Emerson Electric · Shakopee, Minnesota

Salt. Water.
Iron. Copper.

The four most abundant industrial materials on Earth.
A battery that may never need replacing.

Scroll ↓
The Discovery
In February 2026, a team at City University of Hong Kong built an aqueous battery from magnesium chloride dissolved in water.

It charged and discharged 120,000 times without degrading.

The electrolyte is not consumed. It carries ions between electrodes but is not chemically transformed. After a hundred thousand cycles, the salt water is still salt water.
Chen et al. · Nature Communications · February 2026
What the Paper Proved
0
Charge cycles
Lithium-ion: 3,000–5,000
$32–64
Projected cost per kWh
vs. lithium-ion: $130–$150
2.2V
Operating window
Highest for aqueous batteries
0
Hazardous materials
No cobalt. No lithium. No fire risk.
95%
US-sourced materials
New Mexico. North Carolina. Arizona.

The chemistry uses a CuFe-PBA cathode, a COP anode, and MgCl₂ electrolyte — all of which can be sourced domestically, manufactured without clean rooms, and shipped without hazmat classification.

The Pantry
What Emerson already makes.

Every instrument needed to build, test, and control this battery is already in the Emerson product catalog. The pantry is stocked.

DeltaV
The brain. Distributed control system that orchestrates the electrolyte preparation skid — every pump, valve, heater, and sensor in a closed-loop recipe.
Rosemount 228
Toroidal conductivity sensor. Monitors electrolyte concentration in real time. First signal that copper contamination is accumulating.
Rosemount 372 / 3900
Wireless pH and ORP sensors. Tracks the 4.91–7.02 pH window that confirms electrolyte health after cycling.
Micro Motion ELITE
Coriolis density meter. Measures electrolyte density to 0.0005 g/cm³ — the definitive concentration measurement.
Micro Motion Fork
Viscosity sensor. Detects electrolyte degradation before it shows up in cycling performance.
Rosemount 928
Wireless gas monitor. Quantifies H₂ evolution during cycling — the safety sentinel.
NI HPS-17000
150 kW cell cycler. Charges and discharges individual cells at grid-relevant rates. The workhorse of Phase 1.
NI NHR-9300
Pack-level tester. Scales from cells to modules. 500 kW capacity for Phase 2 deployment.
NI PXI + EIS
Electrochemical impedance spectroscopy. Sees inside the cell — ion transport, interface resistance, degradation mechanisms.
Fisher / ASCO
Control and solenoid valves. The hands and fingers of the electrolyte skid. Precision flow control.
Afag
Linear motion and automated assembly. Positions electrodes, stacks cells, builds packs. The Phase 3 production line.
Zitara BMS + Ovation Green
Battery management system and grid-scale BESS integration. The software layer that connects batteries to buildings.
The Shopping List
What we need to order.

Phase 1 materials cost less than a mid-range sedan. Everything ships standard freight. Nothing requires hazmat handling.

Material Grade Source $/kg Phase 1 Qty Cost
MgCl₂ · 6H₂O Battery-grade (99.9%) Nedmag · Veendam, NL $3.00 100 kg $300
MgCl₂ · 6H₂O Industrial (95%) Intrepid Potash · Carlsbad, NM $0.40 200 kg $80
CuSO₄ · 5H₂O Reagent Freeport-McMoRan · Phoenix, AZ $3.00 20 kg $60
K₃[Fe(CN)₆] Reagent Domestic chemical distributors $8.00 15 kg $120
Pyrrole monomer Reagent Sigma-Aldrich / domestic $50.00 5 kg $250
CuO (copper oxide) Technical Freeport-McMoRan / domestic $5.00 10 kg $50
Celgard separator Battery Celgard · Charlotte, NC $3/m² 100 m² $300
Prismatic cell hardware Domestic fabrication $80/cell 50 cells $4,000
DI water system 1 unit $8,000
Lab consumables Annual $15,000
Phase 1 Annual Materials Budget ~$28,000

The raw materials are commodity-priced and globally abundant. The value is in the process — and the instruments that control it.

