OpenFlow Measure

Professional Hydraulic Engineering & Design Suite

Physics-based open channel flow analysis and primary measurement device sizing for weirs and flumes

1. Introduction & Overview

🎯 What Are Discharge Measurement Devices?

Discharge measurement devices (also called primary measurement devices or flow measurement structures) are engineered hydraulic structures installed in open channels to accurately measure water flow rates. These devices work by creating a known relationship between water level (stage) and discharge (flow rate).

Key Applications:

  • Regulatory Compliance: EPA discharge permits, water rights enforcement, environmental monitoring
  • Process Control: Wastewater treatment plants, industrial processes, irrigation systems
  • Hydrologic Studies: Stream gauging, stormwater management, flood monitoring
  • Water Accounting: Municipal water supply, agricultural distribution, billing/allocation

How They Work: By constricting flow through a calibrated geometry (weir notch or flume throat), these devices force a predictable stage-discharge relationship. Measuring water level at a specific location allows precise flow rate calculation using empirical equations validated through decades of research and standardized by organizations like ASTM, ISO, and USGS.

📚 Measurement Devices Covered in This Guide

Rectangular Weirs

Suppressed & contracted configurations. Ideal for medium flows in rectangular channels. Simple construction, ISO 1438 compliant.

V-Notch Weirs

Triangular (90° or 60°) sharp-crested weirs. Excellent for low flows with wide measurement range (25:1). ISO 4360 standard.

Cipoletti Weirs

Trapezoidal weirs with 1H:4V side slopes. Self-compensating for end contractions. Popular in irrigation and water rights.

Broad-Crested Weirs

Long horizontal crest structures. Used in dam spillways and high-flow applications. Excellent structural stability.

Parshall Flumes

Converging-throat flumes with self-scouring action. ASTM D1941 standard. Best for wastewater and sediment-laden flows.

Venturi Flumes

Smooth-transition flumes with minimal head loss (8-12%). High accuracy for clean industrial and municipal flows.

OpenFlow Measure is a specialized hydraulic engineering tool designed for civil engineers, hydrologists, and water resource professionals. It bridges the gap between channel analysis and measurement structure design through an integrated, two-module approach.

Key Distinction: Unlike standalone calculators, OpenFlow Measure ensures your measurement device is hydraulically compatible with the channel it will be installed in.

Core Modules

Module 1: Channel Definition & Analysis

  • Solves Manning’s Equation for uniform flow conditions
  • Calculates normal depth, velocity, and hydraulic radius
  • Determines flow regime via Froude Number analysis
  • Provides real-time SVG cross-section visualization

Module 2: Measurement Device Design

  • Weirs: Sharp-crested rectangular, V-notch, and Cipoletti designs
  • Flumes: Parshall and Venturi configurations
  • Stage-discharge relationship calculations
  • Automatic compatibility checking with channel geometry
  • 3D visualization of installed structures

Visual Feedback: Geometric conflicts (e.g., device taller than channel banks) are flagged immediately through the integrated visualization system.

2. Theoretical Background

Manning’s Equation for Open Channel Flow

Manning’s Equation is the fundamental relationship for uniform open channel flow, connecting velocity to channel characteristics and slope.

V = (1 / n) × R2/3 × S1/2

Variables:

  • V = Average flow velocity (m/s)
  • n = Manning’s roughness coefficient (dimensionless)
  • R = Hydraulic radius = Flow Area ÷ Wetted Perimeter (m)
  • S = Longitudinal bed slope (m/m)

Manning’s n Values: Concrete (0.012-0.014), Clean earth (0.022-0.030), Gravel bed (0.025-0.035), Vegetated channels (0.030-0.150)

Discharge Calculation:

Q = A × V

Where Q = Discharge (m³/s) and A = Cross-sectional flow area (m²)

Froude Number & Flow Regime Classification

The Froude Number determines whether flow is subcritical, critical, or supercritical.

Fr = V / √(g × Dh)

Where:

  • V = Average flow velocity (m/s)
  • g = Gravitational acceleration (9.81 m/s²)
  • Dh = Hydraulic depth = A / Top Width (m)

Flow Classification:

  • Fr < 1: Subcritical (tranquil, deep, slow-moving)
  • Fr = 1: Critical flow (transition state)
  • Fr > 1: Supercritical (rapid, shallow, fast-moving)

3. Complete Formula Reference

Weir Formulas

Rectangular Suppressed Weir

A suppressed weir extends across the full channel width, eliminating side contractions.

