
from
which
the
formulas
were
derived.
Thus,
the disagreement
shown
in
figure
14,
especially
at
small
values
of
h,
is
to
a
large
degree
evidence
of
inadequacies
of
the
for-
mulas
as
representations
of
the
data
on
which
they
were
based.
Figure
7
shows
that
the
source
data
for
all
the
formulas
agree
remarkably
well
in
defining
C
e
for
use
in
equation
6.
OTHER
NOTCH
ANGLES
Figures
15
through
19
show
comparisons
of
well-known
formulas
for
weirs
with
120°,
60°,
45°,
27°,
and
10°
notch
angles.
The
solid
line
in
each figure was
computed
from
equation
25,
with
values
of
C
e
and
k^
from
figures
12
and
4,
respectively.
The
corresponding
comparisons
of
experimental
data
are
shown
in
figures
6
and
8
through
11.
It
is
demonstrated
again
that
the
solution
derived
from
the
effective-head
concept
is
substantiated
by
the
experimental
data,
whereas
the
classic
formulas
show
justifiable
differences
at
small
values
of
h.
CONCLUSIONS
The
triangular-notch,
thin-plate
weir
is
potentially
an
accurate,
con-
venient
means
of
measuring
the
flow
of
liquids.
Classic
discharge
for-
mulas
are
inadequate,
however,
because
they
fail
to
recognize
the
full
significance
of
the
pertinent
variables.
Although
the
triangular-notch
weir
is
not
subject
to
a
completely
analytical
solution,
available
ex-
perimental
data
are
sufficient
to
substantiate
a practical
solution
which
is
based
on
dimensional
analysis
and
experimental
coefficients.
Limita-
tions
of
the
data
restrict
the
use
of
the
solution
to
water.
The
equation
of
discharge
proposed
in
this
report
is
^
5/2
(6)
z
in
which
h
e
,
the
effective
head,
is
defined
by
the
equation
(5)
and
values
of
k^
are
shown
in
figure
4.
DISCHARGE
OVER
TRIANQULAR-NOTCH
THIN-PLATE
WEIRS
B33
do
amvA
0.64
0.63
EXPLANATION
Thomson
formula
Cone
formula
(eqs
9,
10)
Greve
formula
(eq
11)
Hertzler
formula
(eq
21)
Equation
25
0.56
1.0 1.2
1.4
VALUE
OF
h,
IN
FEET
FIGURE
15.
-Comparison
of formulas
for
notch
angles
of
approximately
120°.
0.64
0.63
0.62
EXPLANATION
Cone
formula
(eqs
9,
10)
King
formula
(eq
19)
Greve
formula
(eq
11)
Lenz
formula
(eq
16)
Equation
25
0,57
1.6
1.0 1.2
1.4
VALUE
OF
h,
IN
FEET
FIGURE
16.-Comparison
of
formulas
for
notch
angles
of
approximately
60
1.8
2.0
2.2
2.4
CO
Cn
0.64
0.63
EXPLANATION
Cone
formula
(eqs
9,
10)
-
Greve
formula
(eq
11)
-
Lenz
formula
(eq
16)
Equation
25
0.57
1.0
1.2
1.4
VALUE
OF
h,
IN
FEET
FIGURE
17.
-Comparison
of
formulas
for
notch
angles
of
approximately 45°.
0.65
0.64
EXPLANATION
Cone
formula
(eqs
9,
10)
- -
Greve
formula
(eq
11)
Lenz
formula
(eq
16)
Equation
25
0.2
0.4
0.6 0.8
1.0
1.2
1.4
1.6 1.8
2.0
2.2
2.4
VALUE
OF
h,
IN
FEET
0.58
0.57
FIGURE
18.
-Comparison
of
formulas
for
notch
angles
of
approximately
27°.
to
CO
W
co
0.68
0.67
-
Lenz
formula
(eq
16)
Equation
25
0.61
0.60
0.2
0.4
1.0
1.2
.1.4
VALUE
OF
h,
IN
FEET
1.6
1.8
2.0
2.2
2.4
FIGURE
19.-Comparison
of
formulas
for
notch
angles
of
approximately
10°.
DISCHARGE
OVER
TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
B39
In
general,
the
coefficient
of
discharge,
C
e
,
is
an
experimentally
determined
function
of
the
geometric
parameters
h/P,
PIB,
and
6.