The Kitchen
You already know this building.

Every department. Every hallway. Every lab. The Shell Space sits at the northeast corner — 10,000 square feet, currently empty, adjacent to the first two customers on the grid.

Shakopee Facility Blueprint
THE SALT KITCHEN
10,000 SF · Currently Empty
Customer #1 — North Office
Customer #2 — Cafeteria
⚡ ↓
⚡ →
Receiving
DP Level
Pressure
Shipping
Gas Mfg
West Office
Hub Office
Temperature SA
Wireless
Stockroom

Emerson Shakopee main floor — Pressure, DP Level, Temperature, Wireless, Gas Manufacturing. The instruments that run the world's refineries are built here. The Salt Kitchen goes in the northeast corner.

Two Burners, One Kitchen
Parallel R&D. Converging at qualification.
Track A — The Chemistry
Build cells. Validate the paper.

Pre-purified MgCl₂ from Nedmag (Netherlands) — known-good electrolyte that eliminates supply chain variables during foundational chemistry work.

Zone B: Cell assembly & CuFe-PBA cathode synthesis
Zone C: Cycling, EIS, ICP analysis

Goal: Confirm 120,000 cycles at C/4 to C/2 grid rates.

Track B — The Purification
Refine the feedstock. Build the process.

Industrial MgCl₂ from Intrepid Potash (Carlsbad, NM) — $0.40/kg deicing-grade salt, purified in-house to battery-grade on the DeltaV electrolyte prep skid.

Zone A: Ion exchange, selective precipitation, recrystallization
Rosemount 228 + 372 + ELITE: Closed-loop quality control

Goal: Match Nedmag spec with domestic feedstock. Then switch.

When Track B electrolyte passes ICP qualification against Track A baseline → domestic supply replaces imported.
And the purification process itself becomes a product Emerson can sell.
Inside the Skid
What purification actually looks like.

Industrial-grade MgCl₂ enters from the left. Battery-grade electrolyte exits on the right. Every step is measured, controlled, and automated by Emerson instruments.

DeltaV Distributed Control System
— orchestrating every pump, valve, heater, and sensor in closed-loop control
1
🧂
Dissolution
Industrial MgCl₂ from Intrepid Potash dissolves in heated DI water. Chunky, tan-colored crystals become a cloudy brown brine.
Micro Motion ELITE
Density → confirms concentration
2
⬇️ Fe³⁺ Mn²⁺
Precipitation
NaOH added at controlled pH. Iron hydroxide and manganese hydroxide precipitate as rust-colored sludge. Heavy metals drop out of solution.
Rosemount 372
pH control → precise NaOH dosing
Fisher/ASCO valves
3
▤ ▥ ▦
Filtration
Precipitated solids removed. The brine clears from brown to pale amber. Ca²⁺ and sulfate ions remain — next stage handles those.
Rosemount 228
Conductivity → confirms solids removed
4
⚫ ⚪ ⚫
Ion Exchange
Type 4A zeolite columns selectively strip Ca²⁺ from the brine. Regenerated with HCl. Continuous flow, automated cycling. The brine is now clear.
Rosemount 228
Conductivity → Ca²⁺ breakthrough detection
Rosemount 372 pH monitoring
5
Battery-Grade
Controlled cooling crystallizes pure MgCl₂·6H₂O. White, translucent crystals. >99.9% purity. Dissolve in DI water for electrolyte. Ready for Track A cells.
ICP Analysis
Validates against Nedmag baseline
Micro Motion ELITE final density
INDUSTRIAL · 95% · $0.40/kg BATTERY-GRADE · 99.9% · $3.00/kg equiv.
Intrepid Potash · Carlsbad NM
Zone B · Cell Assembly

The entire process runs on equipment Emerson already sells. The DeltaV recipe, once proven, becomes the template for Product 6 — the Sustainable Electrolyte Recovery System.

Safety Architecture
Every killswitch. Every safeguard. Every layer.

