Magnetic Drive Pump Containment Shell Design - Materials and Efficiency
Complete guide to magnetic drive pump containment shell design including material selection, thickness optimization, eddy current losses, and pressure rating for Equipment Engineers.
API 685ASME Section VIII
Containment Shell Function
The containment shell (also called containment can or rear casing) is the critical hermetic barrier in magnetic drive pumps.
Primary Functions
| Function | Description |
|---|
| Hermetic sealing | Complete barrier between process fluid and atmosphere |
| Pressure containment | Withstand full system pressure + surge |
| Magnetic flux transmission | Allow magnetic coupling through the barrier |
| Corrosion resistance | Resist chemical attack from process fluid |
| Structural integrity | Support internal bearings and inner magnet |
Design Requirements (per API 685)
| Requirement | Specification |
|---|
| Design pressure | ≥ Maximum allowable working pressure |
| Burst pressure | ≥ 4× design pressure (typical) |
| Material | Hastelloy C-4 or equivalent (API 685 default) |
| Secondary containment | Required per API 685 Section 9.1 |
Material Options
| Material | Electrical Resistivity | Eddy Loss | Max Temp | Max Pressure | Best For |
|---|
| 316 SS | Low | High (10-15%) | 400°C | >100 bar | Budget applications |
| Hastelloy C-276 | Medium | High (8-12%) | 450°C | >100 bar | Corrosive service |
| Hastelloy C-4 | Medium | High (8-12%) | 450°C | >100 bar | API 685 default |
| Titanium Gr 2 | High | Medium (4-6%) | 315°C | >100 bar | Balanced efficiency |
| Alloy 20 | Medium | High (8-12%) | 300°C | >60 bar | Sulfuric acid |
| Material | Electrical Resistivity | Eddy Loss | Max Temp | Max Pressure | Best For |
|---|
| PEEK | Insulator | Zero | 120°C | 16 bar | Maximum efficiency |
| PTFE-lined | Insulator | Zero | 150°C | 16 bar | Chemical resistance |
| Ceramic (SiC) | Insulator | Zero | 250°C | 25 bar | High temp + efficiency |
| Carbon/Graphite | Semi-conductor | Very low | 200°C | 20 bar | Good balance |
Eddy Current Losses
What Are Eddy Currents?
When the outer magnet rotates, it creates a rotating magnetic field that passes through the containment shell. In electrically conductive materials, this changing magnetic field induces circulating electric currents (eddy currents) that:
- Generate heat (I²R losses)
- Consume shaft power
- Create opposing magnetic field (reduces coupling efficiency)
P_eddy ∝ (B² × f² × t² × σ) / ρ
Where:
B = Magnetic field strength
f = Rotational frequency (speed)
t = Shell thickness
σ = Electrical conductivity
ρ = Material resistivity
Eddy Loss by Material
| Shell Material | Typical Eddy Loss | At 3000 RPM | Notes |
|---|
| 316 Stainless Steel | 10-15% | 12% typical | Highest loss |
| Hastelloy C-276 | 8-12% | 10% typical | API 685 standard |
| Titanium | 4-6% | 5% typical | ~50% of SS loss |
| PEEK | 0% | 0% | Non-conductive |
| Ceramic | 0% | 0% | Non-conductive |
Temperature Rise from Eddy Losses
| Pump Size | Eddy Loss (kW) | Temp Rise at Min Flow |
|---|
| 5 kW motor | 0.5-0.75 | 10-20°C |
| 15 kW motor | 1.5-2.25 | 15-25°C |
| 50 kW motor | 5-7.5 | 20-35°C |
| 100 kW motor | 10-15 | 25-40°C |
This temperature rise must be added to process temperature when selecting magnet grade.
Shell Thickness Design
| Thinner Shell | Thicker Shell |
|---|
| ✅ Lower eddy losses | ❌ Higher eddy losses |
| ✅ Better magnetic coupling | ❌ Weaker magnetic coupling |
| ❌ Lower pressure rating | ✅ Higher pressure rating |
| ❌ Lower burst strength | ✅ Higher burst strength |
Typical Shell Thickness
| Material | Low Pressure (<25 bar) | Medium (25-60 bar) | High (>60 bar) |
|---|
| Hastelloy | 1.5-2.0 mm | 2.0-3.0 mm | 3.0-5.0 mm |
| Titanium | 1.5-2.5 mm | 2.5-3.5 mm | 3.5-6.0 mm |
| PEEK | 3.0-5.0 mm | 5.0-8.0 mm | Not recommended |
| Ceramic | 3.0-6.0 mm | 6.0-10 mm | Limited |
Thickness Calculation Factors
Shell Thickness = f(Design Pressure, Temperature, Material Strength, Safety Factor)
Per ASME Section VIII:
t = (P × R) / (S × E - 0.6P)
Where:
t = minimum thickness
P = design pressure
R = inside radius
S = allowable stress at temperature
E = joint efficiency (1.0 for seamless)
Secondary Containment (API 685)
API 685 Section 9.1 Requirement
“A secondary containment shall be provided…”
| Component | Function |
|---|
| Primary shell | Main hermetic barrier |
| Secondary containment | Backup containment if primary fails |
| Leak detection | Alert operator of primary failure |
Secondary Containment Options
| Type | Description | Detection Method |
|---|
