flowchart TD
%% EXTRACTION AND PREPARATION
KROT[Mole] -->|dump| BUN[Hopper]
BUN -->|regolith| SEP[Mag. Separator]
BUN -.->|large chunks| GR[Vibrating Screen]
GR -.->|>5 cm| DR[Crusher]
DR -.->|chute| SEP
%% SEPARATION - splitting into 2 streams
SEP -->|36 t| MAGN[Magnetic Fraction]
SEP -->|564 t| NMAG[Non-magnetic Fraction]
%% FLOW DISTRIBUTOR
NMAG --> SPLIT[Flow Splitter]
%% PROCESSING LINES
subgraph LINES[Processing Lines]
direction TB
subgraph TITANIUM[Titanium Line]
SF3[Sublimation 450C]
SF3 -->|chute| TI_OX[Calcination 900C]
TI_OX --> TI_OUT[Titanium dioxide + sulfur]
end
subgraph GLASS_LINE[Glass Line]
SF1[Small Furnace 1400C]
SF1 -->|melt| FILT[W Bushings]
FILT --> FIBER[Fiber 28 t]
end
subgraph MRE_LINE[MRE Line]
SF2[Solar Furnace 1500C]
SF2 -->|melt| MRE[MRE Cell]
MRE --> O2[Oxygen 250 t]
MRE --> FESI[Iron-silicon 35 t]
MRE --> SLAG[Slag 251 t]
end
end
%% Links from separation to furnaces
MAGN -->|chute| SF3
SPLIT -->|28 t| SF1
SPLIT -->|536 t| SF2
%% DISTILLATION
SLAG -->|pipe| EQU024[Induction Furnace]
EQU024 --> EQU031[Condenser K]
EQU031 --> EQU032[Condenser Na]
EQU032 --> EQU033[Condenser Mg]
EQU033 --> AL_OUT[Aluminum 42 t]
%% Styles
style TITANIUM fill:#a8d4e8
style GLASS_LINE fill:#b8e0d2
style MRE_LINE fill:#e8a8d4
style SPLIT fill:#ffe4b5
Regolith Processing
Complete raw material processing cycle: from regolith to finished materials.
Molten Regolith Electrolysis (MRE) is not a theoretical concept but a technology at TRL 6-7:
- NASA KSC (2024): MRE cell testing in the ASSIST chamber under simulated lunar conditions
- Lunar Resources: Processing 25 kg of regolith over 36 hours with measured oxygen yield
- Blue Origin (Blue Alchemist): Complete MRE cycle with Fe/Si/Al purification and solar cell production. CDR passed (September 2025) — per NASA standards, CDR corresponds to ≥TRL 6
- Sierra Space (2024): Carbothermal O₂ extraction in a thermal vacuum chamber
NASA quote: “Both Carbothermal Reduction and MRE have demonstrated operation under simulated lunar conditions to TRL 5/6” (category-wide assessment; Blue Origin specifically — ≥TRL 6)
Details: Technologies and Sources
Process Overview
Technology Cycle: Factory Equipment
Physical chain of units with IDs from the database:
Materials Output (600 t regolith/day)
| Product | t/day | % | Source | Application |
|---|---|---|---|---|
| Oxygen (O₂) | 250 | 42% | MRE | Dome atmosphere, oxidation |
| Fe-Mn steel | ~11 | 2% | MRE + titanium | Frames, rails, tools |
| Ferrosilicon -> Si | 35 -> 25 | 6% | MRE -> zone refining | Electronics, solar panels |
| Aluminum (Al) | 42 | 7% | Distillation | Mirrors, motor windings |
| Magnesium (Mg) | 48 | 8% | Distillation | Al-Mg alloys, MgO ceramics |
| NaK coolant | ~5 | 1% | K + Na | Electronics cooling |
| Sodium (Na) | ~18 | 3% | Distillation | NaS batteries (anode) |
| Sulfur (S) | 18 | 3% | Titanium line | NaS batteries (cathode) |
| TiO₂ | 3 | 0.5% | Titanium line | Mirror electrochromics |
| Glass fiber | 28 | 5% | Silicates (SiO₂ + Al₂O₃ + CaO) | Insulation, composites |
| Carbon (C) | (~6) | — | Phase 2 (not in balance) | Hadfield steel, anodes |
| Waste/slag | ~143 | 24% | Distillation 138 + titanium 5 | Fill, ballast |
Notes:
- Fe-Mn steel: Iron from Mercury contains ~6% Mn - this is automatically a low-alloy steel (MESSENGER)
- Ferrosilicon: Si exits MRE together with Fe. Purification via zone refining (35 t -> 25 t pure Si)
- NaK: Eutectic 78% K + 22% Na, liquid at -12C - ideal coolant for space
- Oxygen: Not for breathing (no humans) - for dome atmosphere (0.1 atm O₂) and chemical processes
- Carbon: Phase 2 - requires separate factories at LRM deposits (not included in 600 t balance).
