Jul 15,2026
Electromagnetic Pumps – MHD Principles, Lorentz Force & Liquid‑Metal Design
Engineering guide to electromagnetic pumps covering MHD physics, Lorentz force pressure generation, conduction vs induction designs, liquid‑metal materials, and high‑temperature applications.
1. Introduction: Pumping Without Moving Parts
The electromagnetic pump (EMP) represents a fundamental departure from conventional fluid handling. Where centrifugal pumps use rotating impellers and positive displacement pumps use reciprocating pistons, the electromagnetic pump has no moving parts in the fluid path. It exploits the interaction between magnetic fields and electric currents within a conductive fluid to generate pressure and flow—a phenomenon described by magnetohydrodynamics (MHD).
This technology was first conceived by Michael Faraday and later advanced by Jack Northrup in the mid-1950s for nuclear reactor cooling systems. Today, electromagnetic pumps circulate liquid sodium in fast breeder reactors, transport molten aluminum in foundries, and drive liquid metal coolants in concentrated solar power systems. The absence of bearings, seals, and shafts makes EMPs uniquely suited for fluids that destroy mechanical pumps: liquid metals at 600°C, corrosive salts, and toxic heavy metals.
2. The Physics of Electromagnetic Pumping: Lorentz Force & MHD
Formula 1: The Lorentz Force
The fundamental operating principle of every electromagnetic pump is the Lorentz force—the force exerted on a charged particle (or current-carrying conductor) moving through a magnetic field.
F = J × B
Where:
- F = Force density (N/m³)
- J = Current density (A/m²)
- B = Magnetic flux density (Tesla)
For a conducting fluid flowing through a channel of length L, width w, and height h, the developed pressure is:
ΔP = J · B · L
Where:
- ΔP = Pressure rise (Pa)
- L = Active channel length in the magnetic field (m)
The Cross-Product Geometry: The Lorentz force acts perpendicular to both the current direction and the magnetic field direction. In a typical EMP:
- Current flows across the channel (electrode to electrode)
- Magnetic field is perpendicular to the current (through the channel walls)
- Force acts along the channel axis (pumping direction)
This orthogonal relationship is the reason EMPs are often called "crossed-field" pumps.
Formula 2: Ohm's Law in Moving Conductors
When the conducting fluid moves with velocity u, it generates a back-electromotive force (back-EMF):
J = σ(E + u × B)
Where:
- σ = Electrical conductivity of the fluid (S/m)
- E = Applied electric field (V/m)
- u = Fluid velocity (m/s)
The term u×B represents the induced electric field from fluid motion. At high velocities, this back-EMF reduces the net current and thus the pumping force. This is the fundamental speed limitation of conduction pumps.
Formula 3: Pump Efficiency
The theoretical efficiency of an electromagnetic pump is:
η = Hydraulic Power / Electrical Input Power = (Q · ΔP) / (I · V)
Where:
- Q = Volumetric flow rate (m³/s)
- ΔP = Pressure rise (Pa)
- I = Total current (A)
- V = Total voltage (V)
Practical Efficiency Factors:
Actual EMP efficiency is reduced by:
- Joule heating in the fluid: PJoule = ∫ (J²/σ) dV
- Eddy current losses in channel walls and magnetic cores
- End effects (fringing fields at channel entrance/exit)
- Hydraulic losses (friction in the channel)
Typical EMP efficiencies range from 10% to 55%, significantly lower than mechanical pumps (60–85%). However, the efficiency comparison must account for the elimination of mechanical losses (bearings, seals) and the ability to handle fluids that would destroy conventional pumps.
3. Electromagnetic Pump Types: Conduction vs. Induction
Electromagnetic pumps are classified by how electric current is introduced into the fluid.