The battery operates at 2.2V — above the 1.23V thermodynamic threshold for water electrolysis. Concentrated MgCl₂ suppresses hydrogen evolution, but does not eliminate it. Trace H₂ is a known characteristic of all high-voltage aqueous batteries. This is the system that manages it.

⚠️
THE KNOWN RISK
Hydrogen gas (H₂) is produced in trace quantities during normal cycling and in larger quantities during overcharge, elevated temperature, or electrode degradation. H₂ is flammable at 4–75% concentration in air. In a properly ventilated lab, trace H₂ dissipates rapidly — but the system is designed so that ventilation failure, sensor failure, or human error alone cannot create a hazardous condition. Every layer is independent.
FIVE INDEPENDENT DEFENSE LAYERS
L1
Detection — Continuous Gas Monitoring
ALWAYS ON
Rosemount 928 wireless multi-gas monitor — continuously measures H₂ concentration in ppm. Mounted at ceiling level in Zone B (cell assembly) and Zone C (testing), where H₂ accumulates first. Alarms at two thresholds:
LOW ALARM · 1,000 ppm · Audible + visual alert · Investigate
HIGH ALARM · 10,000 ppm · Auto-shutdown triggered · Evacuate
H₂ lower explosive limit (LEL) = 40,000 ppm. High alarm fires at 25% of LEL — industry standard safety margin.
L2
Prevention — Overcharge Protection
HARDWARE + SOFTWARE
NI HPS-17000 cell cycler enforces hard voltage cutoffs per channel — cells cannot be charged beyond the programmed upper limit (2.2V nominal, configurable per chemistry). In Phase 2, Zitara BMS provides cell-level voltage monitoring across every cell in every pack, with independent hardware interrupt if any cell exceeds threshold. Two independent systems. Neither trusts the other.
L3
Automated Shutdown — DeltaV Safety Instrumented System
SIL-RATED
DeltaV SIS operates independently from the process control system. On high H₂ alarm OR overtemperature OR overvoltage:
1. All cyclers → immediate open-circuit (cells stop charging/discharging)
2. Fisher/ASCO emergency shutoff valves close on electrolyte lines
3. Ventilation system → maximum exhaust mode
4. Audible alarm + strobe → all personnel alerted
DeltaV SIS is IEC 61511 compliant. The same platform that protects refineries handling pure H₂ at thousands of PSI.
L4
Ventilation — Passive + Active Exhaust
CONTINUOUS
Laboratory fume hood in Zone B provides continuous negative-pressure exhaust during cell assembly and cathode synthesis. Zone C ceiling exhaust sized for 6–12 air changes per hour (ACH) — standard for electrochemistry labs per ANSI/AIHA Z9.5. At 12 ACH, the entire Shell Space air volume is replaced every 5 minutes. H₂ is the lightest gas — it rises and exits first. Backup: natural ventilation path via loading dock doors (northeast wall).
L5
Early Warning — Electrolyte Health Monitoring
PREDICTIVE
H₂ evolution increases before it becomes dangerous — and the electrolyte shows it first. Rosemount 228 conductivity drift signals electrolyte composition change. Rosemount 372 pH shift outside the 4.91–7.02 stable window indicates cathode degradation or parasitic reactions. Micro Motion ELITE density change confirms water loss to electrolysis. These instruments detect the conditions that cause H₂ evolution — hours or days before gas concentration becomes a concern. Fix the cause, not the symptom.
What Emerson already protects
Refinery hydrogen units — pure H₂ at 2,000+ PSI.
Chlor-alkali plants — H₂ and Cl₂ generated at scale.
Ethylene crackers — explosive atmospheres, 24/7.
What the Salt Kitchen produces
Trace H₂ in parts per million from aqueous cells.
In a ventilated lab with 5-minute air replacement.
Monitored by the same instruments that guard refineries.

We don’t just build the battery. We build the safety system that protects it. Because we already do — in every refinery on Earth.