- CaO (calcium oxide): ~10% of regolith (~60 t/day) — not reduced in MRE (Ca is too reactive). Partially used: ~3 t/day for glass fiber (flux) and WAAM fluxes. Remainder (~57 t/day) stays in final slag (fill, ballast).
Reception and Crushing
Dirty zone - VACUUM.
Critical condition: All processes are completely atmosphere-independent.
Regolith Preparation
Mercury regolith is the product of billions of years of meteorite bombardment. Average particle size 40-100 microns, 95% of material is already finer than 1 mm. Regolith goes directly to magnetic separation.
Optional: For deep drilling into bedrock, screen and crusher are used.
Vibratory Feeder (Transport)
| Parameter | Value |
|---|---|
| Drive | Electromagnet |
| Principle | Tray vibrates finely (50 Hz), material “flows” |
| Advantage | No bearings or friction parts |
Electromagnetic Vibrator Operating Principle
An electromagnet is a coil with an iron core. When current flows, a magnetic field is created that attracts the armature.
Operating cycle (50 Hz AC):
- Current in coil -> magnet attracts armature -> tray shifts
- Current = 0 -> springs return tray
- Current reverses sign -> attraction again (magnet works on |I|)
- Result: 100 oscillations/sec (frequency doubles)
Why material “flows”: - When tray moves up-forward, particles are thrown - When tray moves down-backward, it moves away from under the particles - Particles land slightly ahead -> micro-jumps sum into flow
Design for Mercury
Vacuum advantages: - No friction wear (no atmosphere = no oxidation) - No bearings - nothing to lubricate - Simple control - voltage adjustment changes amplitude
Earth analogs: Eriez, Syntron electromagnetic feeders - standard in food, pharmaceutical, and mining industries since the 1950s.
Melting and Separation
Hot zone - VACUUM.
The chemical reactor sits on open ground. Vacuum serves as ideal thermal insulation.
Magnetic Separation
Operating Principle
Material separation by magnetic properties. Mercury regolith contains two types of minerals:
| Type | Share | Minerals | Magnetic Properties |
|---|---|---|---|
| Magnetic | 5-6% | Ilmenite (FeTiO₃), troilite (FeS) | Paramagnetics - attracted to magnet |
| Non-magnetic | 94% | Silicates (Si, Al, Mg, Ca, O) | Diamagnetics - weakly repelled |
In a 0.5-1.5 T magnetic field, paramagnetic minerals (containing Fe) are attracted to the magnet, while silicates are not. This allows stream separation.
