An ECOICE Initiative
Project BioUrea™
A proprietary ETHANABER™ process to end India's dependence on imported fossil gas for fertilizer — turning sugarcane into green urea, with a closed carbon loop.
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Project BioUrea™ — ETHANABER™ Complex
An ECOICE Initiative · ETHANABER™ Proprietary Process

India’s food grows on urea made from imported fossil gas.
We make it from green ethanol.

Almost every bag of urea on Indian farms is made from LNG — fossil gas shipped in from abroad. We want to change that. We make the very same urea from green ethanol, made by India’s own sugar mills and distilleries. Same fertiliser for the farmer. No fossil gas. No imports. A fully sustainable India — starting from the soil. We call it ETHANABER™.

B-Heavy Molasses Route
Also Runs on Grain Ethanol
Zero fossil feedstock
Three plants you can order today — what each costs, makes and returns
Profit figures assume your own ethanol at ₹52/L and ethyl acetate selling at ₹120/kg. The full-scale cost is an early estimate (±50%). Final scope and price are confirmed when you order.
Today

India’s urea is made from imported LNG

Source
Natural gas. India’s own fields supply about one-third. The other two-thirds is LNG, shipped in mainly from West Asia.
Quantity
Urea plants need 46–50 MMSCMD of gas. India produces 14–17.
Impact
₹1.19 lakh crore of urea subsidy a year. Every $1/mmBtu rise in LNG adds ₹2,800 crore. Fossil carbon in every bag.
→
Tomorrow

It is made from India’s own ethanol

Source
Ethanol from sugarcane and grain, converted at the mill or distillery by the ETHANABER™ process.
Quantity
One 60 KLPD complex makes 6,108 t of BioUrea™ a year — enough for 40,720 acres, 1.45× the cane land that feeds it.
Impact
No imported gas. About 65,000 t CO₂e avoided a year per complex. The value stays with the mill and its farmers.
Crop to ethanol to fertilizer, and back to the crop. The same loop works wherever ethanol is made — which is how farming becomes truly sustainable, in India first and then worldwide.
The Problem

India makes its own urea. But not its own gas.

Urea is made from hydrogen. Today that hydrogen comes from natural gas, and most of that gas is imported. So when gas prices jump anywhere in the world, the cost of feeding India jumps with them. That one fact causes five problems.

01
We import energy to grow our food. 70–80% of the cost of making urea is natural gas. India's own gas covers only about a third of what the fertilizer plants need. The rest comes by ship. So India's food depends on other countries' gas.
02
The government pays a huge bill it cannot predict. The fertilizer subsidy is about ₹1.7 lakh crore a year. Urea alone is about ₹1.2 lakh crore. Every time world gas prices rise, the Government of India pays more.
03
Fertilizer is made far from the farm. A few very large gas plants make it. It then travels thousands of kilometres to reach the field. The jobs and the profit stay in industrial cities, not in the villages.
04
It pollutes, and it has to. Making hydrogen from natural gas (steam methane reforming) releases a lot of carbon dioxide, and the heat for it also comes from fossil fuel. That is how the process works. It cannot be cleaned up without changing where the hydrogen comes from.
05
Our ethanol stops at petrol. India has built a big ethanol industry through the Ethanol Blending Programme. But ethanol can do far more than burn in an engine. Today almost none of that extra value is captured.
The Answer

Green urea from green ethanol

Our process takes ethanol and splits it into two things: ethyl acetate, a solvent that sells well, and hydrogen. The hydrogen becomes ammonia. The ammonia, joined with the CO₂ from fermentation, becomes BioUrea™. It is the same fertilizer the farmer already uses. Only the starting point is different. This is India's first integrated renewable nitrogen platform.

01
Bioethanol
↓
02
ETHANABER™ Catalytic Dehydrogenation
↓
03
Renewable Hydrogen
↓
04
Haber-Bosch
↓
05
Renewable Ammonia
↓
06
BioUrea™
↓
07
Circular Agriculture
What makes this different: we do not build a new fertilizer factory somewhere far away. We add this to a sugar mill or distillery that already exists. The same cane then gives ethyl acetate, hydrogen, ammonia, BioUrea™, food-grade CO₂, steam and electricity — all renewable. Nothing becomes waste. Everything becomes a product.
In one line: every sugar mill and distillery can become a green fertilizer plant — run on its own ethanol, its own CO₂ and its own bagasse energy. Less imported gas for India. More value for farmers, industry and villages.
Who Wins

Good for the farmer, the mill, the country and the air

The Farmer

Fertilizer made nearby, from the farmer's own cane. A steadier supply. And in a cooperative mill the farmers are the owners — so the profit from fertilizer comes back to them.

The Mill or Distillery

More products from the same cane. More income for the mill and its village. Sugar and ethanol are no longer the only earners, and less depends on imported LNG.

India

Less imported energy. More value added at home. Fertilizer that keeps flowing even in a world crisis. This is Atmanirbhar Bharat and the bioeconomy, in practice.

The Air

Hydrogen from a crop, not from gas. The CO₂ from fermentation is used, not released. Steam and power come from bagasse. About 65,000 tCO₂e avoided every year, per complex.

What your order builds for India

Each plant is one more step off imported gas.

The money stays with the farmer

India spends about ₹1.19 lakh crore a year in subsidy on urea made from imported, price-swinging gas. Fertilizer made at the mill keeps that value with the mill and its farmers.

Farming free of fossil carbon

Urea made from crop ethanol, not fossil gas. From the field, back to the field.

Freedom from world shocks

No war, shipping strait or LNG price decides what Indian food costs.

A fossil-free supply chain

Green ethyl acetate, green hydrogen and green ammonia give industry inputs with no fossil gas behind them.

Step 1 proves it.Step 2 puts green ethyl acetate and green hydrogen on the market.Step 3 makes green urea and leads the switch.
In Numbers

One mill. Five green products. Zero fossil gas.