However,
within
the
range
of
the
most
common
practical
limits
of
h/P
and
PIB,
C
e
is
a
function
of
6
alone
(fig.
12).
In
this
range,
values
of
C
e
computed
from
the
results
of
experiments
by
Barr,
Cone,
Yarnall,
Greve,
Lenz,
and
Numachi,
Kurokawa,
and
Hutizawa
show
remarkable
agreement.
For
0=
90°
the
available
data
are
sufficient
to
define
C
e
over
a
wider
range
of
values
of
hIP
and
PIB
(fig.
13).
REFERENCES
Allerton,
R.
W.,
1932,
Flow
of
water
over
triangular
weirs:
Princeton
University,
Thesis
(mech.
eng.),
56
p.
29
figs.
Barr,
James,
1910,
Experiments
upon
the
flow
of
water
over
triangular
notches:
Engi-
neering
(London),
v.
89,
(April
8
and
15),
p. 435
ff.
Burgess,
J.
S.,
and
White,
W.
R.,
1966,
The
triangular-profile
(Crump)
weir-two-dimen-
sional
study
of
discharge
characteristics,
Hydraulics
Research
Station
(Wallingford,
U.K.),
HRS
Report
INT
52.
Carter,
R.
W.,
1956,
A
comprehensive
discharge
equation
for
rectangular-notch
weirs,
Master's
thesis,
Georgia
Institute
of
Technology.
Cone,
V.
M.,
1916,
Flow
through
weir
notches
with
thin
edges
and
full
contractions:
U.S.
Department
of
Agriculture,
Journal
of
Agricultural
Research,
v.
V,
no.
23
(March
6),
p.
1051.
Cozzens,
H.
A.,
Jr.,
1915,
Flow
over
V-notch
weirs:
Power,
v.
42,
no.
21
(November
23),
p.
714.
Greve,
F.
W.,
1932,
Flow
of
water
through
circular,
parabolic,
and
triangular
vertical-
notch
weirs:
(Purdue
Univ.,
Eng.
Bull.,
v.
XVI,
no.
2,
Research
Series
No.
40
(March),
84
p.,
15
figs.
Hertzler,
R.
A.,
1938,
Determination
of
a
formula
for
the
120°
V-notch
weir:
Civil
Eng.
(November),
p.
756.
Ho,
Chitty,
and
Wu,
S.
L.,
1931,
The
flow
of
water
over
sharp
crested
weir
notches-
rectangular,
trapezoidal,
and
triangular:
Cornell
Univ.,
Master's
thesis,
155
p.,
78
figs.
International
Standards
Organization,
1975,
Liquid
flow
measurement
in
open
channels
using
thin-plate
weirs
and
venturi
flumes
(ISO
1438-1975).
Kindsvater,
C.
E.,
and
Carter,
R.
W.,
1959,
Discharge
characteristics
of
rectangular
thin-plate
weirs:
Am.
Soc.,
Civil
Engineers
Trans.,
v.
124,
p.
772.
Kindsvater,
Carl
E.,
1964,
Discharge
characteristics
of
embankment-shaped
weirs:
U.S.
Geol.
Survey
Water-Supply
Paper
1617-A,
114
p.,
57
figs.
King,
H.
W.,
1916,
Flow
of
water
over
right-angled
V-notch
weir:
Univ., Michigan
Technic,
v.
29, no.
3
(October),
p.
189.
1954,
Handbook
of
Hydraulics
(Revised
by
Ernest
F.
Brater):
New
York,
McGraw-Hill
Book
Co.,
567
p.,
165
figs.
Lenz,
A.
T.,
1943,
Viscosity
and
surface
tension
effects
on
V-notch
weir
coefficients:
Am.
Soc.
Civil
Engineers
Trans.,
v.
108,
p.
759.
Mawson,
Humbert,
1927,
Applications
of
the
principles
of
dimensional
and
dynamical
similarity
to
the
flow
of
liquids
through
orifices,
notches
and
weirs:
Inst.
Mech.
Engineers,
Proc.,
v.
1,
p.
1033.
Numachi,
F.,
Kurokawa,
T.,
and
Hutizawa,
S.,
1940,
Uber
den
Uberfallbeiwert
eines
rechtwinkelig-dreieckigen
Messwehrs:
Soc.
Mech.
Engineeers
(Japan)
Trans.,
v.