Drum Separator Design
flowchart TD
subgraph INPUT["FEED"]
R[/"Regolith<br/>25 t/hour"/] --> VJ["Vibratory Feeder<br/>(electromagnetic)"]
end
subgraph SEPARATOR["DRUM SEPARATOR"]
VJ --> DRUM["Drum dia 800x1200mm<br/>rotation 20 rpm"]
DRUM --> |"electromagnets<br/>inside drum"| MAG["Magnetic Zone<br/>0.5-1.5 T"]
MAG --> SCRAPER["Scraper<br/>(magnetic fraction removal)"]
end
subgraph OUTPUT["SEPARATION"]
SCRAPER --> M[/"Magnetic Fraction<br/>FeS + FeTiO3<br/>1.5 t/hour"/]
DRUM --> |"falls down"| NM[/"Non-magnetic Fraction<br/>silicates -> MRE<br/>23.5 t/hour"/]
end
style SEPARATOR fill:#e8d4a8
style M fill:#c0c0c0
style NM fill:#f5deb3
Parameters
| Parameter | Value |
|---|---|
| Type | Drum with electromagnets |
| Drum diameter | 800 mm |
| Drum length | 1200 mm |
| Field strength | 0.5-1.5 T |
| Rotation speed | 20 rpm |
| Capacity | 25 t/hour (600 t/day) |
| Mass | 500 kg |
| Power | 20 kW |
Electromagnetic scraper: Metal strip moves left-right on electromagnetic guides. No friction, no bearings - nothing to wear.
Earth analogs: Eriez DR Drum Separator, STEINERT MT - used in mining for magnetite and ilmenite separation.
Processing Lines
After magnetic separation, material is distributed to specialized lines.
Flow Splitter
Non-magnetic fraction (564 t/day) is distributed between glass and MRE lines by a simple mechanical splitter:
- 5% (28 t) -> narrow outlet -> glass fiber line
- 95% (536 t) -> wide outlet -> MRE line
The 1:19 ratio is set by outlet geometry. No electronics - pure mechanics.
Lines Summary Table
| # | Line | Input | t/day | Output |
|---|---|---|---|---|
| 3.1.1 | Glass Fiber | Silicates (5%) | 28 | SiO₂ fiber |
| 3.1.2 | MRE Electrolysis | Silicates (95%) | 536 | O₂ 250t, Fe/Si 35t, slag 251t |
| 3.1.3 | Distillation | MRE slag | 251 | Al 42t, Mg 48t, Na 20t, K 3t, slag 138t |
| 3.1.4 | Titanium Line | Magnetic fraction | 36 | TiO₂ 3t, S 18t, Fe 10t, waste 5t |
| 3.1.5 | Carbon (opt.) | LRM regolith | 200 | Graphite ~6t |
*Distillation processes slag from MRE, not input regolith - this is a sequential, not parallel line.
Wall Transit
Circulatory system.
How to transfer melt (1500C) through a cold crater (-150C) into the factory without losing atmosphere?
Electromagnetic Input with Active Insulation
A pipe with liquid metal passes through the dome’s airlock panel.
Physics: Pipe is a “sandwich” (Ceramics + Inductors + MLI).
| Component | Function |
|---|---|
| MHD pump | Magnetic field pushes metal. No moving parts inside the pipe |
| Plug | Made of the metal itself - provides sealing |
U-shaped Hydraulic Seal (Siphon)
The pipe makes a deep bend downward.
| Element | Function |
|---|---|
| Principle | At the bottom of the U-tube there is always a “plug” of heavy liquid iron, blocking gas escape from the dome |
| Emergency system | Ceramic gate valve (slide gate) automatically cuts the channel when metal level drops |
Casting Unit
Buffering and dosing - INSIDE DOME.
Critical problem: electrolysis runs continuously, but casting is batch. A buffer is needed.
Tundish
Intermediate vessel between MHD input and crystallizer.
| Parameter | Value |
|---|---|
| Capacity | 2-3 tonnes of melt |
| Material | Steel shell + refractory lining (magneite MgO) |
| Heating | Induction (maintaining 1550C temperature) |
| Function | Buffering, composition averaging, inclusion flotation |
Localization: Magnesite (MgO) is produced from local regolith magnesium (8% content, ~48 t/day). Steel shell - from local Fe-6%Mn iron.
Appendix: Screen and Crusher
Optional equipment for working with bedrock during deep drilling.