Emergency Procedures
🚨
HIGH H₂ ALARM
DeltaV SIS auto-triggers.
All cycling stops.
Valves close.
Ventilation to max.
🚶
EVACUATE
All personnel exit
Shell Space via NE
loading dock or south
corridor to main floor.
📞
NOTIFY
Facilities & Safety
notified automatically
via DeltaV alarm
forwarding system.
RE-ENTRY
Only after Rosemount 928
reads <500 ppm H₂
for 15 consecutive
minutes. No override.
PERSONNEL PROTECTIVE EQUIPMENT
Standard — All Zones, All Times
Safety glasses · Nitrile gloves · Lab coat · Closed-toe shoes
Standard electrochemistry lab dress. Not a hazmat environment.
Elevated — Cathode Synthesis (Zone B)
P95 respirator when handling K₃[Fe(CN)₆] powder
Fume hood required — contact with acid releases HCN
This is the one chemical that needs respect. Keep away from acids.
Health exposure: Hydrogen (H₂)
H₂ is a simple asphyxiant — biologically inert, no chronic toxicity, no long-term health effects at any concentration. OSHA does not set a permissible exposure limit because it is not toxic. The only risk is oxygen displacement in sealed, unventilated spaces. At trace ppm in a ventilated lab: zero health concern.
NO PEL
Health exposure: MgCl₂ electrolyte
FDA food-grade at battery-spec purity. Water-soluble salt — any inhaled particles dissolve in lung moisture and are cleared by normal mucociliary action. Classified as a nuisance particulate (PNOR), the same OSHA category as table salt dust, flour, and drywall. Zero fibrosis risk. Zero cancer risk. No cumulative lung damage at any documented exposure level.
5 mg/m³
For comparison: Cutting a granite countertop produces crystalline silica dust — an IARC Group 1 carcinogen with an OSHA PEL of just 50 μg/m³. Those insoluble mineral shards lodge permanently in lung tissue and cause irreversible silicosis. MgCl₂ is permitted at 100× that concentration. Handling battery-grade salt is closer to working in a bakery than a stone shop.

For context: lithium-ion batteries risk thermal runaway — uncontrollable fire at 1,000°F that cannot be extinguished with water. Aqueous batteries cannot thermally run away. The electrolyte is water. The worst case is trace hydrogen in a ventilated room.

Mise en Place
Inside the Shell Space. Phase 1: 2,500 SF.
SHELL SPACE · 10,000 SF
ZONE A — Electrolyte Preparation
~600 SF · Track B
DeltaV
SKID
Rosemount 228
Conductivity
Rosemount 372
pH / ORP
Micro Motion
ELITE Density
Ion Exchange
Columns
DI Water System · Fisher/ASCO Valves · Recrystallization
ZONE B — Cell Assembly & Chemistry
~800 SF · Track A
GLOVEBOX
(Ar atmos.)
Fume Hood
Afag Assembly
ZONE C — Testing & Characterization
~1,100 SF · Shared
NI HPS-17000
Cell Cycler
150 kW
NI PXI
EIS System
Environmental
Chamber
ICP Analysis
Rosemount 928
H₂ Monitor
Micro Motion Fork
Viscosity
PHASE 2 & 3 EXPANSION — 7,500 SF
● Track B — Purification ● Track A — Chemistry ● Shared Testing
The Brigade
Five people.

That's the starting lineup to validate the most promising
battery chemistry published this decade.

1
Electrochemist — Track A
Owns CuFe-PBA cathode synthesis, cell assembly, and cycling protocols. Validates Chen et al. at grid-relevant C-rates.
1
Electrochemist — Track B
Owns electrolyte characterization. Develops the purification process that turns $0.40/kg industrial salt into $3/kg battery-grade.
1
DeltaV Engineer
Programs the electrolyte prep skid. Closes the loop between Rosemount sensors, Fisher valves, and the purification recipe.
1
NI Test Engineer
Runs the HPS-17000 cycler and PXI EIS across both tracks. Shared resource. The quality gate for everything.
1–2
Lab Technicians
Sample preparation, equipment maintenance, data logging. The hands of the operation.