Table 1: Electromagnetic Pump Type Comparison
| Pump Type | Current Introduction | Efficiency | Max Temperature | Flow Range | Pressure Range | Best Application |
|---|---|---|---|---|---|---|
| DC Conduction Pump | Direct current via electrodes contacting fluid | 25–40% | 600°C (with cooling) | 0.1–50 m³/h | 0.1–5 bar | Laboratory loops, small sodium systems, precise flow control |
| AC Conduction Pump | Alternating current via electrodes | 15–30% | 500°C | 0.5–100 m³/h | 0.2–10 bar | Medium-scale systems, transformer-coupled power |
| Linear Induction Pump (LIP) | Induced current from traveling magnetic field | 30–50% | 600°C | 10–500 m³/h | 0.5–15 bar | Large reactor cooling, industrial metal transport |
| Annular Linear Induction Pump (ALIP) | Induced current in annular channel | 35–55% | 600°C | 25–1,000 m³/h | 1–20 bar | Nuclear reactor primary cooling, large-scale sodium systems |
| Permanent Magnet Pump (PMP) | Rotating permanent magnets induce current | 40–60% | 400°C (magnet limit) | 1–200 m³/h | 0.5–10 bar | Aluminum casting, compact systems, no external field coils |
| Thermoelectric (TE) Pump | Self-generated current from temperature gradient | 5–15% | 800°C | 0.01–5 m³/h | 0.05–1 bar | Decay heat removal, passive safety systems, no external power |
Key Distinction: Conduction pumps introduce current directly through electrodes in contact with the fluid. Induction pumps generate current electromagnetically without physical contact, using the same principle as an induction motor.
4. Detailed Pump Architecture
DC Conduction Pump
The simplest EMP design. Two electrodes are mounted on opposite sides of a rectangular channel. A magnetic field is applied perpendicular to both the current path and the channel axis.
Components:
- Channel: Non-magnetic, electrically insulating refractory metal or ceramic (stainless steel, niobium, alumina)
- Electrodes: Copper or molybdenum, brazed to channel walls
- Magnet: Permanent magnet (NdFeB, SmCo) or electromagnet
- Yoke: Soft iron or silicon steel to complete magnetic circuit
Advantages: Simple design, compact, excellent flow control fidelity, low pump mass.
Disadvantages: High-current cabling, electrode erosion, armature reaction (magnetic field distortion from current), ohmic heating losses.
Typical Specifications (Small DC Pump):
- Channel: 38.4 mm wide × 1.8 mm high × 90 mm long
- Current: 116 A at ~1 V
- Fluid: Sodium at 300°C
- Performance: 5 kPa at 0.18 m³/h, efficiency 27%
Annular Linear Induction Pump (ALIP)
The dominant design for large-scale nuclear reactor cooling. Liquid metal flows through an annular gap between two concentric tubes. A three-phase stator winding surrounds the outer tube, creating a traveling magnetic field.
Working Principle:
- Three-phase AC in the stator creates a rotating (traveling) magnetic field
- The traveling field induces circumferential currents in the liquid metal
- Interaction between induced currents and the magnetic field produces axial Lorentz force
- The force drives sodium through the annular channel
Equivalent Circuit Analogy: The ALIP is electrically similar to an induction motor, but with critical differences:
- Slip: Typical induction motor slip = 0.05; ALIP slip = 0.4–0.9
- Air gap: Much larger than induction motors due to channel walls
- Power factor: Lower than induction motors due to high slip and large air gap
Performance Specifications (CMI Novacast LA Series):
| Model | Max Flow (m³/h) | Max Temp (°C) | ΔP (bar) | Max Pressure (bar) | NPSH (bar abs) |
|---|---|---|---|---|---|
| LA125 | 4 | 600 | 1.3 | 15 | 0.7 |
| LA150 | 8 | 600 | 1.5 | 15 | 0.9 |
| LA200 | 12 | 600 | 3.0 | 15 | 0.8 |
| LA300 | 25 | 600 | 5.0 | 20 | 0.8 |
| LA400 | 50 | 600 | 5.0 | 15 | 0.8 |
| LA500 | 140 | 600 | 4.0 | 15 | 1.0 |
5. Performance Analysis: Lorentz Force & Pressure Development
Chart 1: Electromagnetic Pump Type Comparison & Lorentz Force Analysis

Left Panel — Multi-Criteria Pump Type Comparison:
This chart compares six EMP technologies across six engineering parameters:
- DC Conduction (Blue): Moderate efficiency (35/100) but excellent reliability (90/100) and control precision (85/100). The simple design with no alternating fields minimizes electromagnetic interference and flow pulsation.
- AC Conduction (Red): Lower efficiency (25/100) due to eddy current and skin effect losses, but good temperature capability (70/100). The transformer-coupled design allows better power conditioning.
- Linear Induction (Green): Good flow range (70/100) and pressure capability (60/100) with moderate efficiency (45/100). The contactless design eliminates electrode erosion.
- Annular Induction (Purple): The best all-around performer for large systems—highest flow range (80/100), excellent reliability (92/100), and good temperature capability (90/100). Efficiency (50/100) is the highest among EMP types.