Q = 1.84 × L × H1.5

Q = Discharge (m³/s)

L = Crest length (m)

H = Head above crest (m)

Limitations:

  • H/P < 2.0 (P = crest height above bed)
  • Minimum H ≥ 0.05 m
  • Free nappe required (no submergence)
  • L/H > 3 for accurate measurements

Rectangular Contracted Weir

When the weir is narrower than the channel, side contractions reduce effective length.

Q = 1.84 × (L – 0.1 × n × H) × H1.5

Q = Discharge (m³/s)

L = Physical crest length (m)

n = Number of end contractions (typically 2)

H = Head above crest (m)

Note: Each contraction reduces effective length by 0.1H meters

V-Notch (Triangular) Weir

General Formula (Any Angle):

Q = (8/15) × Cd × √(2g) × tan(θ/2) × H2.5

90° V-Notch Simplified (Thomson Equation):

Q = 1.38 × H2.5

Q = Discharge (m³/s)

Cd = Discharge coefficient (0.58-0.62)

θ = Notch angle (90° or 60° common)

H = Head above weir vertex (m)

g = 9.81 m/s²

Advantages: H2.5 relationship provides excellent sensitivity for low flows (25:1 range)

Cipoletti (Trapezoidal) Weir

Trapezoidal weir with side slopes at 1H:4V (14° from vertical).

Q = 1.859 × L × H1.5

Q = Discharge (m³/s)

L = Bottom crest length (m)

H = Head above crest (m)

Key Feature: The 1:4 side slopes automatically compensate for end contractions—no correction factors needed

Broad-Crested Weir

Long crest length (B/H > 2) forces critical flow on the crest.

Q = Cd × L × √(2g) × H1.5

Q = Discharge (m³/s)

Cd = Discharge coefficient (0.82-0.90)

L = Weir length perpendicular to flow (m)

H = Head above crest (m)

B = Crest width parallel to flow (m)

g = 9.81 m/s²

Flume Formulas

Parshall Flume

Free-Flow Equation:

Q = K × Han

Q = Discharge (m³/s)

K = Throat-specific coefficient

n = Throat-specific exponent

Ha = Head at upstream gauge (m)

Throat-Specific Coefficients (SI Units):

Throat Width (W) K n Flow Range (m³/s)
76 mm (3″)0.1761.550.0014 – 0.0085
152 mm (6″)0.3811.580.0042 – 0.054
229 mm (9″)0.5351.530.0085 – 0.110
305 mm (1 ft)0.6901.5220.011 – 0.252
610 mm (2 ft)1.4261.5470.028 – 0.937
914 mm (3 ft)2.1481.5660.045 – 1.922

Submergence Warning: When Hb/Ha > 0.70, flow becomes submerged and correction factors apply

Venturi Flume

Q = Cd × Wt × √(g) × H1.5

Q = Discharge (m³/s)

Cd = Discharge coefficient (0.92-0.98)

Wt = Throat width (m)

H = Upstream head above throat invert (m)

g = 9.81 m/s²

Advantages: Head loss: 8-12% (vs. 30-50% for weirs), Accuracy: ±2-4%

4. Step-by-Step Tutorials

Example 1: Rectangular Suppressed Weir

Problem: Calculate discharge over a rectangular suppressed weir with detailed step-by-step calculations.

📝 Given Data

  • Weir length (L) = 2.5 m
  • Head over crest (H) = 0.40 m
  • Crest height (P) = 0.80 m

📐 Formula

Q = 1.84 × L × H1.5

🔍 Step-by-Step Solution

Step 1: Verify Design Constraints

Check H/P ratio: H/P = 0.40/0.80 = 0.5
✓ Passes (must be < 2.0)

Step 2: Calculate H1.5

H1.5 = (0.40)1.5
= 0.40 × √(0.40)
= 0.40 × 0.6325
= 0.2530

Step 3: Apply the Formula

Q = 1.84 × L × H1.5
Q = 1.84 × 2.5 × 0.2530
Q = 4.6 × 0.2530

Step 4: Final Answer

Q = 1.164 m³/s = 1,164 L/s

✅ Verification

Upstream water level = P + H = 0.80 + 0.40 = 1.20 m above channel bed

Example 2: Rectangular Contracted Weir

Problem: Calculate discharge for a contracted weir accounting for end contractions.