6,
no.
22,
(February),
p.
110.
B40
FLOW
OF
WATER
OVER
WEIRS
AND
DAMS
1941,
Uber
den
Uberfallbeiwert
eines
rechtwinkelig-dreieckigen
Messwehrs:
Tohoku
Imperial
Univ.,
(Japan)
Tech.
reports,
v.
13,
no.
2,
p.
350.
-1943,
Uber
den
Uberfallbeiwert
eines
rechtwinkelig-dreieckigen
Messwehrs,
2.
Mitteilung:
Tohoku
Imperial
Univ.,
(Japan)
Tech.
reports,
v.
13,
no.
3,
p.
473.
Rehbock,
Th.,
1929,
discussion
of
paper
by
Ernest
W.
Schoder
and
Kenneth
B.
Turner,
Precise
weir
measurements:
Am.
Soc.
Civil
Engineers
Trans.,
v.
93,
p. 1148.
Schlag,
Albert,
1962,
Note
sur
la
mesure des
debits
pour
deversoir
triangulare,
La
Tri-
bune
de
Cebedeau
(Liege,
Belgium),
v.
15,
no.
218,
p. 22.
1962b,
Formule
de
debit
de
deversoirs
dont
le
seuil
est
constitue
par
une
s£rie
de
dents
situees
dans
un
plan
horizontal,
La Tribune
du Cebedeau
(Liege,
Belgium),
v.
15,
no.
221,
p.
180.
Smith,
E.
S.,
Jr.,
1934,
The
V-notch
weir
for
hot
water:
Am.
Soc.
Mech.
Engineers
Trans.,
v.
56,
p.
787.
1935,
The
V-notch
weir
for
hot
water:
Am.
Soc.
Mech.
Engineers
Trans.,
v.
57,
p.
249.
Strickland,
T.
P.,
1910,
Mr.
James
Barr's
experiments
upon
the
flow
of
water
over
tri-
angular
notches:
Engineering
(London),
v.
90,
(October
28),
p.
598.
Switzer,
F.
G.,
1915,
Tests
of
the
effect
of
temperature
on
weir
coefficients:
Engineering
News,
v.
73, no.
13,
(April
1),
p.
636.
Thomson,
James,
1858,
On
experiments
on
the
measurement
of
water
by
triangular
notches
in
weir
boards:
Brit.
Assoc.
Adv.
Sci.,
Annual
report,
p.
181.
1861,
On
experiments
on
the
measurement
of
water
by
triangular
notches
in
weir
boards:
Brit.
Assoc.
Adv.
Sci.,
Annual
report,
p.
151.
Thornton,
B.
M.,
1929,
Measurement
of
fluid
flow
with
triangular
notches:
Power
Engineer
(August),
London,
v.
24,
p.
314.
Tracy,
H.
J.,
1957,
Discharge
characteristics
of
broad-crested
weirs:
U.S.
Geological
Survey
Circ.
397,
15
p.,
11
figs.
Yarnall,
D.
R.,
1912,
the
V-notch
weir
method
of
measurement:
Am.
Soc.
Mech.
Engineers
Trans.,
v.
34,
p.
1055.
1926,
Accuracy of
the
V-notch
weir
method
of
measurement:
Am.
Soc.
Mech.
Engineers
Trans.,
v.
48,
p.
939.
SUPPLEMENTAL
INFORMATION
B42
FLOW
OF
WATER
OVER
WEIRS
AND
DAMS
REQUIREMENTS
FOR
PRECISE
MEASUREMENTS
SPECIFICATIONS
FOR
THE
INSTALLATION
Use
of
the
triangular-notch,
thin-plate
weir
for
precise
measure-
ments
is
restricted
to
steady,
free,
and
fully
ventilated
flows.
The
recommended
coefficients
are
applicable
for
water
only,
in
the
approx-
imate
range
of
temperatures
from
40°
F
to
85°
F.
General
specifications
for
a
satisfactory
weir
installation
are
de-
scribed
on
page
B2.
Additional
restrictions
related to
the
actual
measurements
are
discussed
below.
RESTRICTIONS
ON
THE
GEOMETRIC PARAMETERS
Values
of
v
less
than
20°
or
greater
than
100°
are
not
recommended
for
precise
measurements.
Experimental
data
for
weirs outside
this
range are
limited.