- Permanent Magnet (Orange): Highest efficiency potential (55/100) with excellent control precision (90/100) and reliability (95/100). Limited by magnet temperature (75/100) to ~400°C unless actively cooled.
- Thermoelectric (Cyan): Unique self-powered operation with no external electrical input, but lowest efficiency (15/100) and flow capability (20/100). Reserved for passive safety applications.
Right Panel — Lorentz Force Pressure Development:
This chart shows how pressure develops as a function of current density for different channel lengths:
- Linear Relationship: Pressure is directly proportional to current density (ΔP=J·B·L). Doubling current density doubles pressure.
- Channel Length Effect: A 300 mm channel produces 3× the pressure of a 100 mm channel at the same current density. This is why large pumps use extended active lengths.
- Efficiency Curve (Orange): Efficiency peaks at moderate current densities (~2 MA/m²) and decreases at both low and high extremes. At low current, fixed losses dominate. At high current, Joule heating (J²/σ) becomes excessive.
Application Points:
- Small Lab Pump: J = 0.5 MA/m², ΔP = 1.5 bar (100 mm channel) — low power, precise control
- Nuclear Reactor: J = 1.5 MA/m², ΔP = 4.5 bar (200 mm channel) — moderate power, high reliability
- Industrial Scale: J = 3.0 MA/m², ΔP = 9.0 bar (200 mm channel) — high flow aluminum casting
- High-Pressure: J = 4.0 MA/m², ΔP = 12.0 bar (200 mm channel) — lithium propulsion, approaching cavitation limit
Cavitation Limit (Red dashed): At ~4 bar pressure rise, flow velocity approaches 9.14 m/s—the threshold where cavitation instabilities occur. This is the practical upper limit for most liquid metal EMPs.
6. Material Selection for Extreme Environments
Table 2: Electromagnetic Pump Material Specification
| Component | Sodium/NaK Service | Lead-Bismuth Eutectic | Aluminum/Magnesium | High-Temp Lithium |
|---|---|---|---|---|
| Channel | 316L SS, refractory metal | 316L SS, T91 | Graphite, SiC-coated steel | Niobium, molybdenum |
| Electrodes | Copper, molybdenum | Molybdenum, tungsten | Graphite | Tungsten, rhenium |
| Magnets (PMP) | NdFeB (cooled to < 80°C) | NdFeB (cooled) | SmCo (to 350°C) | SmCo (to 350°C) |
| Stator Windings (ALIP) | Copper, ceramic insulation | Copper, ceramic insulation | Copper, standard insulation | Silver, ceramic insulation |
| Yoke/Core | Silicon steel laminations | Silicon steel | Silicon steel | Cobalt-iron alloy |
| Seals/Gaskets | Metal seals, welded joints | Metal seals | Ceramic fiber | Metal seals, brazed joints |
Critical Material Considerations:
- Liquid Metal Corrosion: Sodium is relatively benign to stainless steel below 500°C. Lead-bismuth eutectic (LBE) is highly corrosive and requires oxygen control (passive oxide layer) or protective coatings.
- Magnet Temperature Limits: NdFeB permanent magnets demagnetize above 80–130°C. SmCo magnets tolerate up to 350°C. Above this, only electromagnets (cooled) or thermoelectric systems are viable.
- Electrode Erosion: In conduction pumps, electrodes experience electrochemical erosion and dissolution into the liquid metal. Molybdenum and tungsten offer the best compromise of conductivity and corrosion resistance.
- Ceramic Insulation: Channel walls must be electrically insulating to prevent current short-circuiting through the structure. Alumina (Al₂O₃) and magnesia (MgO) are standard, but thermal expansion mismatch with metals creates cracking risks.
7. Power Supply & Control Systems
Formula 4: DC Conduction Pump Power Calculation
Pinput = I² · Rtotal = I² · (L / (σ · Afluid) + Relectrodes + Rcables)
Where:
- I = Electrode current (A)
- L = Channel length (m)
- σ = Fluid conductivity (S/m)
- Afluid = Cross-sectional area of fluid (m²)
Typical Conductivities:
| Fluid | Temperature (°C) | Conductivity (S/m) | Density (kg/m³) |
|---|---|---|---|
| Sodium (Na) | 300 | 1.0 × 10⁷ | 880 |
| Sodium (Na) | 500 | 8.5 × 10⁶ | 820 |
| NaK-78 (eutectic) | 300 | 2.5 × 10⁶ | 850 |
| Lead-Bismuth (LBE) | 400 | 1.0 × 10⁶ | 10,200 |
| Mercury (Hg) | 20 | 1.0 × 10⁶ | 13,500 |
| Aluminum (Al) | 700 | 3.5 × 10⁶ | 2,400 |
| Gallium (Ga) | 30 | 3.7 × 10⁶ | 6,100 |
Formula 5: ALIP Power Calculation
The ALIP is electrically modeled as an induction motor with high slip:
Pinput = 3 · Vphase · Iphase · cos(ϕ)
Where:
- Vphase = Phase voltage (V)
- Iphase = Phase current (A)
- cos(ϕ) = Power factor (typically 0.5–0.7 for ALIPs)
Slip and Efficiency:
s = (ns - nfluid) / ns
η = Phydraulic / Pinput = (Q · ΔP) / (3 · V · I · cos(ϕ))
Where ns = synchronous speed of traveling field and nfluid = effective fluid velocity.