This is what one 60 KLPD complex makes in a year. Each number has a short note on why it matters.

0t/yr
Renewable Ethyl Acetate
The main earner — 84% of revenue. Made from ethanol alone, without a drop of acetic acid.
0t/yr
Green Hydrogen
It comes with the ethyl acetate — nobody has to buy it. This hydrogen is what makes the fertilizer possible.
0t/yr
Green Ammonia
Made the usual way (Haber-Bosch), like any ammonia. But the hydrogen came from cane, not gas.
0t/yr
BioUrea™ (46% N)
Exactly the same as normal urea. The farmer sees no difference. The country does.
0t/yr
Sugar Co-Produced
The mill keeps making sugar. That business can be even bigger than the chemicals.

There's a different way to grow nitrogen.

Project BioUrea™ turns sugarcane into ethyl acetate, green hydrogen, green ammonia and green urea. No natural gas. No imported LNG. No acetic acid. Here is why that matters.

The Grave Reality, Today

A war 3,000 km away can change the cost of feeding a billion people.

Every tonne of Indian urea starts with hydrogen made from natural gas, and two-thirds of that gas is imported. When one shipping route through the Strait of Hormuz is disturbed, the cost of feeding India moves within weeks. No drought. No crop failure. Nothing changes on the farm. And still, fertilizer prices nearly triple.

India's Urea Subsidy, FY26
India's biggest single subsidy. And it rises and falls with a market India does not control.
What Government Absorbs, Per Tonne
₹20,000–61,000per tonne
The farmer always pays ₹5,360. The government pays the rest. That gap is large in a calm year and much larger in a crisis.
Domestic Gas Meets
~33% of demand
India's 30 gas-based urea plants need 46–50 MMSCMD of gas. India's own fields give only 14–17. The rest is imported, at a higher price.
The Four Numbers That Matter

What one complex is worth

The full working behind each number is under How It Works, Plants & Profit and Why India Needs It.

Total Revenue
₹184.5Cr/yr
Ethyl acetate + BioUrea + CO₂ only. Sugar (₹329–363 Cr) and power export (₹44 Cr) are extra — see Plants & Profit.
Core EBITDA Range
₹19–47Cr/yr
It depends on one choice: buy the ethanol, or use your own. Nothing else matters as much.
Avoided Emissions
Range 53,400–76,800 tCO₂e/yr. Like ~28,000 cars off the road, or 3 million trees planted.
Fertilizer Reach
40,700acres
Green fertilizer for Indian farmland, made from Indian sugarcane, under the Indian sun.
Why B-Heavy

Why B-heavy molasses: sugar and fertilizer, both

We compared three ways of getting ethanol from cane. B-heavy molasses is the balance. The mill still makes plenty of sugar, and still has enough ethanol for the chemicals, at a normal mill size.

RouteL Ethanol / t CaneCane RequiredAcreageSugar Co-ProducedVerdict
C-Heavy Molasses10.81.83M t56,559 ac210,800 tSugar-dominant, mill ~7× larger
B-Heavy Molasses — SELECTED21.75910,345 t28,097 ac86,483 tBalanced — our choice
Full Juice / Syrup84235,714 t7,272 ac0 tNo sugar business at all
Checked twice: the project visuals show 910,000 t cane / ~28,084 acres / 86,500 t sugar / ₹346 Cr revenue for B-heavy. Recalculated separately here: 910,345 t / 28,097 ac / 86,483 t / ₹329–363 Cr — ₹346 Cr sits exactly at the midpoint. The numbers agree to within rounding.

India's food depends on gas it has to import.

Here is what that costs the country, what it means for the farmer, and how much carbon this project takes out.

On this page
The National Stakes

A war 3,000 km away changes the cost of Indian food

These are the Government of India's own budget numbers.

This is the structural problem in one picture: India's gas-based urea plants need 46–50 MMSCMD of natural gas, but domestic production supplies only 14–17 MMSCMD — roughly a third. The rest is imported, which means the price of feeding India is only ever as stable as the shipping route the gas travels on. The infographic below shows what happens to that price when the route isn't stable: LNG more than doubling during the 2026 West Asia crisis, and urea's landed cost following it almost exactly.

Grave reality of fossil-based Indian agriculture
46–50 MMSCMD gas required, only 14–17 MMSCMD domesticClick to zoom ↗
Total Fertilizer Subsidy FY26
Roughly 3% of the entire Union Budget, on one input.
Urea Subsidy Alone
₹1.19lakh Cr
India's single largest direct subsidy line item.
FY23 Crisis Peak
₹2.25lakh Cr
What one bad year in global gas markets costs India.
Domestic Gas Meets
~33% of need
Two-thirds of urea's core feedstock is imported.

Here's the mechanism behind that number, made concrete. The farmer's price at the counter — ₹5,360 per tonne — hasn't moved since March 2018, regardless of what's happening in global gas markets. Every rupee of difference between that fixed price and the real cost of production is absorbed by the government as subsidy. In a stable year that gap is already large; in a crisis year, it more than doubles. The farmer never sees the volatility — the exchequer absorbs all of it.

The real cost of every tonne of urea
Farmer pays ₹5,360/t always — government absorbs the restClick to zoom ↗
ScenarioCost/tonneFarmer PaysSubsidy GapGovt. Absorbs
Normal market₹25,300–28,650₹5,360₹19,950–23,290~80%
Crisis (Apr 2026, West Asia)₹65,300–66,850₹5,360₹59,960–61,490~92%
The single sharpest argument in this whole project: the incremental cost of green, hydrogen-route urea is roughly ₹5,000–25,000/tonne above conventional. India's own subsidy volatility — the swing from ₹19,950 to ₹61,490 per tonne between a calm year and a crisis — is larger than that entire gap. This isn't "green urea is cheap." It's "the volatility India already tolerates is bigger than the cost gap green urea needs to close."

