Register to enable "Calculate" button. Demonstration mode for throat width b of 0.5 m (cookies must be enabled).
Units in Parshall Flume calculation: cm=centimeter, ft=foot, gal=U.S. gallon, hr=hour, m=meter, MGD=million gallons (US) per day, min=minute, s=second
Comparison of ASTM D1941 and ISO 9826 Variables
Our Parshall flume calculation is based on the ISO 9826 (1992) standard. The
standard is valid for submerged as well as free-flowing Parshall flumes. A free flowing
flume can be identified by the drop in water depth at the flume throat. In submerged
flow, the downstream water backs up into the throat swallowing the drop making the drop
difficult or impossible to identify. Analysis of submerged flow requires two head
measurements - one in the approach channel and one in the throat. Free flow
requires only the upstream head measurement.
Parshall flumes must be built with their dimensions in strict accordance with
specifications in published documents such as the ISO 9826 and ASTM D1941 (1991) standards
or USBR (1997). Flumes (like weirs) are designed to force a transition from
sub-critical to super-critical flow. In the case of Parshall flumes, the transition is
caused by designing flumes to have a narrowing at the throat and a drop in the channel
bottom. Such a transition causes flow to pass through critical depth in the flume
throat. At the critical depth, energy is minimized and there is a direct relationship
between water depth and velocity (and flowrate). However, it is physically very difficult
to measure critical depth in a flume because its exact location is difficult to determine
and may vary with flowrate. Through mass conservation, the upstream depth is related to
the critical depth. Therefore, discharge can be determined by measuring the upstream depth,
which is a highly reliable measurement.
Equations and Methodology
The methodology for our Parshall flume calculation follows that of ISO 9826 (1992).
ASTM D 1941 (1991) also addresses Parshall flumes but has pages of tabular data
which are more difficult to implement into a computer program compared to the figures and
equations of ISO 9826.
Variable definitions can be found in the Variables section.
The LMNO Engineering calculation allows 0≤h≤3 m and 0.01<b<16 m, but the
calculation is most accurate when used within the ISO 9826 recommendations of h≤2
m and 0.152 ≤ b ≤ 15.24 m.
For b≤0.152 m, C and n values are from Herschy (1995). For b>0.152 m, C and n
values are from ISO 9826 (1992), equations 10 and 11.
Free flow occurs when a hydraulic jump is visible at the throat; that is,
when the downstream head is significantly less than the upstream head. Our
calculation defines free flow as occurring when H/h≤0.6 for b<3.05 m or when
H/h≤0.8 for b≥3.05 m. These criteria (called "modular limits") are
similar, but not identical, to the ISO 9826 criteria.
For free flow,
Q = C hn where Q is in m3/s and h is in m
Submerged flow occurs when a hydraulic jump is not visible at the throat;
that is, when the downstream head is sufficiently high that it "drowns out" or
"swallows up" the hydraulic jump. In our calculation, submerged flow
occurs when H/h>0.6 for b<3.05 m and when H/h>0.8 for b≥3.05 m.
For submerged flow, ISO equation 12 is re-written as:
Q = C hn - Qe where C and n are found from the
above figure based on width (b). Qe accounts for the effects of
For b<3.05 m, ISO 9826 equation 13 provides the following equation for Qe
which is implemented in our calculation:
For b≥3.05 m, Qe=CsQ3
Cs =(0.3281)b. ISO 9826 Figure 2 is a graph of Q3 as a
function of H/h and h. LMNO Engineering fit equations to all of the lines in
the ISO figure for use in our calculation. A graph using our equations for selected
H/h ratios is shown:
Comparison of ISO and ASTM methods
Both ISO 9826 and ASTM D1941 present methods for computing discharge through Parshall
flumes. Since a Parshall flume is a standard flume, the two methods should be
similar. Looking at the two standards, they at first appear somewhat different
because ISO 9826 is in SI units while ASTM D1941 uses predominantly English units.
Further, the ISO standard presents information in tables, equations, and figures while
ASTM D1941 uses tables almost exclusively. Curious as to how well the two methods
compare, we developed the following table. We also have done other comparisons but,
due to space considerations, have chosen not to show the results on this web page.
In general, there is good agreement for free flow, but in some cases the submerged
flow rates are significantly different, such as for the b=0.152 m case shown below.
|Comparison of ASTM D1941 and ISO 9826
||Upstream Head, h
||ASTM Flow, Q
||ISO Flow, Q
|(1) based on Table 2 in ASTM D1941. (2)
based on Equation 10 in ISO 9826.
(3) based on Tables 2 and 6B in ASTM D1941.
(4) based on Equations 10, 12, and 13 in ISO 9826.
(5) based on Tables 2, 9A, and 9C in ASTM D1941.
(6) based on Equations 11, 12, and 14 and Figure 2 in ISO 9826.
ISO 9826 specifies the indicated units for the equations shown above. Our
calculation allows you to select a variety of units from dropdown menus.
b=Throat width [m].