| Metal backing plate | Thick plate behind shell | Pressure switch in cavity |
| Double-wall shell | Two shells with monitored space | Pressure or leak detector |
| Drip collection | Contained area for any leakage | Visual or liquid sensor |
Shell Design Configurations
Standard Designs
| Configuration | Description | Application |
|---|
| Cylindrical | Simple cylinder | Most common |
| Domed | Hemispherical end | High pressure |
| Flat-backed | Flat rear face | Easy manufacturing |
| Profiled | Optimized for flux | Premium efficiency |
Shell Mounting Methods
| Method | Advantage | Disadvantage |
|---|
| Bolted flange | Easy replacement | More leak paths |
| Welded | Maximum integrity | Difficult replacement |
| Press-fit | Compact | Limited to low pressure |
| Threaded | Easy service | Requires sealing |
Efficiency Optimization
Strategies to Minimize Eddy Losses
| Strategy | Effectiveness | Trade-off |
|---|
| Non-metallic shell | Eliminates 100% | Lower P/T rating |
| Titanium instead of SS | Reduces 50% | Higher cost |
| Thinner shell | Proportional to t² | Lower pressure rating |
| Lower speed | Proportional to f² | May need larger pump |
| Laminated shell | Reduces 30-50% | Complex, expensive |
When Efficiency Matters Most
| Application | Efficiency Priority | Recommended Shell |
|---|
| Continuous operation | Very High | PEEK or Ceramic |
| Large motors (>50 kW) | High | Titanium |
| High energy cost areas | High | Non-metallic |
| Intermittent operation | Medium | Hastelloy acceptable |
| Small pumps (<5 kW) | Low | Any suitable material |
Energy Cost Impact Example
Motor: 50 kW
Operating hours: 8,000 hr/year
Energy cost: $0.10/kWh
Shell Option A (Hastelloy): 10% eddy loss = 5 kW loss
Annual cost: 5 × 8,000 × $0.10 = $4,000/year
Shell Option B (Titanium): 5% eddy loss = 2.5 kW loss
Annual cost: 2.5 × 8,000 × $0.10 = $2,000/year
Savings: $2,000/year → Payback titanium premium in 2-3 years
Pressure Rating
Design Pressure Determination
| Factor | Consideration |
|---|
| Maximum operating pressure | Normal process conditions |
| Surge pressure | Valve closure, pump trips |
| Hydrostatic test | 1.5× design pressure |
| Safety factor | Typically 4× for burst |
Pressure Rating by Material
| Material | Typical Max Design Pressure |
|---|
| Hastelloy C-276 (3mm) | 100+ bar |
| Titanium (3mm) | 80+ bar |
| PEEK (6mm) | 16 bar |
| Ceramic (6mm) | 25 bar |
Corrosion Considerations
Material Selection for Corrosive Service
| Process Fluid | Recommended Shell | Alternative |
|---|
| HCl acid | Hastelloy C-276 | Titanium |
| H₂SO₄ acid | Alloy 20 | Hastelloy |
| HF acid | Monel | Hastelloy |
| Caustic (NaOH) | 316 SS | Hastelloy |
| Seawater | Titanium | Hastelloy |
| Organic solvents | 316 SS | PEEK |
| Clean water | PEEK | 316 SS |
Corrosion Allowance
| Service | Typical Allowance |
|---|
| Mild corrosion | 1.5 mm |
| Moderate corrosion | 3.0 mm |
| Severe corrosion | 6.0 mm or upgrade material |
=== CONTAINMENT SHELL SPECIFICATION ===
Design Conditions:
- Design Pressure: ___ barg at ___°C
- Design Temperature: ___°C
- Test Pressure: ___ barg (1.5× design)
Shell Construction:
- Material: _________ (Grade: ___)
- Type: Metallic / Non-metallic
- Nominal Thickness: ___ mm
- Minimum Thickness: ___ mm
Performance:
- Estimated Eddy Losses: ___ kW (___ % of shaft power)
- Temperature Rise at Min Flow: ___°C
Secondary Containment:
- Type: _______________
- Detection Method: _______________
Certification:
- ASME Section VIII: □ Required
- PED (European): □ Required
- Other: _______________
Vendor Data Requirements
Request from Vendor
| Data Point | Purpose |
|---|
| Shell material certificate | Verify grade and composition |
| Thickness calculation | Confirm pressure rating |
| Eddy current loss | For motor sizing and efficiency |
| Temperature rise data | For magnet selection |
| Burst test results | Safety verification |
| NDT reports | Quality assurance |
Review Checklist
□ Shell material matches specification
□ Thickness adequate for design pressure
□ Eddy losses included in motor sizing
□ Temperature rise added to magnet selection
□ Secondary containment per API 685
□ Leak detection provision included
□ Material test reports available
□ Weld procedures qualified (if welded)
Summary: Shell Selection Guide
| Factor | Metallic (Hastelloy) | Non-Metallic (PEEK/Ceramic) |
|---|
| Max Pressure | >100 bar | 16-25 bar |
| Max Temperature | 450°C | 120-250°C |
| Eddy Losses | 8-12% | 0% |
| Corrosion Resistance | Excellent | Good-Excellent |
| Cost | Higher | Lower |
| Best Application | High P/T, corrosive | Efficiency-critical |