What one plant saves the government

Calm-Year Scenario
6,108t × ~₹20,000–23,000/t subsidy gap
Crisis-Year Scenario
₹36.6–37.5Cr/yr avoided
What one plant would have saved during exactly the crisis India just lived through. Scale to 100 plants: ₹3,500–5,700 Cr/yr.
Agriculture & Circularity

From cane to clean fertilizer — all Indian, all renewable

The whole B-heavy loop from the project visual, checked against this dashboard's own calculation.

This one picture shows the whole loop. Sugarcane comes in. Sugar and B-heavy molasses come out. The molasses is fermented into ethanol. The ethanol goes to the ETHANABER™ and BioUrea™ stages. The CO₂ is captured and used in the urea plant, not released. Every figure on it is checked against the tables below. It is the same route as the spreadsheet, drawn as one story.

Project BioUrea integrated bioeconomy
Sugarcane through CO₂ recovery — B-Heavy Molasses routeClick to zoom ↗
Sugarcane Land
28,097acres
Visual: ~28,084 — matches
Sugar Co-Produced
86,483t/yr
Visual: 86,500 — matches
BioUrea™
6,108t/yr
Visual: 6,105 — matches
Fertilizer Reach
40,700acres
At 150 kg/acre — matches

Application rate — verified for sugarcane

Application RateAcreage FertilizedSource
150 kg/acre/yr40,700 acresMid-range Indian agronomy for cane — matches visual
250 kg/acre/yr24,420 acresHeavier dose for high-yield cane
The vision, stated plainly: today, the nitrogen that grows India's food comes from gas pumped through the Strait of Hormuz. Project BioUrea™ grows it instead from sugarcane rooted in Indian soil — fixing carbon from the atmosphere, closing the loop, and handing the farmer the same product at the same price, with none of the geopolitical fragility. This is what a transition from a fossil agricultural economy to a renewable one actually looks like, one integrated complex at a time.
Carbon Balance

A net-positive carbon story

This is a screening estimate by engineers, not a certified LCA. Every figure comes from the mass and energy balance.

This chart lays out where the carbon avoidance actually comes from — not as one number, but as four separate pathways that each get compared against their fossil equivalent: ethyl acetate against the petrochemical route, hydrogen against steam methane reforming, ammonia and urea against the gas-based process, and biogenic CO₂ utilization against venting it. Adding those four together, with a wide low-to-high range reflecting real uncertainty in emission factors, is how the ~65,000 tCO₂e/yr midpoint figure used throughout this dashboard is built.

Net positive carbon balance
Avoided-emissions pathways & total conceptual impactClick to zoom ↗
Avoided PathwayLowMidHighBasis
Ethyl acetate vs. fossil route26,80034,20041,70014,883t × 1.8–2.8 kgCO₂e/kg
BioUrea™ vs. grey urea11,00015,30019,5006,108t × 1.8–3.2 tCO₂e/t
Steam, bagasse vs. coal—6,250—17,860 MWh × 0.35
Electricity, bagasse vs. grid—4,900—6,869 MWh × 0.71
Subtotal — production only48,90060,60072,300
+ Urea field hydrolysis (biogenic C)+4,5006,108t × 0.733 (IPCC)
Total, all boundaries53,400~65,10076,800
The one caveat that must travel with this: the field-hydrolysis credit is CO₂-only. N₂O from the nitrogen pathway is identical whether urea is fossil or bio-sourced — this project does not reduce field N₂O, and shouldn't be presented as if it does.
≈ Cars off the road
28,000per year
≈ Mature trees planted
3 Mequivalent
≈ Households' power offset
40,000Indian homes

Ethanol goes in. Fertiliser comes out.

Every step, every tonne and every unit of energy is shown here, with nothing hidden.

On this page
Process & Plant

15 steps, in two stages

From splitting the ethanol (ETHANABER™ catalytic dehydrogenation) to finished BioUrea™ prills. Click any diagram to zoom in on a step.

The diagram below is the full ETHANABER™ and BioUrea™ complex, laid out block by block exactly as it would be built. Ethanol comes in on the left; it passes through catalytic dehydrogenation (Block 3, the core proprietary step), separation, and hydrogen purification to yield ethyl acetate and hydrogen. In parallel, fermentation CO₂ and nitrogen feed the ammonia and urea trains along the bottom row, closing the loop from raw biomass to bagged fertilizer. The utilities and offsite facilities strips at the base are the supporting infrastructure every one of those blocks depends on — steam, cooling water, DM water, and the workshop, warehouse and control room that keep the plant running day to day.

ETHANABER Process and BioUrea Complex
Full complex — 15 process blocks, utilities & offsite facilitiesClick to zoom ↗

Block 3 — Catalytic Dehydrogenation

The core innovation

Fixed-bed tubular reactor, copper / copper-chromite catalyst. 240–270°C, 10–20 bar, 1–3 sec residence. Converts ethanol directly to ethyl acetate + hydrogen. No acetic acid in the reaction at all.

Block 6 — Hydrogen Purification

PSA to 99.99%

Pressure swing adsorption, dryer, buffer vessel. Nameplate 2.05 TPD (677 t/yr gross). This dashboard uses the PSA-corrected 647 t/yr net figure downstream — 95% recovery, applied consistently.

Block 13 — BioUrea™ Plant

Ammonia + CO₂ → Urea

HP reactor, carbamate condenser + stripper, decomposer, evaporator, vacuum concentrator, prilling. Output 46% N BioUrea™, identical spec to conventional urea — drop-in for the farmer.

Equipment & materials

What it takes to build it

This second diagram shows what has to be built: the equipment in each stage, the utilities they share, and the metals used (carbon steel, stainless, duplex, alloy). The choice of metal decides both the cost and how well the plant resists corrosion. Read it together with the cost table below to see where the money goes.