Phase 1 creates 5–6 new technical roles in Shakopee.
Phase 3 grows to 26–35 — a new team built from the ground up.

The Meter
What it costs to keep the lights on.
Equipment Avg. Draw Daily kWh
NI HPS-17000 cycling losses (net) 5 kW 120
Glovebox (Ar atmosphere) 3 kW 72
DeltaV electrolyte skid 5 kW 40
Environmental chamber 4 kW 96
Fume hood exhaust 1.5 kW 36
HVAC + lighting (2,500 SF lab) 8 kW 192
ICP, EIS, instruments, DI water 3.5 kW 32
Phase 1 Total ~30 kW ~588 kWh/day
~$23,000 / year

At Minnesota commercial rates ($0.105/kWh).
About 20 homes’ worth of electricity per day — to power a lab that might change how the grid stores energy.

Family Meal
The moment the battery starts powering
the building where it was built.

In a restaurant, family meal is when the kitchen cooks for itself. The staff eats what they make, before the doors open. This is that.

Shell Space lighting & HVAC
Phase 2 · Month 14 · ~35 kW load
North Office sub-panel
Phase 2 · Month 18 · +20 kW
Cafeteria
Phase 2 · Month 22 · +15 kW
Every test cycle IS a power cycle.
The charge/discharge cycles that validate the chemistry are simultaneously the operational cycles that keep the lights on. You're not wasting energy on testing. You're doing useful work.

The Xcel Energy bill is the scoreboard.

The Green Crossover
The math behind Phase 1.
Proven in the lab (Chen et al., 20 A/g)
120,000 cycles · stable pH · no hazardous byproducts · 2.2V window
What Phase 1 must confirm (C/4 to C/2 grid rates)
Cycle life at slower rates · copper accumulation rate · electrolyte reuse · energy efficiency at scale
Manufacturing energy (500 kWh bank) ~25 MWh
Projected lifetime delivery — if cycle life holds 51,000 MWh
~60 days
Projected energy payback
At 1 cycle/day, 500 kWh bank
2,000:1
Projected energy return
Lithium-ion: 10–30:1 · Solar: 10–20:1

If Phase 1 confirms what the paper suggests, the energy return exceeds two thousand to one.

That is the question worth $1.8 million to answer.

Honest Kitchen
What could go wrong.

Four ways this doesn’t work. What we’d see, and when we’d know.

Risk 1
Cycle life doesn’t hold at grid rates
The paper proved 120,000 cycles at 20 A/g — a fast lab rate. Grid storage runs at C/4 to C/2, orders of magnitude slower. Different degradation mechanisms may emerge.
Detection: NI HPS-17000 cycling + NI PXI EIS. Impedance changes visible within first 500 cycles. Go/no-go at Month 6.
Risk 2
Copper contamination is worse than expected
CuFe-PBA cathodes leach copper into the electrolyte. If accumulation is too fast, the electrolyte degrades before remediation can intervene.
Detection: Rosemount 228 conductivity + ICP analysis after every 1,000 cycles. Copper accumulation rate known within first month of cycling.
Risk 3
Purification can’t reach battery-grade
Track B may not achieve 99.9% purity from industrial feedstock using ion exchange and selective precipitation alone. This would keep Emerson dependent on imported Nedmag supply.
Mitigation: Track A runs on Nedmag regardless. Track B failure doesn’t kill the battery — it narrows the supply chain thesis. ICP comparison at Month 9.
Risk 4
Someone else gets there first
The paper is public. CATL, BYD, and every national lab on Earth can read it. The head start has an expiration date.
Advantage: Emerson doesn’t need to own the chemistry. Nobody else has DeltaV + Rosemount + NI + Ovation under one roof. The instruments are the advantage.

Track A and Track B run independently. No single failure kills the program. And every one of these risks is something Emerson instruments can measure.

329
329
years.

A battery installed during Phase 2, cycling once daily,
would still be running in the year 2355.