Furthermore,
the
data
available
indicate
that
weirs
with
very
small
and
very
large
notch
angles
exhibit
characteristics
of
instability
which
result
from
the
fact
that
the
nappe
intermittently
clings
to
the
upper
surfaces
of
the
crest.
Practical
restrictions
on
hIP
and
PIE
are
suggested
by
the
observa-
tion
that
head-measurement
difficulties
and
errors
result
from
surges
and
waves
which
occur
in
the
approach
channel when
the
velocity
of
ap-
proach
is
large
in
comparison
with
the
depth
of
flow.
The
available
data
are
not
adequate
to
establish
the
limiting
values
of
hIP
and
PIB
which
are
associated
with
this
condition.
Therefore,
the
user
himself
must
determine
practical
limits
which
are
consistent
with
the
required
ac-
curacy
for
head
measurements.
These
limits
are
separate
from
restric-
tions
on
the
use
of
figure
12,
which
is
applicable
only
when
the
effects
of
hIP
and
PIB
are
negligible.
RESTRICTIONS
ON
h
AND
P
Restrictions
on
the
magnitude
of
h
are
related
to
the
unpredictable,
unsteady
clinging
phenomena
which
occur
at
small
heads.
To
ensure
a
freely
discharging,
stable
nappe,
a
minimum
value
of
h=Q.2
foot
is
recommended.
There
is
disagreement
in
the
literature
regarding
an
independent
correlation
between
P
and
the
coefficient
of discharge.
It
is
tentatively
recommended
that
P
be
limited
to
values
greater
than
0.3
foot.
EFFECT
OF
NEGLECTING
k
k
It
is
apparent
from
equations
5
and
6
that
the
relative
influence
of
kh
decreases
as
h
increases
in
magnitude.
Consequently,
the
error
which
results
from
using
h
instead
of
h
e
in
equation
6
is
appreciable
only
for
small
values
of
h.
The
relative
error
in
the
discharge
is
plotted
as
a
function
of
h
in
figure
20.
DISCHARGE
OVER
TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
B43
0.4
0.8
1.2
VALUE
OF
h,
IN
FEET
1.6
2.0
FIGURE
20.
-Effect
of
using
h
instead
of
h
e
in
equation
6.
EFFECT
OF
APPROACH-CHANNEL
CONDITIONS
Specifications
for
a satisfactory
weir
installation
include
the
require-
ment
that
turbulence
and
velocity
in
the
channel
upstream
from
the
weir
be
such
as
to
simulate
normal
(uniform
flow)
conditions
in
a
smooth,
horizontal,
rectangular
channel.
If
the
effective
notch
area
is
very
small
in
comparison
with
the
area
of
the
approach
channel,
ap-
proach
velocities
are
negligible,
and
the
shape
of
the
channel
is
in-
significant.
Short
channels
are
satisfactory
if
they
are
provided
with
baffles
capable
of
producing
a
nearly
normal
turbulence
and
velocity
distribution.
When
in
doubt,
the
velocity
distribution
should
be
checked
with
a
velocity
traverse
located
at
or
near
the
headwater-gage
section.
The
experimental
data
available
are
inadequate
to
evaluate
the
influence
of
velocity
distribution
over
a
full
range
of
values
of
v,
hIP,
and
PIB.
However,
the
remarkable
consistency
and
agreement
shown
by
the
data
plotted
in
figures
6
through
11
indicate
a
corresponding
lack
of
correlation
with
the different
approach-channel
conditions
which
are
represented
by
those
data.
Therefore,
in
the
range
of
values
of
h/P
from
0.03
to
0.35
and
PIB from
0.1
to
1.5,
the
influence
of
approach-channel
velocity
distribution
is
believed
to
be negligible.
B44
FLOW
OF
WATER
OVER
WEIRS
AND
DAMS
MEASUREMENT
OF
v
Precise
discharge
computations
require
that
v
be
measured
accurate-
ly.
One
of
several
satisfactory
methods
of
measuring
v
is
described:
(1)
two
true
disks
of
different,
micrometered
diameters
are
placed
in
the
notch
with
their
edges
tangent
to
the
sides of
the
notch;
(2)
the
vertical
distance
between
the
centers
(or
two
corresponding
edges)
of
the
two
disks
is
measured
with
a
micrometer
caliper;
(3)
the
angle
v
is
twice
the
angle
whose
sine
is
equal
to
the
difference
between
the
radii
of
the
disks
divided
by
the
distance
between
the
centers
of
the
disks.