BioUrea equipment and material distribution
Stage 1 & 2 equipment, common utilities, material distributionClick to zoom ↗

Equipment cost, section by section

An early, rough estimate (Class 5, ±50%), built from standard sizing rules on our own mass balance. Vendor quotes are needed before financing.

SectionFab. SteelKey equipment
1. ETHANABER reactor train40.3 tDehydrogenation reactors (×2), Cu-Cr catalyst
2. Separation / distillation77.4 tRecycle + purification columns (azeotrope duty)
3. Hydrogen purification—PSA package + H₂ compressor to 150–200 bar
4. Ammonia synthesis89.5 tSyngas compressor, Fe-catalyst converter, ASU
5. Urea synthesis & finishing57.9 tTi-clad reactor + stripper, granulator
6. CO₂ recovery & liquefaction62.6 tScrubber, compressor, food-grade bottling
7. Storage & utilities163.2 tTankage, cooling tower, DCS/PLC
Total Purchased Equipment490.8 t₹31.11 Cr
Total Installed (Lang 3.5–4.5×)~1,915–2,514 tincl. structural + piping steel — cost pending vendor quotes
Carbon Steel
~55%
Stainless 304/316
Duplex / Ti-Clad
~8%
Alloy / Cr-Mo
~5%
Why 8% of the steel drives the cost: the urea reactor and stripper need duplex/titanium-clad steel because ammonium carbamate is brutally corrosive — just 29 tonnes of steel costing ₹2.80 Cr, roughly 10× the ₹/tonne of the plain carbon-steel storage tanks. Any estimate that ignores this metallurgy will under-price the plant.
Feedstock Flexibility

Not a sugarcane platform. An ethanol platform.

Some people think this only works for sugar mills. It works for any distillery. ETHANABER™ runs on purified ethanol, whatever that ethanol was made from. Sugarcane is our base case — and today most of India's ethanol actually comes from grain.

Grain's share of India's ethanol supply, ESY 2025–26
70%
624 of 895 crore litres supplied to oil companies came from grain — not sugarcane.
Maize alone beats all sugar routes combined
345 vs 271crore L
Maize alone, vs. all sugarcane routes (juice + B-heavy + C-heavy) combined.

Where India's ethanol actually comes from

Through August 2026, Ethanol Supply Year 2025–26.

FeedstockSupplyShare
Maize345 crore L38.5%
Surplus FCI rice214 crore L23.9%
Damaged food grains64 crore L7.2%
Sugarcane juice149 crore L16.6%
B-heavy molasses107 crore L12.0%
C-heavy molasses15 crore L1.7%

Same platform, same base plant, either feedstock

Recomputed for a grain-fed version of the base 60 KLPD ETHANABER™ plant (15,622 t/yr ethanol) used throughout this dashboard.

Cane B-HeavyCane Direct JuiceMaize (Grain)Surplus Rice (Grain)
Yield per tonne feedstock21.75 L70–84 L380 L440–450 L
Feedstock required910,345 t/yr235,714 t/yr52,105 t/yr44,494 t/yr
Land required28,097 acres7,272 acres~37,760 acres— (FCI stock)
Ethanol yield / acre~715 L~2,300 L~524 L—
Admin. price, ESY25–26₹60.73/L₹65.61/L₹71.86/L₹60.32/L
Distinct co-productSugar (86,500 t/yr)NoneDDGS (~14,300 t/yr)DDGS

The circular model — cane first, grain too

The loop closes on either feedstock: the crop makes the ethanol, the ethanol makes the BioUrea™, and the BioUrea™ goes back onto the land that grew the crop. Base 60 KLPD plant.

Circular loopSugarcane (B-Heavy)Maize (Grain)
Crop in910,345 t/yr52,105 t/yr
Land growing it28,097 acres~37,760 acres
Food / feed co-productSugar 86,483 t/yrDDGS ~14,300 t/yr
BioUrea™ back out6,108 t/yr6,108 t/yr
Land fertilised at 150 kg/acre40,700 acres40,700 acres
Fertiliser made vs. own land1.45×1.08× cane dose basis
Cane is the stronger loop: a cane complex fertilises its whole catchment and still has ~12,600 acres of BioUrea™ to spare, and it keeps a full sugar business alongside. A maize distillery just about covers its own acreage and adds DDGS as animal feed. The maize figure uses the same 150 kg/acre dose verified here for cane — maize-specific dosing is not separately verified.
The honest cost picture: at the administered/open-market price, maize ethanol (₹71.86/L) is actually the most expensive feedstock option here — pricier than any sugarcane route. But forward-integrated with a maize distillery's own cost (₹53–63/L gross, before DDGS credit) rather than the administered price, and crediting DDGS (estimated ~₹14–15/L at an assumed ₹20/kg DDGS price — not independently sourced, needs verification), effective ethanol cost falls to roughly ₹38–49/L — competitive with, and potentially better than, forward-integrated cane.
Why this matters: grain distilleries are concentrated in Punjab, Haryana, Bihar, Madhya Pradesh and Maharashtra — a materially different geography than the cane belt. This platform's addressable market isn't just "sugar mills in the cane belt." It's every distillery in India producing purified ethanol, from any feedstock, anywhere.
Mass Balance

Four reactions run the whole complex

Each number follows from the chemistry of the step before it. None of it is a market guess. Molar masses: ethanol 46.07, EtAc 88.11, H₂ 2.016, CO₂ 44.01, NH₃ 17.03, urea 60.06.

