California State University Sacramento                             Department of Civil Engineering
Department of Civil Engineering                                                Instructor      MEH

For general information go to the Background Presentation

FLOW OVER A SHARP-CREASTED WEIR -- PROCEDURES

References:
Roberson, J.A. and C. T. Crowe, Engineering Fluid Mechanics, 6th ed., John Wiley and Sons, 1997, pp. 542-546
Daugherty, R., J. Franzini, and E. J. Finnemore, Fluid Mechanics with Engineering Applications, 8th ed., McGraw-Hill, Inc., 1985.


Objectives:
            To examine the fundamental characteristics of flow over two sharp-crested weirs
            To measure the coefficient discharge values of rectangular and triangular weirs
            To gather pressure information for a future lab on hydrostatic forces

Apparatus:
            One-half meter flume and sharp-crested weir with manometer board
            V-notch weir in return-flow channel
            Point gages and manometer board /piezometers

Experimental Procedure:
   Set up for the experiment.
   Open the surge tank valve and turn on the large pump.
   Close the drain valve on the upstream side of the flume head tank.

   Forces On Rectangular Weir
When the water just covers the flume bottom, read the piezometer heights.
These tell you the elevations of the taps.
Check that the water height is at the weir crest elevation
and that the piezometer tubing doesn’t have any air in it.
   Forces On Rectangular Weir (cont)

    Measure the flow profile and pressure on the weir at one medium flow rate

Establish the flow over the weir crest necessary to obtain a head H of about 0.3-ft .
Determine the discharge from the flow meters.
Make sure the vent is open.
Record the height of each of the piezometer columns.
Some of the piezometers record the pressure on the face of the weir;
the others record the pressure on the bottom of the flume.
Record the point gage readings at each flume tap position.
Close the valve on the ventilation pipe at the base of the weir
Note the change in the nappe profile and level of water backed up against
the downstream face of the weir.

Calibrate the rectangular and V-notch weirs.
Establish a steady flow and record the discharge and water levels (head) at both weirs.
Note: Storage of water in the channel may cause the V-notch weir head to stabilize slowly,
so don’t record the height prematurely.
Repeat the previous step at least five more times.

Shut-down


FLOW OVER A SHARP-CRESTED WEIR -- RESULTS

Format: Memo Report [Include your team logo somewhere in the report.]


SUMMARY

Present the key results and describe any major deviations from the printed procedures and why you did them.

You do not need to turn in the lab procedure sheet with your report, but it is ok to add it as an attachment. You may use a computer sketch of the apparatus in the body of the report, but the attachment must be hand drawn.

RESULTS:


Plot the approaching head and flow data for the vented rectangular weir, and the V-notch weir on a graph with log-log-scaled paper. Determine the unconstrained equations of the rating curve for each device. Comment on the linearity of your plotted rating curves in terms of standard deviation and coefficient of determination.

Compare your experimental values for the vented rectangular weir and the V-notch weir with literature equations or graphs such as the equations in Ch. 13 of Roberson & Crowe.

Plot the water surface profiles from the point gage and piezometer readings for the vented and the unvented rectangular weirs for a single Q only. Comment on any differences you observe between the point gage data and the piezometer data.

Plot the pressure distribution curve from your manometer data on the upstream face of the rectangular sharp-crested weir. Calculate the force on the weir by integration of the pressure distribution and compare this value with that obtained by assuming a linear hydrostatic pressure distribution.

ATTACHMENTS:
Discussion questions
Are the values of the exponent on the approaching head and the weir coefficient consistent with theory and empirical relations in the literature? Using an exponent of 1.5 for the heads on the rectangular weir and 2.5 on the V-notch weir, compute the weir coefficients for both weirs at each experimental flow rate. Is the use of constants for the exponent and the coefficient acceptable?

Compare the performance of the V-notch weir with that of the rectangular weir at both high and low flows.
For the convenience of computation, the hydrostatic assumption has been widely used by the engineers. Do you think the assumption is acceptable in terms of accuracy and magnitude? Overestimated or underestimated?



CALIBRATE SHARP-CRESTED WEIRS: INPUT (OBSERVED) DATA


Lab. Team:                                                                              Date of Experiment: 
        Lab Team Members:


--------------------------------- CONSTANT DATA ----------------------------------
Water Temperature ________° F                    Rectangular Channel Width ________ ft
Rectangular Weir: By Manometer at Crest ________ in, & at Bottom: ________ in.
                             By Point Gage at Crest ________ ft, & at Bottom: ________ ft.
V-notch Weir: Channel Bottom-to-Notch ________ ft          V-notch Angle ____°

------------------------------- VARIABLE DATA --------------------------------------

Flow Rectangular Weir V-Notch
Run Meter Point Gage Manometer Point Gage
No. (gpm) (ft) (in) (ft)
1
2
3
4
5
6
7

Pressure Forces on Rectangular Weir At Q = _________ gpm

    Note: This table assumes tap A is at the top.

Tap Manometer Heads
Tap Elevation No Flow With Flow
(in) (in) (in)
Crest
A
B
C
D
E
F

Observe shapes for flows over the two weirs at a high flow rate. Sketch the patterns. Note the conditions near the rectangular weir for both vented and non-vented flows.


FLOW PROFILE WITH SHARP-CRESTED WEIR: INPUT (OBSERVED) DATA


CONSTANT DATA
Profile Run Flow Rate: ________ gpm           Rectangular Flume Width: ________ ft
Rectangular Weir Height: ________ ft

VARIABLE DATA

Flow Profile Along Rectangular Channel:

                                                    Zeroing Datums                                Reading With Flow

Tap         Distance to           Point Gage (ft)           Manometer           Point Gage      Manometer

No.          Tap (ft)           Bottom      Slight Flow      Head (in)         at Surface (ft)   Heads (in)

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


  1

  2

  3

  4

  5

  6

  7

  8

  9

10

11

12

13

14