📝 Given Data

  • Weir length (L) = 1.8 m
  • Head over crest (H) = 0.35 m
  • Number of contractions (n) = 2 (both ends)

📐 Formula

Q = 1.84 × (L – 0.1 × n × H) × H1.5

🔍 Step-by-Step Solution

Step 1: Calculate End Contraction Reduction

Contraction reduction = 0.1 × n × H
= 0.1 × 2 × 0.35
= 0.07 m

Step 2: Calculate Effective Length

Leffective = L – (0.1 × n × H)
= 1.8 – 0.07
= 1.73 m

Step 3: Calculate H1.5

H1.5 = (0.35)1.5
= 0.35 × √(0.35)
= 0.35 × 0.5916
= 0.2070

Step 4: Apply the Formula

Q = 1.84 × Leff × H1.5
Q = 1.84 × 1.73 × 0.2070
Q = 3.1832 × 0.2070

Step 5: Final Answer

Q = 0.659 m³/s = 659 L/s

💡 Key Insight

End contractions reduced effective length by 7 cm (4%), demonstrating why contracted weirs have slightly lower discharge than suppressed weirs of the same physical length.

Example 3: 90° V-Notch Weir

Problem: Determine discharge through a triangular V-notch weir using the Thomson equation.

📝 Given Data

  • Notch angle (θ) = 90°
  • Head above vertex (H) = 0.25 m
  • Discharge coefficient (Cd) = 0.585

📐 Formula

Q = (8/15) × Cd × √(2g) × tan(θ/2) × H2.5

🔍 Step-by-Step Solution

Step 1: Calculate √(2g)

√(2g) = √(2 × 9.81)
= √(19.62)
= 4.429 m/s

Step 2: Calculate tan(θ/2)

tan(θ/2) = tan(90°/2)
= tan(45°)
= 1.000

Step 3: Calculate H2.5

H2.5 = (0.25)2.5
= 0.25² × √(0.25)
= 0.0625 × 0.5
= 0.03125

Step 4: Calculate (8/15) × Cd

(8/15) × Cd = 0.5333 × 0.585
= 0.312

Step 5: Apply the Full Formula

Q = 0.312 × 4.429 × 1.000 × 0.03125
Q = 1.382 × 0.03125
Q = 0.0432

Step 6: Final Answer

Q = 0.0432 m³/s = 43.2 L/s

📊 Simplified Formula (90° V-Notch)

For 90° V-notch weirs, you can use the simplified Thomson equation:

Q = 1.38 × H2.5
Q = 1.38 × 0.03125
Q = 0.0431 m³/s ≈ 43.1 L/s

(Note: Small difference due to rounding in coefficient derivation)

💡 Key Advantage

V-notch weirs excel at low flows due to H2.5 sensitivity. A 10% change in head results in ~25% change in discharge, providing excellent measurement precision.

Example 4: Cipoletti Weir

Problem: Calculate discharge for a trapezoidal (Cipoletti) weir.

📝 Given Data

  • Crest length (L) = 2.0 m
  • Head (H) = 0.30 m
  • Side slopes: 1H:4V (14.04° from vertical)

📐 Formula

Q = 1.859 × L × H1.5

🔍 Step-by-Step Solution

Step 1: Verify Side Slope

Side slope = 1H:4V ✓
This compensates for end contractions

Step 2: Calculate H1.5

H1.5 = (0.30)1.5
= 0.30 × √(0.30)
= 0.30 × 0.5477
= 0.1643

Step 3: Apply the Formula

Q = 1.859 × L × H1.5
Q = 1.859 × 2.0 × 0.1643
Q = 3.718 × 0.1643

Step 4: Final Answer

Q = 0.611 m³/s = 611 L/s

💡 Key Advantage

The coefficient 1.859 already accounts for the 1:4 side slope compensation—no end contraction corrections needed! This makes Cipoletti weirs simpler to calculate than contracted rectangular weirs.

📏 Top Width Calculation

At head H = 0.30 m, the top width is:

Wtop = L + 2 × (H/4)
= 2.0 + 2 × (0.30/4)
= 2.0 + 0.15
= 2.15 m

Example 5: Broad-Crested Weir

Problem: Calculate discharge over a broad-crested weir used in a spillway.

