AODD Pump Selection Guide - Sizing and Application
Complete selection guide for Air Operated Double Diaphragm pumps including sizing methodology, flow calculation, air consumption, and application matching for Equipment Engineers.
ANSI/HI 10.1-10.5
Selection Process Overview
Step-by-Step Selection
1. Define process requirements
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2. Calculate hydraulic requirements
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3. Check suction conditions
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4. Select pump size
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5. Choose materials of construction
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6. Verify air supply capacity
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7. Consider accessories needed
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8. Final verification
Step 1: Process Requirements
| Parameter | Required | Units |
|---|
| Flow rate | Yes | LPM or GPM |
| Discharge pressure | Yes | bar or psi |
| Suction lift | Yes | m or ft |
| Fluid properties | Yes | See below |
| Temperature | Yes | °C |
| Solids content | If applicable | % or size |
Fluid Properties Checklist
□ Fluid name/composition
□ Specific gravity
□ Viscosity (at operating temperature)
□ Vapor pressure
□ Solids content (% and particle size)
□ Abrasiveness
□ Chemical composition
□ Temperature range (min/normal/max)
Step 2: Hydraulic Calculations
Total Dynamic Head (TDH)
TDH = Hstatic + Hfriction + Hpressure
Where:
Hstatic = Static head difference (discharge - suction elevation)
Hfriction = Pipe friction losses
Hpressure = Vessel pressure difference
Flow Rate with Safety Factor
Design Flow = Required Flow × 1.2
Example:
Required: 100 LPM
Design: 100 × 1.2 = 120 LPM
Pressure Calculation
Discharge Pressure Required = TDH × SG × 0.0981 (bar)
Or: Discharge Pressure = TDH × SG × 0.433 (psi)
Example:
TDH = 30 m, SG = 1.2
Pressure = 30 × 1.2 × 0.0981 = 3.53 bar
Step 3: Suction Conditions
NPSHa Calculation
NPSHa = (Patm - Pvapor)/(ρ×g) + Hstatic(suction) - Hfriction(suction)
Suction Lift Verification
| Condition | Max Suction Lift |
|---|
| Water at 20°C | 6 m (20 ft) |
| Viscous fluid (>100 cP) | 3-4.5 m (10-15 ft) |
| High temperature fluid | Reduced (check vapor pressure) |
| At altitude | Reduce 1.2 m per 1000 m |
Suction Design Rules
✓ Keep suction lift as low as possible
✓ Use flooded suction when available
✓ Minimize suction line length
✓ Suction pipe ≥ pump inlet size
✓ Avoid air pockets in suction line
Step 4: Pump Size Selection
Flow Range by Port Size
| Port Size | Flow Range (LPM) | Flow Range (GPM) | Typical Application |
|---|
| 1/4” | 15-30 | 4-8 | Sampling, dosing |
| 3/8” | 30-60 | 8-16 | Small transfer |
| 1/2” | 60-115 | 16-30 | Light duty |
| 3/4” | 115-190 | 30-50 | Medium duty |
| 1” | 190-380 | 50-100 | General purpose |
| 1-1/2” | 380-570 | 100-150 | Heavy duty |
| 2” | 570-870 | 150-230 | Industrial |
| 3” | 870-1135 | 230-300 | High volume |
Optimal Operating Point
Optimal Point = 60-80% of maximum capacity
Why?
- At max capacity: High wear, short life
- Below 50%: Inefficient air consumption
- 60-80%: Best balance of life and performance
Selection Example
Requirements:
- Flow: 100 GPM
- Pressure: 50 psi
Option 1: 1" pump (max 100 GPM)
- Operating at 100% = Too high ❌
Option 2: 1-1/2" pump (max 150 GPM)
- Operating at 67% = Good ✓
Option 3: 2" pump (max 230 GPM)
- Operating at 43% = OK but inefficient
Best choice: 1-1/2" pump ✓
Step 5: Material Selection
Material Selection Matrix
| Fluid Type | Housing | Diaphragm | Ball/Seat |
|---|
| Water | PP, SS | EPDM, Santoprene | EPDM |
| Acids | PVDF, PP | PTFE | PTFE |
| Caustics | PP, SS | EPDM, PTFE | EPDM, PTFE |
| Solvents | PVDF, SS | PTFE | PTFE |
| Petroleum | Aluminum, SS | Buna-N, Viton | Buna-N |
| Food/Pharma | 316 SS | FDA PTFE | FDA PTFE |
| Abrasive | SS, PVDF | Santoprene | SS |
Quick Material Reference
Housing Materials:
| Material | Best For | Avoid |
|---|
| Polypropylene | Acids, chemicals | High temp (>80°C) |
| PVDF | Aggressive chemicals | Very high pressure |
| Aluminum | General, petroleum | Acids, caustics |
| 316 SS | Food, high purity | Chlorides |
| Cast Iron | Water, general | Corrosives |
Diaphragm Materials:
| Material | Best For | Temp Range |
|---|
| Santoprene | General, abrasives | -40 to 100°C |
| EPDM | Water, acids, alcohols | -50 to 120°C |
| Buna-N | Petroleum, oils | -40 to 80°C |
| PTFE | Aggressive chemicals | -10 to 100°C |
| Viton | High temp, solvents | -20 to 200°C |
Step 6: Air Supply Verification
Air Consumption Estimation
Quick Estimate:
SCFM ≈ GPM × 1.5 to 2.0 (at moderate pressures)
Typical Air Consumption by Size:
| Pump Size | Flow @ 50 psi | Air Consumption |
|---|
| 1/2” | 10 GPM | 12-15 SCFM |
| 1” | 50 GPM | 35-45 SCFM |
| 1-1/2” | 100 GPM | 60-80 SCFM |
| 2” | 150 GPM | 90-120 SCFM |