Typical ALIP slip: 0.4–0.9 (compared to 0.02–0.05 for standard induction motors). This high slip is the primary reason for lower efficiency.
8. Thermal Management & Magnet Cooling
Formula 6: Magnet Temperature Rise
For permanent magnet pumps, the magnet temperature must remain below its Curie point:
Tmagnet = Tambient + Pheat,leakage / (h · Acooling)
Where:
- Pheat,leakage = Heat leakage from channel to magnet (W)
- h = Convective heat transfer coefficient (W/m²·K)
- Acooling = Cooling surface area (m²)
Cooling Strategies:
| Method | Application | Effectiveness | Complexity |
|---|---|---|---|
| Radiation cooling | Space reactors | Moderate | Low |
| Forced air cooling | Industrial pumps | Good | Low |
| Water jacket cooling | Large ALIPs | Excellent | Moderate |
| Heat pipe cooling | Compact PMPs | Very Good | High |
| Thermal isolation | All designs | Essential | Low |
Critical Design Rule: For NdFeB magnets, maintain temperature < 80°C under all operating conditions. For SmCo, limit to < 350°C. Above these temperatures, permanent magnet pumps require electromagnets or active cooling systems.
9. Flow Instabilities & Cavitation
Formula 7: Cavitation Onset Velocity
In liquid metal EMPs, cavitation occurs when local pressure drops below vapor pressure:
ucavitation = √[2(Plocal - Pvapor) / ρ]
Practical Limit: Empirical data shows cavitation instabilities begin at flow velocities exceeding ~9.14 m/s (30 ft/s) in sodium systems. Above this threshold:
- Pressure pulsations increase dramatically
- Flow becomes unstable and oscillatory
- Pump efficiency degrades
- Structural vibration may damage components
Mitigation Strategies:
- Limit design velocity to 7–8 m/s
- Use diffuser sections to reduce velocity after the pump
- Maintain adequate NPSH (subcooling)
- Avoid sharp channel transitions that create local low-pressure zones
Formula 8: MHD Instability Criteria
At high magnetic fields and currents, magnetohydrodynamic instabilities can develop:
Ha = B · L · √(σ / (ρ · ν))
Where Ha = Hartmann number (dimensionless). When Ha>1000, flow becomes laminar and stable. When Ha<100, turbulent instabilities may occur.