📝 Given Data

  • Crest width (B) = 4.0 m (parallel to flow)
  • Crest length (L) = 3.5 m (perpendicular to flow)
  • Head (H) = 0.60 m
  • Discharge coefficient (Cd) = 0.848

📐 Formula

Q = Cd × L × √(2g) × H1.5

🔍 Step-by-Step Solution

Step 1: Verify Broad-Crested Criteria

B/H ratio = 4.0/0.60 = 6.67
✓ Passes (must be > 2.0 for broad-crested)

H/B ratio = 0.60/4.0 = 0.15
✓ Passes (should be < 0.5)

Step 2: Calculate √(2g)

√(2g) = √(2 × 9.81)
= √(19.62)
= 4.429 m/s

Step 3: Calculate H1.5

H1.5 = (0.60)1.5
= 0.60 × √(0.60)
= 0.60 × 0.7746
= 0.4648

Step 4: Apply the Formula

Q = Cd × L × √(2g) × H1.5
Q = 0.848 × 3.5 × 4.429 × 0.4648
Q = 2.968 × 4.429 × 0.4648
Q = 13.143 × 0.4648

Step 5: Final Answer

Q = 6.11 m³/s = 6,110 L/s

💡 Critical Flow Verification

On the broad crest, critical depth occurs:

yc = (2/3) × H
= (2/3) × 0.60
= 0.40 m

This ensures the weir operates in the calibrated regime.

Example 6: Parshall Flume (305 mm throat)

Problem: Calculate discharge through a standard 1-ft Parshall flume.

📝 Given Data

  • Throat width (W) = 305 mm = 0.305 m (1 ft)
  • Head at upstream gauge (Ha) = 0.15 m
  • Free-flow conditions verified (Hb/Ha < 0.70)

📐 Formula (ASTM D1941)

Q = 0.690 × Ha1.522

For 305 mm (1 ft) throat: K = 0.690, n = 1.522

🔍 Step-by-Step Solution

Step 1: Identify Throat-Specific Constants

From ASTM D1941 table:
W = 305 mm (1 ft) → K = 0.690, n = 1.522

Step 2: Calculate Ha1.522

Ha1.522 = (0.15)1.522
Using logarithms:
log(Ha1.522) = 1.522 × log(0.15)
= 1.522 × (-0.8239)
= -1.2540

Ha1.522 = 10-1.2540 = 0.0557

Alternative calculation using calculator:

Ha1.522 = 0.151.522 = 0.0557

Step 3: Apply the Formula

Q = K × Han
Q = 0.690 × 0.0557

Step 4: Final Answer

Q = 0.0384 m³/s = 38.4 L/s

✅ Submergence Check

If downstream head Hb is measured:

Submergence ratio = Hb/Ha
If < 0.70 → Free flow (use equation above) ✓
If > 0.70 → Submerged flow (correction factors needed)

📏 Gauge Location

The upstream gauge (Ha) is located at 2/3 of the converging section length from the throat. For a 1-ft flume, this is approximately 0.46 m upstream of the throat.

Example 7: Parshall Flume (152 mm throat)

Problem: Calculate discharge for a smaller 6-inch Parshall flume.

📝 Given Data

  • Throat width (W) = 152 mm = 0.152 m (6 inches)
  • Head at upstream gauge (Ha) = 0.09 m

📐 Formula (ASTM D1941)

Q = 0.381 × Ha1.58

For 152 mm (6″) throat: K = 0.381, n = 1.58

🔍 Step-by-Step Solution

Step 1: Identify Throat-Specific Constants

From ASTM D1941 table:
W = 152 mm (6″) → K = 0.381, n = 1.58

Step 2: Calculate Ha1.58

Ha1.58 = (0.09)1.58
Using logarithms:
log(Ha1.58) = 1.58 × log(0.09)
= 1.58 × (-1.0458)
= -1.6524

Ha1.58 = 10-1.6524 = 0.0223

Alternative calculation:

Ha1.58 = 0.091.58 = 0.0223

Step 3: Apply the Formula

Q = K × Han
Q = 0.381 × 0.0223

Step 4: Final Answer

Q = 0.0085 m³/s = 8.5 L/s

⚠️ Important Note

Notice that different throat widths have different K and n values. Always use the throat-specific equation! Using the wrong constants will result in significant errors (±20-40%).

📊 Flow Range Check

Recommended range for 152 mm throat: 0.0042 – 0.054 m³/s
Our Q = 0.0085 m³/s ✓ (within range)

Example 8: Venturi Flume

Problem: Calculate discharge through a custom Venturi flume with calibrated coefficient.