1 · Fermentation (existing distillery)C₆H₁₂O₆ → 2 C₂H₅OH + 2 CO₂
2 · ETHANABER™ dehydrogenative coupling2 C₂H₅OH → CH₃COOC₂H₅ + 2 H₂
3 · Haber-Bosch synthesisN₂ + 3 H₂ → 2 NH₃
4 · Urea synthesis2 NH₃ + CO₂ → CO(NH₂)₂ + H₂O
No acetic acid, anywhere. ETHANABER is direct dehydrogenative coupling — conventional ethyl acetate plants esterify acetic acid + ethanol. That one difference means zero exposure to acetic acid pricing, and it's why this route needs roughly double the ethanol per tonne of product (half the ethanol becomes hydrogen, not ethyl acetate) — which is exactly what makes the downstream green hydrogen → ammonia → urea chain possible.

B-Heavy chain — cane to ethanol

StreamValueCalculationStatus
Sugarcane crushed910,345 t/yr19.8M L ÷ 21.75 L/t caneCross-checked
Sugar co-produced86,483 t/yr910,345 × 95 kg/t caneCross-checked
Ethanol plant capacity15,622 t/yr60,000 L/d × 0.789 × 330 d330-day basis
Cane acreage required28,097 ac910,345 ÷ 32.4 t/acreCross-checked
Nameplate vs. operating days: the P&ID states "21,900 KLPY" (60 KLPD × 365 calendar days). This dashboard uses 330 operating days throughout (~90% uptime), giving 19,800 KLPY / 15,622 t/yr. Both are valid — just never mix them in one calculation.

ETHANABER™ → BioUrea™ — the full chain

StreamValueCalculationvs. Visual
Ethyl acetate14,883 t/yr50,000 L/d × 0.902 × 330 dMatches exactly
Ethanol required15,881 t/yr14,883 × (2×46.07÷88.11) ÷ 0.98259 t/yr (1.7%) above distillery capacity
Hydrogen, gross681 t/yr14,883 × (2×2.016÷88.11)Visual: 677 t / 2.05 TPD — matches
Hydrogen, usable647 t/yr681 × 95% PSA recoveryPSA loss applied
Fermentation CO₂, recovered13,431 t/yr14,923 gross × 90% captureCapture eff. applied
Green ammonia3,534 t/yr647 × (2×17.03÷3×2.016) × 0.97Visual: 11.6 TPD — uses gross H₂
BioUrea™6,108 t/yr3,534 × (60.06÷2×17.03) × 0.98Visual: 6,105 t — matches
CO₂ to urea4,567 t/yr3,534 × (44.01÷2×17.03)—
CO₂ surplus (food grade / dry ice)8,864 t/yr13,431 − 4,567Visual: 9,940 — likely omits capture eff.

Circularity — it grows more than it consumes

01
Cane land
28,097 ac
→
02
Ethanol
15,622 t
→
03
Ethyl Acetate
14,883 t
→
04
Hydrogen
647 t
→
05
Ammonia
3,534 t
→
06
BioUrea™
6,108 t
→
07
Fertilizes
40,700 ac
Verified against real agronomy: at 150 kg urea/acre/yr — independently confirmed against Indian sources citing 130–200 kg/acre specifically for sugarcane — 6,108 t of BioUrea™ feeds 40,700 acres. That's the crop this project is built around, not a generic figure. At 250 kg/acre for high-yield cane, reach is 24,420 acres — both figures shown in your visuals.
Energy Balance

Powered entirely by the cane's own bagasse

No coal. No dependence on the grid for the main process. The bagasse the mill already has runs everything.

ConsumerBasisMWh/yr
Ethyl acetate — thermal (steam)14,883 t × 1,200 kWh-th/t17,860
Ethyl acetate — electrical14,883 t × 150 kWh-e/t2,232
Ammonia loop + ASU3,534 t × 750 kWh-e/t2,651
Urea granulation6,108 t × 180 kWh-e/t1,099
CO₂ liquefaction8,864 t × 100 kWh-e/t886
Total thermal demand17,860
Total electrical demand6,869

Is the bagasse enough?

Total bagasse energy pool

From 910,345 t/yr cane (B-heavy)

910,345 t × 29% yield = 264,000 t bagasse/yr. At 7.37 GJ/t and 80% boiler efficiency:

~431,900MWh-th/yr

New cascade needs

Thermal + electrical combined

The whole ETHANABER + ammonia + urea + CO₂ cascade, together:

24,729MWh/yr
Just 5.7% of the gross bagasse pool.
Honest flag: the gross pool comfortably exceeds the cascade's needs — roughly 17× headroom before the existing mill takes its share. But the existing sugar mill and distillery draw on that same bagasse first, and their exact steam consumption at this specific site has never been provided. The sufficiency conclusion is directionally strong but needs the mill's real boiler data to confirm, not an assumption.

Net energy position

New Cascade Demand
24,729MWh/yr
Gross Bagasse Pool
431,900MWh-th/yr
Headroom Before Mill Draw
17×demand covered

Three plant sizes. Pick the one that fits you.

Start small to see it work. Run a selling plant inside your distillery. Or build the full complex. The price, products and profit of each are below.

On this page
Pick a Plant

Test it. Run it. Lead the market.

It is the same ETHANABER™ process at three sizes. Read the three cards, pick the one that fits you, and press its button to order.

⚡ Pilot-scale kinetics already completed ⚡ 50 KLPD plant ~50% built at an MIDC site = 9-month market lead for early partners
01 · Test it · Proof of Concept

Pilot Plant

100 L/day
Makes: ethyl acetate + green hydrogen
Plant cost
~₹35 lakh indicative
Return: proof and data for your decision. Not built for payback.
  • See it work on your own ethanol, cane or grain, before you spend big.
  • Makes about 30 t ethyl acetate and 1.35 t green hydrogen a year.
  • Gives you the real numbers — yield, catalyst life, utilities — for your big decision.
  • It is a test unit. It is not meant to earn back its cost.
  • Your part: you prove, on your own ethanol, that green chemistry works.
02 · Run it · Semi-Commercial Demo

