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

FunctionDescription
Hermetic sealingComplete barrier between process fluid and atmosphere
Pressure containmentWithstand full system pressure + surge
Magnetic flux transmissionAllow magnetic coupling through the barrier
Corrosion resistanceResist chemical attack from process fluid
Structural integritySupport internal bearings and inner magnet

Design Requirements (per API 685)

RequirementSpecification
Design pressure≥ Maximum allowable working pressure
Burst pressure≥ 4× design pressure (typical)
MaterialHastelloy C-4 or equivalent (API 685 default)
Secondary containmentRequired per API 685 Section 9.1

Material Options

Metallic Shells

MaterialElectrical ResistivityEddy LossMax TempMax PressureBest For
316 SSLowHigh (10-15%)400°C>100 barBudget applications
Hastelloy C-276MediumHigh (8-12%)450°C>100 barCorrosive service
Hastelloy C-4MediumHigh (8-12%)450°C>100 barAPI 685 default
Titanium Gr 2HighMedium (4-6%)315°C>100 barBalanced efficiency
Alloy 20MediumHigh (8-12%)300°C>60 barSulfuric acid

Non-Metallic Shells

MaterialElectrical ResistivityEddy LossMax TempMax PressureBest For
PEEKInsulatorZero120°C16 barMaximum efficiency
PTFE-linedInsulatorZero150°C16 barChemical resistance
Ceramic (SiC)InsulatorZero250°C25 barHigh temp + efficiency
Carbon/GraphiteSemi-conductorVery low200°C20 barGood 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:

  1. Generate heat (I²R losses)
  2. Consume shaft power
  3. Create opposing magnetic field (reduces coupling efficiency)

Eddy Loss Formula

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 MaterialTypical Eddy LossAt 3000 RPMNotes
316 Stainless Steel10-15%12% typicalHighest loss
Hastelloy C-2768-12%10% typicalAPI 685 standard
Titanium4-6%5% typical~50% of SS loss
PEEK0%0%Non-conductive
Ceramic0%0%Non-conductive

Temperature Rise from Eddy Losses

Pump SizeEddy Loss (kW)Temp Rise at Min Flow
5 kW motor0.5-0.7510-20°C
15 kW motor1.5-2.2515-25°C
50 kW motor5-7.520-35°C
100 kW motor10-1525-40°C

This temperature rise must be added to process temperature when selecting magnet grade.

Shell Thickness Design

Thickness vs Performance Trade-off

Thinner ShellThicker 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

MaterialLow Pressure (<25 bar)Medium (25-60 bar)High (>60 bar)
Hastelloy1.5-2.0 mm2.0-3.0 mm3.0-5.0 mm
Titanium1.5-2.5 mm2.5-3.5 mm3.5-6.0 mm
PEEK3.0-5.0 mm5.0-8.0 mmNot recommended
Ceramic3.0-6.0 mm6.0-10 mmLimited

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…”

ComponentFunction
Primary shellMain hermetic barrier
Secondary containmentBackup containment if primary fails
Leak detectionAlert operator of primary failure

Secondary Containment Options

TypeDescriptionDetection Method
Metal backing plateThick plate behind shellPressure switch in cavity
Double-wall shellTwo shells with monitored spacePressure or leak detector
Drip collectionContained area for any leakageVisual or liquid sensor

Shell Design Configurations

Standard Designs

ConfigurationDescriptionApplication
CylindricalSimple cylinderMost common
DomedHemispherical endHigh pressure
Flat-backedFlat rear faceEasy manufacturing
ProfiledOptimized for fluxPremium efficiency

Shell Mounting Methods

MethodAdvantageDisadvantage
Bolted flangeEasy replacementMore leak paths
WeldedMaximum integrityDifficult replacement
Press-fitCompactLimited to low pressure
ThreadedEasy serviceRequires sealing

Efficiency Optimization

Strategies to Minimize Eddy Losses

StrategyEffectivenessTrade-off
Non-metallic shellEliminates 100%Lower P/T rating
Titanium instead of SSReduces 50%Higher cost
Thinner shellProportional to t²Lower pressure rating
Lower speedProportional to f²May need larger pump
Laminated shellReduces 30-50%Complex, expensive

When Efficiency Matters Most

ApplicationEfficiency PriorityRecommended Shell
Continuous operationVery HighPEEK or Ceramic
Large motors (>50 kW)HighTitanium
High energy cost areasHighNon-metallic
Intermittent operationMediumHastelloy acceptable
Small pumps (<5 kW)LowAny 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

FactorConsideration
Maximum operating pressureNormal process conditions
Surge pressureValve closure, pump trips
Hydrostatic test1.5× design pressure
Safety factorTypically 4× for burst

Pressure Rating by Material

MaterialTypical 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 FluidRecommended ShellAlternative
HCl acidHastelloy C-276Titanium
H₂SO₄ acidAlloy 20Hastelloy
HF acidMonelHastelloy
Caustic (NaOH)316 SSHastelloy
SeawaterTitaniumHastelloy
Organic solvents316 SSPEEK
Clean waterPEEK316 SS

Corrosion Allowance

ServiceTypical Allowance
Mild corrosion1.5 mm
Moderate corrosion3.0 mm
Severe corrosion6.0 mm or upgrade material

Specification Format

=== 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 PointPurpose
Shell material certificateVerify grade and composition
Thickness calculationConfirm pressure rating
Eddy current lossFor motor sizing and efficiency
Temperature rise dataFor magnet selection
Burst test resultsSafety verification
NDT reportsQuality 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

FactorMetallic (Hastelloy)Non-Metallic (PEEK/Ceramic)
Max Pressure>100 bar16-25 bar
Max Temperature450°C120-250°C
Eddy Losses8-12%0%
Corrosion ResistanceExcellentGood-Excellent
CostHigherLower
Best ApplicationHigh P/T, corrosiveEfficiency-critical

Frequently Asked Questions

What is the function of containment shell in mag-drive pump?
The containment shell provides hermetic separation between the process fluid and atmosphere. It allows magnetic flux to pass through while containing the pressurized fluid, enabling sealless pump operation with zero leakage.
Why does metallic shell cause efficiency loss?
Rotating magnetic field induces eddy currents in electrically conductive (metallic) shells. These currents generate heat, consuming 3-15% of shaft power depending on material conductivity, shell thickness, and rotational speed.
When should I use non-metallic shell?
Use non-metallic shells (PEEK, ceramic) when efficiency is critical, temperature is below 120-250°C, and pressure is moderate (<16-25 bar). They eliminate eddy current losses completely but have lower pressure/temperature ratings.

📚 References & Sources

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