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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 TypeCurrent IntroductionEfficiencyMax TemperatureFlow RangePressure RangeBest Application
DC Conduction PumpDirect current via electrodes contacting fluid25–40%600°C (with cooling)0.1–50 m³/h0.1–5 barLaboratory loops, small sodium systems, precise flow control
AC Conduction PumpAlternating current via electrodes15–30%500°C0.5–100 m³/h0.2–10 barMedium-scale systems, transformer-coupled power
Linear Induction Pump (LIP)Induced current from traveling magnetic field30–50%600°C10–500 m³/h0.5–15 barLarge reactor cooling, industrial metal transport
Annular Linear Induction Pump (ALIP)Induced current in annular channel35–55%600°C25–1,000 m³/h1–20 barNuclear reactor primary cooling, large-scale sodium systems
Permanent Magnet Pump (PMP)Rotating permanent magnets induce current40–60%400°C (magnet limit)1–200 m³/h0.5–10 barAluminum casting, compact systems, no external field coils
Thermoelectric (TE) PumpSelf-generated current from temperature gradient5–15%800°C0.01–5 m³/h0.05–1 barDecay 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:

  1. Three-phase AC in the stator creates a rotating (traveling) magnetic field
  2. The traveling field induces circumferential currents in the liquid metal
  3. Interaction between induced currents and the magnetic field produces axial Lorentz force
  4. 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):

ModelMax Flow (m³/h)Max Temp (°C)ΔP (bar)Max Pressure (bar)NPSH (bar abs)
LA12546001.3150.7
LA15086001.5150.9
LA200126003.0150.8
LA300256005.0200.8
LA400506005.0150.8
LA5001406004.0151.0

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

ComponentSodium/NaK ServiceLead-Bismuth EutecticAluminum/MagnesiumHigh-Temp Lithium
Channel316L SS, refractory metal316L SS, T91Graphite, SiC-coated steelNiobium, molybdenum
ElectrodesCopper, molybdenumMolybdenum, tungstenGraphiteTungsten, rhenium
Magnets (PMP)NdFeB (cooled to < 80°C)NdFeB (cooled)SmCo (to 350°C)SmCo (to 350°C)
Stator Windings (ALIP)Copper, ceramic insulationCopper, ceramic insulationCopper, standard insulationSilver, ceramic insulation
Yoke/CoreSilicon steel laminationsSilicon steelSilicon steelCobalt-iron alloy
Seals/GasketsMetal seals, welded jointsMetal sealsCeramic fiberMetal 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:

FluidTemperature (°C)Conductivity (S/m)Density (kg/m³)
Sodium (Na)3001.0 × 10⁷880
Sodium (Na)5008.5 × 10⁶820
NaK-78 (eutectic)3002.5 × 10⁶850
Lead-Bismuth (LBE)4001.0 × 10⁶10,200
Mercury (Hg)201.0 × 10⁶13,500
Aluminum (Al)7003.5 × 10⁶2,400
Gallium (Ga)303.7 × 10⁶6,100

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:

MethodApplicationEffectivenessComplexity
Radiation coolingSpace reactorsModerateLow
Forced air coolingIndustrial pumpsGoodLow
Water jacket coolingLarge ALIPsExcellentModerate
Heat pipe coolingCompact PMPsVery GoodHigh
Thermal isolationAll designsEssentialLow

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

IndustryFluidPump TypeTemperatureKey Advantage
Nuclear (SFR)SodiumALIP300–550°CNo moving parts in radioactive sodium; inherent reliability
Nuclear (LFR)Lead-BismuthALIP/DC400–600°CHandles corrosive LBE without seals
Nuclear (Fusion)Lithium/Lead-LithiumDC conduction300–500°CTritium breeding + cooling; no contamination
Concentrated SolarSodium, saltALIP300–600°CHigh-temperature heat transfer; thermal storage
Aluminum CastingMolten AlPMP700–750°CNon-contaminating transport; no dross formation
Steel ProcessingMolten steelInduction1,500–1,600°CControlled flow in continuous casting
Semiconductor CoolingGallium alloyDC micro-EMP30–80°CUltra-compact; no vibration; precise flow
Space NuclearNaKDC/TE300–650°CZero-g operation; no bearings; radiation tolerant
Medical DevicesBlood (MHD)Micro-EMP37°CNon-contact pumping; no hemolysis

11. Comparison with Mechanical Pumps

Table 4: Electromagnetic vs. Mechanical Pump Comparison

ParameterElectromagnetic PumpCentrifugal Mechanical Pump
Moving partsNone in fluid pathImpeller, shaft, bearings, seals
Maximum temperature600°C (standard); 1,600°C (special)~350°C (standard seals); 500°C (special)
Fluid compatibilityAny conductive liquidLimited by corrosion, erosion, temperature
Efficiency10–55%60–85%
Flow controlExcellent (current-controlled)Good (VFD or valve-controlled)
MaintenanceMinimal (no wear parts)Regular (bearings, seals, impeller)
Leakage riskVery low (no shaft seal)Present (mechanical seal required)
Startup timeInstantaneousRequires priming, warm-up
Power densityModerateHigh
Cost (small scale)HigherLower
Cost (large scale, exotic fluid)Competitive or lowerVery high (special materials, seals)
Noise/vibrationVery low (no mechanical contact)Moderate to high
Reliability in hazardous fluidsExcellentPoor 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

SymptomDiagnosticRoot CauseCorrective Action
Low flow, normal currentCheck magnetic field strength; inspect channelDemagnetization; channel blockage; electrode erosionReplace magnets; clean channel; replace electrodes
Low flow, high currentMeasure voltage drop; check fluid conductivityLow fluid conductivity (contamination, wrong temperature); short circuitVerify fluid purity; check temperature; inspect insulation
Flow pulsationSpectrum analysis of pressure signalAC pump at line frequency; MHD instability; cavitationSwitch to DC or higher frequency; reduce current density; lower velocity
Magnet overheatingMeasure magnet temperatureInsufficient cooling; excessive heat leakage from channelImprove cooling; add thermal barrier; reduce operating temperature
Electrode erosion (conduction)Visual inspection; measure electrode thicknessElectrochemical dissolution; high current densityUpgrade to molybdenum/tungsten; reduce current density; verify polarity
Insulation failureMegger test; check for shortsThermal degradation; cracking from thermal expansion; sodium ingressReplace ceramic insulation; improve thermal expansion design
Efficiency degradationCompare to baseline performanceIncreased channel wall conductivity (sodium deposition); magnet demagnetizationClean channel; replace magnets; verify operating temperature
Control instabilityReview current/flow relationshipNon-linear MHD effects at high field; sensor driftImplement 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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