Semi-Commercial Plant

1,000 L/day
Makes: ethyl acetate + green hydrogen
Plant cost
₹1.5 Cr equipment quote
Return: ~₹1.2 Cr profit a year · pays back in ~1.2 years
  • A real, selling plant inside your distillery. It uses your steam, your ethanol and your crew.
  • Makes about 298 t ethyl acetate and 13.5 t green hydrogen a year.
  • Earns about ₹1.2 Cr a year on your own ethanol. Pays for itself in about 1.2 years.
  • Proves the business — running, selling, margins — before you build big.
  • Your part: you put green ethyl acetate and green hydrogen on the Indian market.
Steps 1 and 2Ethyl acetate + green hydrogenNo urea section. The hydrogen is sold as hydrogen. Quick to build, quick to earn.
Step 3 · the full complexEthyl acetate + BioUrea™Adds the ammonia and urea section, so the hydrogen becomes fertilizer. The full profit and loss further down is for this urea complex. The 50 KLPD plant now being built is its first stage, the ethyl acetate plant.
Specifications

What each plant is, and what it makes

100 L Pilot1,000 L Semi-Commercial60 KLPD Full Scale
RoleProof of conceptScale-up demo, first salesCommercial complex
Ethanol feed132 L/day1,316 L/day60,000 L/day
Ethyl acetate100 L/day (90 kg)1,000 L/day (902 kg)45,580 L/day (41.1 t)
Green hydrogen4.1 kg/day41 kg/day1,869 kg/day
Ethyl acetate per year29.8 t298 t13,568 t
Hydrogen per year1.35 t (15,150 Nm³)13.5 t (1.52 lakh Nm³)617 t (69 lakh Nm³)
Byproduct per year3.5 t34.6 t1,576 t
Ammonia per year——3,367 t
BioUrea™ per year——5,822 t
Conversion cost / kg ethyl acetate~₹40 estimate~₹15~₹9
Investment~₹35 lakh₹1.5 Cr~₹34 Cr
Why conversion cost falls with size: the chemistry itself costs about ₹6–9 per kg at every scale — steam, power, catalyst, water. What changes is the crew: a fixed operating team spread over 90 kg a day costs about 15× more per kg than the same team spread over 41 tonnes a day.
Conservative case vs. design basis: this tab holds all three scales to 90% selectivity. The plant design mass balance used elsewhere in this dashboard gives slightly more from the same 60 KLPD — 14,883 t ethyl acetate, 647 t hydrogen and 6,108 t BioUrea™ a year.
Products & Profit

Where the money comes from, product by product

Profit per year from running the plant. Ethyl acetate carries the whole cost of ethanol and conversion. Hydrogen and byproduct are extra income on top.

Own ethanol at ₹52/L100 L Pilot1,000 L Semi-Commercial60 KLPD Full Scale
Ethyl acetate₹1.2 lakh₹86.7 lakh₹47.6 Cr
Byproduct₹2.4 lakh₹24.2 lakh₹11.0 Cr
Green hydrogen (sold)₹1.1 lakh₹10.9 lakh₹5.0 Cr
Total operating profit₹4.7 lakh₹1.22 Cr₹63.6 Cr
Simple payback7.4 years1.2 years0.5 years
Hydrogen turned into BioUrea™ instead——₹6.4 Cr (+₹1.5 Cr)
Bought ethanol at ₹70/L100 L Pilot1,000 L Semi-Commercial60 KLPD Full Scale
Ethyl acetate−₹6.6 lakh₹8.5 lakh₹12.0 Cr
Byproduct₹2.4 lakh₹24.2 lakh₹11.0 Cr
Green hydrogen (sold)₹1.1 lakh₹10.9 lakh₹5.0 Cr
Total operating profit−₹3.1 lakh₹43.6 lakh₹28.0 Cr
Simple paybacknone3.5 years1.2 years
Read these with two cautions: the byproduct is valued at ₹70/kg and its buyer is not yet confirmed — at fuel value the totals fall by the byproduct line. And everything moves with the ethyl acetate price: the table below shows how far it can fall before a 5-year payback is lost.
5-Year Payback Lock

The prices that keep payback under 5 years

If ethyl acetate sells at or above the price shown, the plant pays for itself in 5 years or less.

Ethanol price100 L Pilot needs1,000 L Semi needs60 KLPD Full needs
₹45/L₹117/kg₹79/kg₹67/kg
₹52/L (own ethanol)₹128/kg₹89/kg₹77/kg
₹60/L₹139/kg₹101/kg₹89/kg
₹70/L (bought)₹154/kg₹115/kg₹103/kg
Highest ethanol price at ₹120/kg ethyl acetate₹47/L₹73/L₹81/L
What this says: every ₹1/L on ethanol moves the ethyl acetate price you need by about ₹1.46/kg, at every scale — so owning the ethanol matters more than anything else. Full scale holds a 5-year payback even on bought ethanol; the semi-commercial plant holds it on own ethanol with wide room to spare; the pilot is a proof unit and is not bought for payback.
Payback At Every Price

Years to earn back the plant, at each price pair

Find your ethanol price on the left and the ethyl acetate price on top. Green means the plant pays for itself in 5 years or less.