📝 Given Data

  • Throat width (Wt) = 0.40 m
  • Approach width (Wa) = 1.20 m
  • Measured head (H) = 0.35 m (above throat invert)
  • Discharge coefficient (Cd) = 0.95 (from calibration)

📐 Formula

Q = Cd × Wt × √(g) × H1.5

🔍 Step-by-Step Solution

Step 1: Calculate √(g)

√(g) = √(9.81)
= 3.132 m0.5/s

Step 2: Calculate H1.5

H1.5 = (0.35)1.5
= 0.35 × √(0.35)
= 0.35 × 0.5916
= 0.2071

Step 3: Calculate Cd × Wt

Cd × Wt = 0.95 × 0.40
= 0.38

Step 4: Apply the Formula

Q = Cd × Wt × √(g) × H1.5
Q = 0.38 × 3.132 × 0.2071
Q = 1.190 × 0.2071

Step 5: Final Answer

Q = 0.246 m³/s = 246 L/s

💡 Head Loss Calculation

Venturi flumes have minimal head loss compared to weirs:

Typical head loss = 10% of H
= 0.10 × 0.35
= 0.035 m = 3.5 cm

Compare to weir: ~40% of H = 14 cm
Head loss savings: 10.5 cm

🎯 Accuracy Note

The discharge coefficient Cd = 0.95 was determined by site-specific calibration. Without calibration, use Cd = 0.92-0.94 for preliminary design, then field-calibrate for ±2% accuracy.

Example 9: Comparison – Same Flow, Different Devices

Problem: Compare head requirements for Q = 0.500 m³/s using three different measurement devices.

📝 Target Discharge

  • Required flow rate: Q = 0.500 m³/s

Device A: Rectangular Suppressed Weir (L = 2.0 m)

Formula: Q = 1.84 × L × H1.5

Step 1: Rearrange for H

H1.5 = Q / (1.84 × L)
H = [Q / (1.84 × L)]2/3

Step 2: Calculate Q / (1.84 × L)

Q / (1.84 × L) = 0.500 / (1.84 × 2.0)
= 0.500 / 3.68
= 0.1359

Step 3: Apply Exponent 2/3

H = (0.1359)0.6667
= 0.275 m
Rectangular Weir: H = 0.275 m = 27.5 cm

Device B: 90° V-Notch Weir

Formula: Q = 1.38 × H2.5

Step 1: Rearrange for H

H2.5 = Q / 1.38
H = (Q / 1.38)0.4

Step 2: Calculate Q / 1.38

Q / 1.38 = 0.500 / 1.38
= 0.3623

Step 3: Apply Exponent 0.4

H = (0.3623)0.4
= 0.643 m
V-Notch Weir: H = 0.643 m = 64.3 cm

Device C: Parshall Flume (W = 610 mm / 2 ft)

Formula: Q = 1.426 × Ha1.547

Step 1: Rearrange for Ha

Ha1.547 = Q / 1.426
Ha = (Q / 1.426)1/1.547
Ha = (Q / 1.426)0.6464

Step 2: Calculate Q / 1.426

Q / 1.426 = 0.500 / 1.426
= 0.3506

Step 3: Apply Exponent 0.6464

Ha = (0.3506)0.6464
= 0.482 m
Parshall Flume: Ha = 0.482 m = 48.2 cm

📊 Comparison Summary

Device Required Head Head Loss Best For
Rectangular Weir 27.5 cm (lowest) ~11 cm (40%) Clean water, low head available
V-Notch Weir 64.3 cm (highest) ~26 cm (40%) Low flows, not ideal here
Parshall Flume 48.2 cm (moderate) ~5 cm (10%) Debris-laden, minimal head loss

💡 Decision Analysis

  • Rectangular Weir: Requires least head (27.5 cm) but high head loss; sediment risk
  • V-Notch: Oversized for this flow—designed for low flows; impractical here
  • Parshall Flume: Best choice—moderate head requirement, minimal head loss (5 cm vs 11-26 cm), self-cleaning

✅ Recommendation

For Q = 0.500 m³/s: Choose Parshall Flume (610 mm throat)

Rationale: Only 5 cm head loss (vs. 11+ cm for weirs), handles sediment well, moderate installation cost, excellent accuracy over wide flow range.