Vibrating Screen
The “Mole” robot dumps material onto an inclined grate.
| Parameter | Solution |
|---|---|
| Drive | Unbalanced motors (inertia) |
| Dust | Does not hang as a cloud - falls straight down (ballistics). Filters not needed |
| Cooling | Conductive (through frame metal) |
Why Dust Does Not Float in Vacuum?
On Earth, fine particles “float” in air due to aerodynamic drag - air molecules slow the fall. In vacuum there is no air, so:
- All particles (from boulders to micron dust) fall with the same acceleration
- On Mercury g = 3.7 m/s² - a particle travels 1 meter in ~0.7 seconds
- Trajectory is a pure parabola (ballistics), like a thrown stone
- Dust does not form clouds - it simply falls
Consequence: Filters and dust suppression systems are not needed. This radically simplifies equipment.
Analogy: Apollo experiments showed that lunar dust behaves like sand - it pours and settles instantly.
Unbalanced Motors
The simplest way to create vibration is to attach an eccentric weight to the motor shaft.
| Component | Function |
|---|---|
| Electric motor | Standard induction, ~3000 rpm |
| Eccentric | Asymmetric weight on shaft |
| Centrifugal force | F = mw²r - creates vibration |
Principle: During rotation, the eccentric’s center of mass is offset from the axis -> centrifugal force arises -> motor housing “shakes”. Two motors rotating in opposite directions create directed vibration.
Advantages:
- No wearing parts except bearings
- Works in vacuum without modifications
- Amplitude is adjusted by changing eccentric mass
Earth analogs: Martin Engineering, VIBCO vibrators - used in mining for decades.
Induction Motor Design
The induction motor is the workhorse of industry. On Mercury, it is adapted to local materials and vacuum:
- Windings from aluminum - no copper on Mercury (MESSENGER), Al has 60% conductivity of Cu -> motor is 20-30% heavier
- Bearings ceramic Al₂O₃ (corundum) - work without lubrication in vacuum, 100% local production
- Cooling conductive - fan not needed, no convection in vacuum
Factory capacity: Producing ~10 t iron and 42 t aluminum per day, the factory can produce hundreds of motors/day - significant surplus.
Conductive Cooling
In vacuum there is no air -> no convection. Heat escapes only two ways:
- Radiation - radiators “shine” into space
- Conduction - heat flows through solid body contact
For the screen, the second method is used:
| Element | Temperature |
|---|---|
| Motor (operating) | +80…+150C |
| Frame (massive) | Intermediate |
| Crater floor ground | -150C (permanent shadow) |
Heat flow: Motor -> bolts -> frame -> supports -> ground. Cold ground works as infinite heat sink.
Alternative: Radiator panels radiating toward space (3 K). But for mechanical equipment, conduction is simpler.
Jaw Crusher
| Parameter | Value |
|---|---|
| Principle | Mechanical plate compression |
| Plate material | Low-alloy steel (Fe-6%Mn) |
| Vacuum advantage | No corrosion - longer service life |
| Plate life | ~2-3 months, then replacement |
Manganese in Mercury Iron
| Parameter | Value |
|---|---|
| Mn content in crust | ~0.1% (MESSENGER data) |
| Mn output | ~600 kg/day (from 600 t regolith) |
| Mn content in iron | ~6% (600 kg Mn / 10000 kg Fe) |
Conclusion: Iron from Mercury already contains ~6% manganese - this is low-alloy steel with improved mechanical properties. Manganese is reduced together with iron during MRE electrolysis (Mn density is similar to Fe), requiring no separate process.
Crusher plate consumption:
| Parameter | Value |
|---|---|
| Plate set mass | ~400 kg |
| Replacement | Every 2-3 months |
| Consumption | ~1.6 t/year |
| Share of Fe production | 0.04% (at 3650 t Fe/year) |
Conclusion: Fe-6%Mn plates wear faster than Hadfield steel, but consumption is so low (0.04% of iron production) that metallurgy complexity is not justified.
Equipment (Screen and Crusher)
See Also
- Production - complete factory cycle
- Energy - factory power supply
- Batteries - NaS batteries from sulfur