The building outlasts the engineers who built it.

The electrolyte outlasts the building.

This is not a product. This is infrastructure.
Like copper wire. Like concrete.
Like the telephone line.

From Soft Opening to Grand Opening
The three-phase buildout.
Phase 1: Research Lab
Year 0–1 · 2,500 SF
Validate Chen et al. chemistry at grid-relevant C-rates. Two parallel R&D tracks: battery chemistry (Track A, Nedmag electrolyte) and purification process development (Track B, Intrepid Potash feedstock). Five people. $28K/year in materials.
$1.0M–$1.8M 5 people Load bank → Shell Space lights
Phase 2: Pilot Deployment
Year 1–2 · 5,000 SF
Scale to modules and packs. Connect to building electrical via Zitara BMS and Ovation Green. Full Emerson product stack in concert. Copper remediation loop live — electrowinning recovers Cu at ~$13–14/kg LME (June 2026), turning maintenance into revenue. Family meal: the battery powers Shell Space, then North Office, then Cafeteria.
+$0.9M–$1.7M 8–12 people 100–500 kWh displacing grid
Phase 3: Production Line
Year 2–4 · 10,000 SF
Seven production stations. Repeatable manufacturing. Ship aqueous battery modules to customers. BOM at $32–$64/kWh. 95% US-sourced. No hazmat shipping. No clean rooms. Standard freight. Grand opening.
+$2.0M–$4.0M 26–35 people Customer deployments ship
$3.9M – $7.5M
Total investment across all three phases.
Less than one floor of a lithium gigafactory.
The Scorecard
Phase 1 milestones. Four checkpoints.

What you’ll see at each checkpoint. What kills the project, and what earns the next quarter of funding.

M3
MONTH 3
First cells assembled and cycling
Track A: CuFe-PBA cathode synthesized, first prismatic cells built with Nedmag electrolyte. Initial cycling at C/4 underway. DeltaV skid commissioned for Track B.
Gate: Cells cycle without catastrophic failure. Electrolyte pH within 4.91–7.02 range.
M6
MONTH 6
1,000+ cycles at grid rate. Degradation curve visible.
Track A: EIS impedance data reveals degradation trajectory. Copper accumulation rate measured via ICP. Coulombic efficiency trend established. Track B: first purification runs complete.
Gate: Capacity retention >95% at 1,000 cycles. Copper leach rate supports remediation interval >6 months. Primary go/no-go decision point.
M9
MONTH 9
Track B electrolyte tested against Nedmag baseline
Track B: ICP analysis compares domestically purified MgCl₂ against Nedmag spec. If purity matches, cells switch to domestic electrolyte for remaining cycling. Purification process recipe documented for Product 6 development.
Gate: Track B purity ≥99.9%. Cell performance on domestic electrolyte matches Nedmag baseline within 5%.
M12
MONTH 12
Phase 1 report. Phase 2 go/no-go.
Everything on paper: cycle life projection, copper remediation plan, electrolyte reuse data, energy efficiency at C/4 and C/2, domestic supply chain validation. Phase 2 decision made with data, not projections.
Deliverable: Phase 1 dataset + Phase 2 recommendation. Fund it, modify it, or stop.
Beyond the Kitchen
142,000,000
cubic meters of MgCl₂-rich brine.
Produced every day by desalination plants.
Almost all of it is dumped into the ocean.
Phase 3+ Aspiration — Product 6
Sustainable Electrolyte Recovery System

The DeltaV electrolyte prep skid — developed and proven in Track B — adapted for desalination brine feedstock. A second product line. A second revenue stream.

Partner candidates: Tampa Bay Desal (25M gal/day) · Carlsbad Desal (50M gal/day, Poseidon Water)

The thesis: Sell the recovery system. Take a royalty on the recovered mineral salt. The electrolyte is waste. The waste is free.

The Integration
How it fits inside a desalination plant.