1,000 L/day Semi-Commercial · ethyl acetate + hydrogen · ₹1.5 Cr
Ethyl acetate price →₹80₹90₹100₹110₹120
Ethanol ₹45/L4.5 yr2.4 yr1.6 yr1.2 yr1.0 yr
Ethanol ₹52/L56 yr4.6 yr2.4 yr1.6 yr1.2 yr
Ethanol ₹60/Llossloss5.5 yr2.6 yr1.7 yr
Ethanol ₹70/Llosslossloss10.9 yr3.5 yr
60 KLPD Full Scale · ethyl acetate + BioUrea™ · ~₹34 Cr
Ethyl acetate price →₹80₹90₹100₹110₹120
Ethanol ₹45/L1.4 yr0.9 yr0.7 yr0.5 yr0.4 yr
Ethanol ₹52/L3.1 yr1.4 yr0.9 yr0.7 yr0.5 yr
Ethanol ₹60/Lloss4.0 yr1.5 yr1.0 yr0.7 yr
Ethanol ₹70/Llossloss14.6 yr2.1 yr1.2 yr
5 years or lessmore than 5 yearsruns at a loss
How to read this: on its own ethanol (₹52/L or less) the full complex pays back within 5 years at every ethyl acetate price shown, and the semi-commercial plant does from ₹90/kg up. On bought ethanol at ₹70/L both need ethyl acetate near ₹110–120/kg. Inside a distillery, with its own ethanol, steam and crew, the conversion cost stays near ₹9–15 per kg and the margin is wide. No plant is free of risk: the two prices in this table are the ones to lock in before you build.
Feedstock Behind Each Plant

What it takes from the field — cane first, grain too

Sugarcane on the B-heavy molasses route is the base case. Maize is shown as the grain alternative for the same ethanol.

100 L Pilot1,000 L Semi-Commercial60 KLPD Full Scale
Ethanol used per year43,400 L4.34 lakh L198 lakh L
Sugarcane crushed (B-heavy)1,997 t19,971 t910,345 t
Cane land62 acres616 acres28,097 acres
Sugar still produced190 t1,897 t86,483 t
Or maize (grain)114 t1,143 t52,105 t
Maize land83 acres829 acres~37,760 acres
DDGS feed co-product31 t314 t~14,300 t
BioUrea™ back to the land (150 kg/acre)——38,800 acres
The loop closes at full scale: the BioUrea™ from one complex fertilises about 38,800 acres — 1.38× the cane land that feeds it, or roughly the whole maize acreage on the grain route (1.03×). The crop makes the ethanol, the ethanol makes the fertiliser, and the fertiliser goes back to the crop. At the pilot and semi-commercial sizes the hydrogen is sold as hydrogen; the urea section is added at full scale.
What your order builds for India

Each plant is one more step off imported gas.

The money stays with the farmer

India spends about ₹1.19 lakh crore a year in subsidy on urea made from imported, price-swinging gas. Fertilizer made at the mill keeps that value with the mill and its farmers.

Farming free of fossil carbon

Urea made from crop ethanol, not fossil gas. From the field, back to the field.

Freedom from world shocks

No war, shipping strait or LNG price decides what Indian food costs.

A fossil-free supply chain

Green ethyl acetate, green hydrogen and green ammonia give industry inputs with no fossil gas behind them.

Step 1 proves it.Step 2 puts green ethyl acetate and green hydrogen on the market.Step 3 makes green urea and leads the switch.
Place Your Order

Tell us which plant. We do the rest.

Fill this in and press the button. That places your order request. ECOICE then confirms the scope, final price and delivery date with you. You pay nothing until that is agreed.

Economics

Full-scale profit and loss, every line shown

Switch between buying ethanol and using your own. That one choice changes the result more than anything else. Figures below use cane-route ethanol pricing (₹65/L open-market, ₹52/L forward-integrated). Grain-route ethanol runs the same chemistry at different feedstock economics — see Cane or grain under How It Works.

Ethyl Acetate
₹3.1Cr
2.0% margin — razor thin
BioUrea™
₹10.4–12.9Cr
46–57% margin
CO₂ Bottling
₹5.9Cr
~83% margin
Core EBITDA Total
₹19–21Cr
on ₹184.5 Cr revenue
Ethyl Acetate
₹29.3Cr
18.9% margin
BioUrea™
₹10.4–12.9Cr
Unchanged
CO₂ Bottling
₹5.9Cr
Unchanged
Core EBITDA Total
₹45–47Cr
on ₹184.5 Cr revenue

Ethyl acetate — full cost build-up

LineCalculationOpen MarketFwd-Integrated
Revenue14,883t × ₹104,000₹154.8 Cr₹154.8 Cr
Ethanol feedstock20.13M L × price₹130.8 Cr₹104.7 Cr
Utilitiessteam + power₹3.8 Cr₹3.8 Cr
Opex (11% of rev)catalyst+labour+maint₹17.0 Cr₹17.0 Cr
EBITDA₹3.1 Cr (2.0%)₹29.3 Cr (18.9%)
Break-even selling price: ₹101.7/kg on open-market ethanol (2.3% cushion) vs. ₹81.9/kg forward-integrated (real cushion). Sensitivity: ₹1/kg EtAc price ≈ ₹1.33 Cr EBITDA; ₹1/L ethanol ≈ ₹2.01 Cr. Ethanol sourcing is worth a ₹26 Cr/yr swing on this one product alone.

BioUrea™ — full running cost

ItemConservativeAdjustedNote
Electricity₹2.62 Cr₹2.62 CrNH₃ loop + granulation, rebuilt
Labour₹1.60 Cr₹1.07 Cr⅓ shared with EtAc crew
Packaging₹1.50 Cr₹0.38 CrBulk vs. retail bagging
Maintenance₹1.30 Cr₹0.87 CrShared overhead
Steam₹1.20 Cr₹1.20 Cr
Nitrogen (ASU)₹1.11 Cr₹1.11 Cr
Carbon Dioxide₹0.91 Cr₹0.91 CrCorrected from a 10× error
Administration₹0.80 Cr₹0.53 Cr
Chemicals₹0.60 Cr₹0.45 CrCatalyst line stripped
Cooling + DM water₹0.60 Cr₹0.60 Cr
Total OPEX₹12.25 Cr₹9.74 Cr
EBITDA (Rev ₹22.6 Cr)₹10.4 Cr (46%)₹12.9 Cr (57%)
The honest structure: BioUrea is profitable because hydrogen is genuinely free — a byproduct of a reaction run anyway for ethyl acetate. Charge hydrogen at its ₹300/kg replacement value and the urea unit would lose ₹10.5 Cr/yr standalone. That's not a weakness; it's the whole point of integration. Urea contributes ~69% of core EBITDA despite being a fraction of revenue.