C=Parshall flume constant [empirical units].
Cs=Submergence coefficient [unit-less]. This is not the submergence
h=Measured upstream head [m].
H=Measured downstream head [m]. Only needed if the flume is submerged, or to
determine mathematically if the flume is submerged. Usually, one can visually see if
there is a hydraulic jump, but determining the ratio H/h is a quantitative method.
H/h=Submergence ratio. Flume is submerged if H/h>0.6 for b<3.05m or if
H/h>0.8 for b≥3.05 m.
n=Parshall flume power constant [unit-less].
Q=Flow rate (discharge) through flume [m3/s].
Qe=Reduction in flow rate due to submergence [m3/s].
Q3=Flow factor for determining Qe if b≥3.05 m [m3/s].
Error Messages given by calculation
"Need h ≥ 0". Negative head was entered. If h=0,
calculation automatically sets Q=0.
"Need h ≤ 3 m". Head cannot exceed 3 m.
"Need H > 0". For submerged flow, downstream head must be
"Need H/h > 0", "Need H/h ≤ 1". If
submerged flow is selected, H/h must be in this range.
"Need b > 0". Throat width must be positive.
"Need 0.01≤b≤16 m". Flume throat width must be in this
"Qe will be > Chn ". Message will only appear if submerged flow. Input values result in negative Q.
Usually this occurs with very small upstream heads h and when H/h>0.6 resulting in Qe > Chn. See variables and equations for Qe, C, and n.
Input checks for graph. If one of these messages
appears, the graph will not proceed. Note that if any value is out of range in the
upper portion of the calculation, a graph will not be shown.
"Min h must be ≥0", "Min H/h must be ≥0".
Minimum head or H/h ratio entered for graph cannot be < 0.
"Max h must be ≤ 3 m". Graph has maximum limit of h=3 m.
"Need 0.6<Max H/h≤1". Message will only appear if
b<3.05 m. Q is independent of H/h until H/h becomes greater than 0.6. So to
avoid a "boring" graph showing a constant value for Q, the calculation requires
that max H/h be in the range where submergence affects Q.
"Need 0.8<Max H/h≤1". Message will only appear if
b≥3.05 m. Q is independent of H/h until H/h becomes greater than 0.8. So
to avoid a "boring" graph showing a constant value for Q, the calculation
requires that max H/h be in the range where submergence affects Q.
"Min/Max must be ≤ 0.99". Minimum value entered for graph must
be less than 0.99 times maximum value entered for graph. Otherwise, the minimum and
maximum are too close together to have good axis labels for the graph.
"Min must be < Max". Minimum value entered for graph must be
less than maximum value entered for graph.
Run-time errors. The following message may be generated
by the graphing portion of the calculation:
"No graph for input range". The entire range from minimum to maximum results in parameters that are out of the range of validity of the flume equations. Usually this occurs for submerged flow with very small upstream heads h and when H/h>0.6 resulting in Qe > Chn. See variables and equations for Qe, C, and n.
"Q=0 when low h and/or high H/h".
Some heads in the range entered for the graph result in parameters that are invalid,
so those could not be computed and were plotted at Q=0. Message appears on graph and table pages.
When the graph "Q vs. H/h (h constant)" is selected, you may notice a
discontinuity in the graph at H/h=0.6 for b<3.05 m or H/h=0.8 for b≥3.05 m.
The discontinuity occurs because the flow is transitioning from free flow to submerged
flow. For some ranges of H/h, you may observe something similar to the following:
Graph of Q vs. H/h, for b=0.5 m and h=0.5 m
The discharge for H/h<0.6 does not appear to be shown. However, our software
scales the y-axis based on the maximum value on the curve. In this case, the maximum
value on the curve is 0.398 m3/s which blends in with the boxed outline of the
graph. The flow is 0.398 m3/s for all H/h <0.6.
Back to calculation
American Society for Testing and Materials (ASTM D1941-91). 1991. Standard
test method for open channel flow measurement of water with the Parshall flume.
Available at http://www.astm.org.
Herschy, Reginald W. 1995. Streamflow Measurement. E & FN Spon
(an imprint of Chapman and Hall). 2ed.
International Organization of Standards (ISO 9826). 1992. Measurement of
liquid flow in open channels - Parshall and SANIIRI flumes. Reference number: ISO
9826:1992(E). ISO documents can be downloaded as .PDF files for a fee at http://webstore.ansi.org.
USBR. 1997. U.S. Department of the Interior, Bureau of Reclamation.
Water Measurement Manual. 1997. 3ed. Available from http://www.usbr.gov/tsc/techreferences/mands/wmm/index.htm .
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Software, Ltd. All rights reserved.
Please contact us for consulting or questions about Parshall flumes.
LMNO Engineering, Research, and Software, Ltd.
7860 Angel Ridge Rd. Athens, Ohio 45701 USA Phone: (740) 707-2614
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