5. Device Comparison Guide

Selecting the appropriate flow measurement device depends on multiple factors including flow characteristics, accuracy requirements, maintenance considerations, and budget constraints.

Criterion Rectangular Suppressed Rectangular Contracted V-Notch Cipoletti
Best Application Medium flows, full-width channels Narrow channels, flexible installation Low flows, high precision Irrigation, simplified design
Head Loss High (30-50% of head) High (35-55% of head) High (40-60% of head) High (30-50% of head)
Sediment Tolerance Poor – Sediment ponds Poor – Sediment ponds Very Poor – V traps debris Poor – Sediment ponds
Accuracy Range ±2% to 5% ±3% to 5% ±2% to 3% ±3% to 5%
Installation Cost Low Low Very Low Low
Maintenance Moderate – Regular cleaning Moderate – Regular cleaning High – Frequent debris removal Moderate – Regular cleaning
Flow Range Moderate (8:1 ratio) Moderate (10:1 ratio) Wide (25:1 ratio) Moderate (8:1 ratio)
Regulatory Acceptance Very High (ISO 1438) High (ISO 1438) Very High (ISO 4360) Moderate (Regional standards)
Discharge Formula Q = 1.84·L·H1.5 Q = 1.84·(L-0.1nH)·H1.5 Q = 1.38·H2.5 (90°) Q = 1.859·L·H1.5
Criterion Broad-Crested Weir Parshall Flume Venturi Flume
Best Application High flows, dam spillways Wastewater, debris-laden flows Clean water, industrial flows
Head Loss Moderate (15-25% of head) Low (10-15% of head) Low (8-12% of head)
Sediment Tolerance Good – Wide crest area Excellent – Self-scouring Good – Smooth transitions
Accuracy Range ±3% to 5% ±3% to 5% ±2% to 4%
Installation Cost Moderate High Very High
Maintenance Low – Periodic inspection Very Low – Minimal cleaning Low – Minimal cleaning
Flow Range Moderate (12:1 ratio) Very Wide (20:1 ratio) Wide (15:1 ratio)
Regulatory Acceptance High (ISO 3846) Very High (ASTM D1941) High (ISO 4359)
Discharge Formula Q = Cd·L·√(2g)·H1.5 Q = K·Han Q = Cd·Wt·√(g)·H1.5

Device Selection Guide

Choose Rectangular Suppressed Weir when:

  • Channel width matches desired weir width
  • Medium flows (0.05 to 2 m³/s)
  • Clean water with minimal sediment
  • Simple, cost-effective installation required

Choose Rectangular Contracted Weir when:

  • Weir must be narrower than channel
  • Flexible installation positioning needed
  • End contractions are acceptable
  • Budget constraints favor simple designs

Choose V-Notch Weir when:

  • Low flows require high accuracy (0.001 to 0.5 m³/s)
  • Wide flow range expected (25:1 ratio)
  • Flow is clean with no debris
  • Seepage or laboratory measurement applications

Choose Cipoletti Weir when:

  • End contraction corrections should be avoided
  • Irrigation water rights enforcement
  • Simple field calibration preferred
  • Regional standards specify trapezoidal weirs

Choose Broad-Crested Weir when:

  • High flows in dam spillways or large channels
  • Moderate head loss acceptable
  • Structural stability is primary concern
  • Long service life with minimal maintenance

Choose Parshall Flume when:

  • Wastewater or sediment-laden flows
  • Head loss must be minimized
  • Self-cleaning action required
  • Wide flow range (20:1 ratio)
  • ASTM D1941 compliance required

Choose Venturi Flume when:

  • Minimal head loss critical (8-12%)
  • Clean industrial or municipal flows
  • High accuracy needed (±2-4%)
  • Budget allows for premium installation

6. Real-World Applications

Wastewater Treatment Plants (WWTP)

Parshall flumes are the industry standard for influent and effluent measurement. Their self-cleaning properties prevent clogging from suspended solids, and the low head loss preserves hydraulic grade line elevation throughout the treatment train. OpenFlow Measure helps verify NPDES permit compliance by ensuring reported flows match installed device capacity.

Stormwater Management

V-notch weirs are commonly installed in detention/retention pond outlets to:

  • Control peak discharge to downstream systems
  • Meet municipal stormwater ordinances (e.g., 100-year storm attenuation)
  • Generate stage-storage-discharge curves for pond design

The high sensitivity of V-notch geometry allows precise measurement of both low baseflow and high storm events.