Other
equally
satisfactory
methods
of
measuring
v
are
described
in
the
listed
references.
MEASUREMENT
OF
h
The
head
is
measured
with
a
hook
gage,
point
gage,
or
precise
ma-
nometer.
Hook
and
point
gages
preferably
are
used
in
a
stilling
well.
However,
if
approach
velocities
and
surface
disturbances
in
the
ap-
proach
channel
are
negligible,
the
gages
can
be
mounted
over
the
head-
water
surfaces.
Stilling
wells
and
manometers
are
connected to
piezometers
located
in
the
floor
or
walls
of
the
channel.
To
prevent
er-
rors
due
to
excessive
head
losses
or
surface
drawdown,
the
piezometnc
section
is
located
upstream
from
the
weir
a
distance
equal
to
from
four
to
five
times
the
maximum
head.
Gages
are
mounted
as
close
to
the
weir
as
possible
in
order
to
avoid
errors
in
the
gage
zero
due
to
deflec-
tion
or
movement
under
different
water
loads.
DETERMINATION
OF
GAGE
ZERO
Accuracy
of
head
measurements
is
critically
dependent
upon
the
determination
of
the
gage
zero,
which
is
defined
as
the
gage
reading
corresponding
to
the
level
of
the
vertex
of
the
notch.
Numerous
accept-
able
methods
of
determining
the
gage
zero
are
in
use.
One
such
method
is
described:
(1)
still
water
in
the
channel
upstream
from
the
weir
is
drawn
to
a
level below
the
vertex
of
the
notch;
(2)
a
temporary,
precise
hook
gage
is
mounted
over
the
approach
channel,
with
its
point
a
short
distance
upstream
from
the
weir
plate;
(3)
a
true
cylinder
of
known
(micrometered)
diameter
is
placed
with
its
axis
horizontal,
with
one
end
resting
in
the
notch
and
the
other
end
balanced
on
the
point
of
the
tem-
porary
hook
gage;
(4)
a
machinist's
level
is
placed
on
the
top
of
the
cylinder
and the
hook
gage
is
adjusted
to
make
the
cylinder
precisely
horizontal;
(5)
the
reading
of
the
temporary
gage
is
recorded;
and
(6)
the
temporary
hook
gage
is
lowered
to
the
water
surface
in
the
ap-
proach
channel
and
the reading
is
recorded.
DISCHARGE
OVER
TRIANGULAR-NOTCH
THIN-PLATE
WEIRS
B45
The
permanent
headwater
gage
is
adjusted
to
read
the
level
in
the
stilling
well,
and this
reading
is
recorded;
(7)
the
distance
from
the
bot-
tom
of
the
cylinder
to
the
vertex
of
the
notch
is
computed
with
the
known
values
of
v
and
the
diameter
of
the
cylinder;
(8)
the
vertical
distance from
the
vertex
of
the
notch
to the
still
surface
is
computed
from
the
readings
in
step
5
and
6
and the
computation
in
step
7;
(9)
finally,
the
zero
reading
on
the
permanent
gage
is
computed
as
its
reading
on
the
still
water
surface
plus
the
computed
distance
from
the
vertex
to
the
still
surface.
An
obvious
advantage
of
this
method
is
that
it
refers
the
gage
zero
to the
geometrical
vertex
which
is
defined
by
the
sides
of
the
notch.
Studies
of
Flow
of
Water
Over
Weirs
and
Dams
GEOLOGICAL
SURVEY
WATER-SUPPLY
PAPER
1617
This
volume
was
published
as
separate
chapters
A
-B
UNITED
STATES
DEPARTMENT
OF
THE
INTERIOR
JAMES
G.
WATT,
Secretaiy
GEOLOGICAL
SURVEY
Doyle
G.
Frederick,
Acting
Director
CONTENTS
[Letters
designate
the
chapters]
(A)
Studies
of
Flow
of
Water
Over
Weirs and
Dams-Discharge
Characteristics
of
Embankment-Shaped
Weirs,
by
Carl
E.
Kindsvater.
(B)
Studies
of
Flow
of
Water
Over
Weirs
and
Dams-Discharge
Characteristics
of
Triangular-Notch
Thin-Plate
Weirs,
by
John
Shen.