The brine isn’t stored. It flows continuously to the ocean — a river of raw material that nobody captures. The recovery skid taps a sidestream from the discharge pipeline. No disruption to plant operations.

🌊
Ocean Intake
Carlsbad: 50M gal/day
Tampa Bay: 44M gal/day
🏭
Reverse Osmosis Plant
Membranes separate
freshwater from brine
3 kWh/m³
Freshwater → City
25M gal/day drinking water
Brine → Ocean Outfall
25M gal/day · 2× salinity
~470 tons MgCl₂/day dumped
↓ The intervention point ↓
Brine Sidestream
1–5% of discharge
tapped before outfall
Emerson Product 6
Sustainable Electrolyte Recovery System
3–5 modular DeltaV skids per plant
Rosemount 228 + 372 + Micro Motion ELITE
Ion exchange → selective precipitation → recrystallization
Same process proven in Track B at Shakopee
Battery-Grade MgCl₂
4.7 tons/day (at 1%)
~1,700 tons/year
Recovered Cu, Ca, K
Resale value or reuse
Clean Brine → Ocean
Lower mineral load
THE CIRCULAR ECONOMY
🌊
Seawater
Desalinated into
drinking water
🧂
Brine Waste
MgCl₂ recovered
by Emerson skid
🔋
Battery
Stores solar energy
in salt electrolyte
☀️
Powers the Plant
Discharges overnight
to run desal 24/7

The waste from making water becomes the battery that powers the water plant.

470
tons MgCl₂ / day
Tampa Bay alone. Dumped.
3–5
modular skids / plant
Sidestream. No disruption.
$0
feedstock cost
The brine is waste. Waste is free.

Saudi Arabia has committed $65M to industrial-scale brine mineral extraction at Ras Al Khair. US DOE funding targets lithium recovery — high-value at $15–$20/kg. Nobody recovers MgCl₂ because at $0.40/kg, the economics don’t justify it. Unless you have a battery that turns $0.40 salt into $32/kWh energy storage. That changes the math entirely.

What Salt Can Do
The lithium supply chain runs through
the Atacama Desert, the Congo,
and the South China Sea.
The salt supply chain runs through
New Mexico, Arizona,
and the Netherlands.
Lithium-ion cycle life
3,000–5,000
Aqueous cycle life
120,000
Lithium-ion cost
$130–$150/kWh
Aqueous cost
$32–$64/kWh
Lithium-ion fire risk
Thermal runaway
Aqueous fire risk
None. It's salt water.

Salt, water, iron, and copper trade on every continent.
No nation needs to ask permission to store its own energy.

Emerson has spent 136 years building the instruments that measure and control industrial processes.

The question has always been:
what do we measure next?

The answer is the most important electrochemical reaction of the 21st century.

And it happens in salt water.

The same salt water Emerson has been measuring in every refinery, every food plant, every water treatment facility — for decades.

The Ask

We know what to build. We know what to buy. We know who to hire. We know what to measure and when to stop.

Build the lab. Answer the question.

PHASE 1 INVESTMENT
$1.0M – $1.8M
A 2,500-square-foot lab, five people, twelve months. One question: does the chemistry hold at grid scale?
Equipment
NI cycler, EIS, glovebox,
DeltaV skid, env. chamber
Materials
$28K/year. Nedmag +
Intrepid Potash feedstock
People
2 electrochemists, 1 DeltaV,
1 NI test, 1–2 technicians
IP & Counsel
Freedom-to-operate analysis,
CityU tech transfer outreach

The asymmetry: If Month 6 kills it, we’ve spent a fraction of the budget and we have a definitive answer. If Month 6 confirms it, Emerson owns the industrial process for permanent grid storage before anyone else gets to the starting line.

A detailed technical proposal is available for full review.

Emerson Electric · Shakopee, Minnesota

The Salt Frontier.

Edison didn’t invent electricity. He gave it a filament.
Bell didn’t invent sound. He gave it a wire.

The chemistry already exists.
Who gives it a factory?

Connor Scanlan · Material Attendant · Shakopee · 2026