Agricultural Irrigation

Rectangular and Cipoletti weirs enforce water rights allocations in distribution canals. OpenFlow Measure assists irrigation districts in:

  • Calibrating turnout structures for equitable distribution
  • Auditing historical flow records
  • Designing proportional dividers

Industrial Discharge Monitoring

Environmental regulations (e.g., EPA 40 CFR Part 122) often require continuous flow monitoring for industrial effluent. Engineers use OpenFlow Measure to:

  • Size primary devices for permit-required accuracy (±10%)
  • Validate existing installations against hydraulic theory
  • Troubleshoot measurement discrepancies during regulatory audits

Hydropower & Dam Operations

Spillway rating curves, powerhouse discharge calculations, and environmental flow releases all require accurate flow measurement. OpenFlow Measure supports:

  • Calibration of existing gauge-discharge relationships
  • Design of new measurement sections for license compliance
  • Verification of turbine efficiency curves

Mining & Dewatering Operations

Continuous pit dewatering and tailings management require robust flow measurement systems. Flumes are preferred due to:

  • Resistance to erosive flows
  • Handling of high sediment loads
  • Minimal maintenance in remote locations

7. Frequently Asked Questions

Q: Why must I define the channel before sizing the measurement device?

A weir or flume is an obstruction placed within an existing channel. If the device creates a water surface elevation exceeding the channel bank height, overflow will occur. OpenFlow Measure links Module 1 (channel analysis) and Module 2 (device design) to prevent this hydraulic failure mode by checking compatibility automatically.

Q: What’s the difference between suppressed and contracted weirs?

A suppressed weir spans the full channel width with no side contractions—the crest length equals channel width. A contracted weir is narrower than the channel, causing lateral flow convergence. This contraction reduces effective discharge area and requires correction factors (e.g., Francis formula includes end contraction coefficients).

Q: Can OpenFlow Measure handle pipe flow calculations?

The primary focus is open channel (free-surface) flow. However, the Pipe module does support full-pipe pressure flow analysis using the Darcy-Weisbach equation. For partially-filled pipes flowing by gravity, use the Open Channel module with circular geometry.

Q: How do I export cross-section diagrams and rating curves?

Click the Download icon (bottom-right of visualization panel) to export high-resolution PNG images. Rating curves can be exported as CSV tables via the “Export Data” button in the results panel.

Q: What does the submergence warning mean?

Weirs require free-falling nappe (jet) conditions to maintain calibrated accuracy. When downstream water level rises and “drowns” the weir crest, the flow transitions to submerged conditions. Standard discharge equations no longer apply, and correction factors (or different measurement approaches) are required. The software alerts you when tailwater elevation approaches critical submergence thresholds.

Q: How accurate is Manning’s equation for natural channels?

Manning’s equation is semi-empirical and highly sensitive to the roughness coefficient (n). For natural channels with vegetation, irregular cross-sections, and variable bed material, accuracy typically ranges from ±15% to ±25%. For engineered channels with uniform geometry and lining, accuracy improves to ±5% to ±10%. Always field-calibrate when possible.

Q: What is the minimum head requirement for weirs?

Sharp-crested weirs require minimum head typically in the range of 0.05-0.10 m (2-4 inches) to ensure nappe ventilation and avoid surface tension effects. Below this threshold, accuracy degrades significantly. The software displays minimum recommended head values in the device limitations panel.

Q: Can I use this software for tidal or backwater-affected flows?

No. OpenFlow Measure assumes uniform, steady flow conditions. Tidal influence, backwater curves, and gradually varied flow require unsteady flow models or step-backwater calculations (e.g., HEC-RAS). Use this tool only for reaches where normal depth conditions apply.

Q: Why does changing the channel slope dramatically affect device performance?

Channel slope controls the approach velocity and flow depth. Steep slopes create supercritical approach flow, which can cause hydraulic jumps at the device. Mild slopes produce subcritical flow with higher upstream water levels. OpenFlow Measure recalculates the entire hydraulic profile when slope changes to ensure the device operates within its calibrated range.

Q: Is professional review required for designs generated by this software?

Yes. OpenFlow Measure is an engineering aid, not a replacement for professional judgment. All designs should be reviewed and stamped by a licensed Professional Engineer (PE) or appropriate regulatory authority. Site-specific conditions (seepage, frost heave, seismic loads) are not modeled and require separate analysis.

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