10. Applications Across Industries
Table 3: Electromagnetic Pump Application Matrix
| Industry | Fluid | Pump Type | Temperature | Key Advantage |
|---|---|---|---|---|
| Nuclear (SFR) | Sodium | ALIP | 300–550°C | No moving parts in radioactive sodium; inherent reliability |
| Nuclear (LFR) | Lead-Bismuth | ALIP/DC | 400–600°C | Handles corrosive LBE without seals |
| Nuclear (Fusion) | Lithium/Lead-Lithium | DC conduction | 300–500°C | Tritium breeding + cooling; no contamination |
| Concentrated Solar | Sodium, salt | ALIP | 300–600°C | High-temperature heat transfer; thermal storage |
| Aluminum Casting | Molten Al | PMP | 700–750°C | Non-contaminating transport; no dross formation |
| Steel Processing | Molten steel | Induction | 1,500–1,600°C | Controlled flow in continuous casting |
| Semiconductor Cooling | Gallium alloy | DC micro-EMP | 30–80°C | Ultra-compact; no vibration; precise flow |
| Space Nuclear | NaK | DC/TE | 300–650°C | Zero-g operation; no bearings; radiation tolerant |
| Medical Devices | Blood (MHD) | Micro-EMP | 37°C | Non-contact pumping; no hemolysis |
11. Comparison with Mechanical Pumps
Table 4: Electromagnetic vs. Mechanical Pump Comparison
| Parameter | Electromagnetic Pump | Centrifugal Mechanical Pump |
|---|---|---|
| Moving parts | None in fluid path | Impeller, shaft, bearings, seals |
| Maximum temperature | 600°C (standard); 1,600°C (special) | ~350°C (standard seals); 500°C (special) |
| Fluid compatibility | Any conductive liquid | Limited by corrosion, erosion, temperature |
| Efficiency | 10–55% | 60–85% |
| Flow control | Excellent (current-controlled) | Good (VFD or valve-controlled) |
| Maintenance | Minimal (no wear parts) | Regular (bearings, seals, impeller) |
| Leakage risk | Very low (no shaft seal) | Present (mechanical seal required) |
| Startup time | Instantaneous | Requires priming, warm-up |
| Power density | Moderate | High |
| Cost (small scale) | Higher | Lower |
| Cost (large scale, exotic fluid) | Competitive or lower | Very high (special materials, seals) |
| Noise/vibration | Very low (no mechanical contact) | Moderate to high |
| Reliability in hazardous fluids | Excellent | Poor to moderate |
Economic Break-Even Analysis:
For pumping liquid sodium at 500°C:
- Mechanical pump: Requires special bearings ($50,000/year), seals ($30,000/year), impeller replacement ($100,000 every 3 years)
- EMP: No wear parts; only power supply maintenance ($5,000/year)
10-year lifecycle cost:
- Mechanical: $1,200,000 (including 3 overhauls)
- EMP: $800,000 (including 15% higher energy cost)
EMP savings: $400,000 over 10 years
12. Troubleshooting Electromagnetic Pump Systems
| Symptom | Diagnostic | Root Cause | Corrective Action |
|---|---|---|---|
| Low flow, normal current | Check magnetic field strength; inspect channel | Demagnetization; channel blockage; electrode erosion | Replace magnets; clean channel; replace electrodes |
| Low flow, high current | Measure voltage drop; check fluid conductivity | Low fluid conductivity (contamination, wrong temperature); short circuit | Verify fluid purity; check temperature; inspect insulation |
| Flow pulsation | Spectrum analysis of pressure signal | AC pump at line frequency; MHD instability; cavitation | Switch to DC or higher frequency; reduce current density; lower velocity |
| Magnet overheating | Measure magnet temperature | Insufficient cooling; excessive heat leakage from channel | Improve cooling; add thermal barrier; reduce operating temperature |
| Electrode erosion (conduction) | Visual inspection; measure electrode thickness | Electrochemical dissolution; high current density | Upgrade to molybdenum/tungsten; reduce current density; verify polarity |
| Insulation failure | Megger test; check for shorts | Thermal degradation; cracking from thermal expansion; sodium ingress | Replace ceramic insulation; improve thermal expansion design |
| Efficiency degradation | Compare to baseline performance | Increased channel wall conductivity (sodium deposition); magnet demagnetization | Clean channel; replace magnets; verify operating temperature |
| Control instability | Review current/flow relationship | Non-linear MHD effects at high field; sensor drift | Implement feedback control; recalibrate sensors; reduce field strength |
13. Conclusion: The Future of Contactless Pumping
The electromagnetic pump is not merely an alternative to mechanical pumping—it is the only viable solution for fluids that destroy conventional pumps. Liquid metals at 600°C, corrosive salts, and toxic heavy metals demand a pump with no moving parts, no seals, and no bearings. The EMP delivers this through the elegant physics of magnetohydrodynamics.
The technology continues to evolve. Permanent magnet pumps are achieving 60% efficiency in aluminum casting applications. Miniaturized DC conduction pumps are enabling microfluidic systems for medical devices. Annular linear induction pumps remain the backbone of fast breeder reactor safety systems, circulating sodium through primary loops with reliability that mechanical pumps cannot match.
The formulas, performance curves, and material specifications in this guide provide the technical foundation for electromagnetic pump selection. Remember three principles:
- Efficiency is not the primary metric. An EMP at 30% efficiency that operates for 20 years without maintenance is more economical than a mechanical pump at 80% efficiency that requires annual overhaul.
- Material compatibility is everything. The wrong electrode material in a sodium pump will dissolve within months. The wrong magnet cooling strategy will cause demagnetization within hours.
- Cavitation is the speed limit. No amount of current density can overcome the 9.14 m/s cavitation threshold. Design for 7–8 m/s maximum velocity and live within the limit.
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