| 3” | 250 GPM | 150-200 SCFM |
Air Supply Checklist
□ Available air pressure: ___ psi (need 10-20 psi above discharge)
□ Available air volume: ___ SCFM
□ Air quality (filtration, drying)
□ Distance from compressor
□ Pipe size adequate
Air Supply Requirements
| Parameter | Requirement |
|---|
| Pressure | 10-20 psi above required discharge |
| Volume | SCFM from curves + 10-20% margin |
| Quality | Class 4 per ISO 8573-1 |
| Temperature | Ambient to 80°C max |
Step 7: Accessories
Common Accessories
| Accessory | When Needed | Purpose |
|---|
| Pulsation dampener | Sensitive instrumentation | Reduce flow pulsation |
| Suction strainer | Solids in fluid | Protect pump |
| Y-strainer | Air line | Protect air valve |
| FRL unit | All installations | Filter, regulate, lubricate |
| Muffler | Noise sensitive areas | Reduce exhaust noise |
| Flow meter | Process control | Monitor flow rate |
Pulsation Dampener Sizing
Dampener Volume ≥ 10 × Stroke Volume (for 90% reduction)
Example:
Stroke volume = 500 mL
Dampener volume = 500 × 10 = 5,000 mL = 5 L
Step 8: Final Verification
Selection Checklist
Performance:
□ Flow rate within 60-80% of max
□ Pressure within rating
□ Suction conditions acceptable
□ Air supply adequate
Materials:
□ Housing compatible with fluid
□ Diaphragm compatible with fluid
□ Elastomers compatible with fluid
□ Temperature rating adequate
System:
□ Pipe sizes match pump ports
□ Pulsation dampener sized (if needed)
□ Air supply piped correctly
□ Accessories specified
Decision Tree
When to Choose AODD
START
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Need pump for transfer application?
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├── YES: Continue
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Hazardous area (ATEX required)?
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├── YES → AODD (inherently safe) ✓
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▼
Self-priming required?
│
├── YES → AODD excellent choice ✓
│
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May run dry?
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├── YES → AODD (safe) ✓
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Continuous precise flow needed?
│
├── YES → Consider centrifugal or progressive cavity
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Shear sensitive fluid?
│
├── YES → AODD good choice ✓
│
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High flow (>300 GPM)?
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├── YES → Consider other pump types
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AODD is suitable choice ✓
AODD vs Other Pumps Quick Guide
| Application | Best Choice |
|---|
| Chemical transfer | AODD |
| Hazardous area | AODD |
| Tank emptying | AODD |
| Drum unloading | AODD |
| High viscosity (>5000 cP) | Progressive cavity |
| High flow continuous | Centrifugal |
| Accurate metering | Peristaltic |
| Abrasive slurries | AODD or Peristaltic |
Viscosity Correction
Flow Correction Factors
| Viscosity (cP) | Flow Factor | Pressure Factor |
|---|
| < 100 | 1.0 | 1.0 |
| 100-500 | 0.9 | 1.0 |
| 500-1000 | 0.8 | 0.95 |
| 1000-5000 | 0.65 | 0.9 |
| > 5000 | 0.5 | 0.85 |
Viscosity Selection Adjustment
Corrected Flow = Catalog Flow × Viscosity Factor
Example:
Catalog flow at duty point: 100 GPM
Fluid viscosity: 2000 cP
Factor: 0.65
Actual flow: 100 × 0.65 = 65 GPM
Action: Select larger pump to compensate
Sizing Worksheet
=== AODD PUMP SIZING WORKSHEET ===
1. PROCESS REQUIREMENTS
Required flow: ___ LPM (___ GPM)
Design flow (+20%): ___ LPM
Discharge pressure: ___ bar (___ psi)
Suction lift: ___ m (___ ft)
Fluid: _______________
Temperature: ___ °C
Viscosity: ___ cP
Specific gravity: ___
Solids: ___ % / ___ mm size
2. PUMP SELECTION
Selected pump size: ___ inch
Max flow at duty pressure: ___ GPM
Operating percentage: ___ % (target 60-80%)
Selected model: _______________
3. MATERIALS
Housing: _______________
Diaphragm: _______________
Ball/Seat: _______________
O-rings: _______________
4. AIR SUPPLY
Required pressure: ___ psi
Required volume: ___ SCFM
Available pressure: ___ psi ✓
Available volume: ___ SCFM ✓
5. ACCESSORIES
□ Pulsation dampener: Size ___ L
□ Suction strainer: Size ___
□ FRL unit: Size ___
□ Muffler
□ Other: _______________
6. VERIFICATION
□ Flow at 60-80% capacity
□ Pressure within rating
□ Materials compatible
□ Air supply adequate
□ Accessories specified
Common Selection Mistakes
Mistakes to Avoid
| Mistake | Problem | Solution |
|---|
| Undersizing | Runs at max capacity | Size for 60-80% |
| Oversizing | Poor efficiency | Match to actual need |
| Ignoring viscosity | Flow shortfall | Apply correction factor |
| Wrong materials | Premature failure | Verify compatibility |
| Inadequate air | Poor performance | Verify SCFM available |
| No pulsation dampener | Instrument damage | Add dampener |