BioUrea™ at real market prices — farmer price plus subsidy

Everything above prices BioUrea™ at a flat ₹37,000/t "equivalent value." But if BioUrea™ is sold into the same system as conventional urea, its true realized revenue is farmer MRP + government subsidy — the full amount a urea producer actually receives, which moves with global gas prices exactly as shown under Why India Needs It. Here's what that does to the numbers.

ScenarioRealized Price/tBioUrea™ RevenueOPEXBioUrea™ EBITDA
Normal market (worst case)₹25,300–28,650₹15.5–17.5 Cr₹12.25 Cr₹3.2 Cr
Crisis market (best case)₹65,300–66,850₹39.9–40.8 Cr₹9.74 Cr₹31.1 Cr

Ethyl acetate + BioUrea™ — combined profit, worst & best case

Worst Case — Open-Market Ethanol + Normal Urea Market
₹6.3Cr EBITDA
EtAc ₹3.1 Cr + BioUrea™ ₹3.2 Cr, on ₹170.3 Cr combined revenue — a 3.7% margin. The floor case if nothing goes your way.
Best Case — Forward-Integrated Ethanol + Crisis Urea Market
₹60.4Cr EBITDA
EtAc ₹29.3 Cr + BioUrea™ ₹31.1 Cr, on ₹195.6 Cr combined revenue — a 30.9% margin. Both levers moving favorably at once.
The honest range is wide, and that's the point: ₹6.3–60.4 Cr is nearly a 10× spread on the same two products. It isn't model uncertainty — it's two real, external variables (ethanol sourcing and the global gas cycle) that this project doesn't control but is directly exposed to in both directions.

Sugar, CO₂ & power — the three upside lines

Sugar Co-Product (B-Heavy)
₹329–363Cr/yr revenue
86,483 t/yr at ₹38–42k/t. Belongs to the existing mill's economics, not modeled here — but potentially larger than the entire chemicals platform.
CO₂ Bottling (Food Grade / Dry Ice)
₹7.1Cr/yr revenue
8,864 t/yr at ₹8,000/t, ~₹5.9 Cr EBITDA at ~83% margin. Already inside the core ₹184.5 Cr revenue figure — the most certain of the three lines here.
Power Export (unverified)
Rests on a 22–25 MW cogen assumption never checked against the mill's actual boiler capacity. Treat as upside pending verification.
Updated View

P&L at current commercial urea rate, CO₂ excluded

A separate, more cautious version. Only ethyl acetate and BioUrea™ count as income. CO₂ is treated as an input — nearly free, from the host distillery's own fermentation — not as something this complex sells. Urea is priced at the real market rate (what farmer price plus government subsidy add up to today), not the flat ₹37,000/t assumption used above.

WORST CASE — Open-Market Ethanol + Stable Urea Market
₹7.3–9.9Cr EBITDA
₹171.3–174.5 Cr revenue — a 4.3–5.7% margin.
BEST CASE — Forward-Integrated + Crisis Urea Market
₹57.4–59.9Cr EBITDA
₹194.5–195.7 Cr revenue — a 29.4–30.7% margin.
Ethyl Acetate EBITDAUrea EBITDACombined
Worst case₹3.1 Cr₹4.2–6.8 Cr₹7.3–9.9 Cr
Best case₹29.3 Cr₹28.1–30.6 Cr₹57.4–59.9 Cr
Urea pricing basis: ₹25,000–29,000/t in a stable market, ₹65,000–67,000/t during a gas-price crisis — the actual production/import cost range, not the ₹5,360/t farmer price. Selling directly at this rate captures what would otherwise be split between the farmer and the government subsidy.

This is not just a plan. It is being built.

A 50 KLPD plant is about half built. The pilot tests are done. And the team has built plants before.

On this page
ETHANABER™ Stage 1 · MIDC Industrial Site

Real assets, real progress, on the ground today

50 KLPD Ethyl Acetate manufacturing plant at an MIDC industrial site. This is not a concept — civil works, fabricated equipment and site infrastructure are already in place.

⚡ 6-month lead on physical construction ⚡ 3-month lead from completed pilot-scale kinetics = 9 months ahead of competition, combined
0%
Plant Complete
50KLPD
Ethyl Acetate Capacity · MIDC Site
On Site
Major Fabricated Equipment Delivered

~50% PHYSICAL PLANT COMPLETION · MIDC INDUSTRIAL SITE

On The Ground

The work so far, in photographs

Civil works, storage, the boiler section and fabricated distillation columns at the 50 KLPD plant. Click any photo to enlarge it.

Storage shed - steel structure erected
Storage shed — steel structure erected
Shed interior - clear-span floor, foundations cast
Shed interior — clear-span floor, foundations cast
Boiler section - foundations and civil works
Boiler section — foundations and civil works
Underground storage tank - RCC walls built
Underground storage tank — RCC walls built
Storage tanks - three units under construction
Storage tanks — three units under construction
Site - structures and columns going up
Site — structures and columns going up
Distillation column shell - fabricated, on site
Distillation column shell — fabricated, on site
Column sections and trays - delivered
Column sections and trays — delivered
Column shells - ready for erection
Column shells — ready for erection
Pilot-Scale Validation

Twin reactor setup — kinetics already done

Before any big spending, the reaction speeds (kinetics) and the scale-up were already tested on this twin-reactor rig. That takes much of the risk out of the commercial design before it is built.

Twin reactor pilot lab setup
Twin reactor pilot lab setup — 50 L/day capacity, instrumented & automatedClick to zoom ↗
Pilot Configuration
Twinreactor setup
Parallel reactors enable direct kinetics comparison and scale-up validation in a single campaign.
Throughput
50L/day capacity
Sized specifically for process kinetics and scale-up study, not production — a deliberate, de-risking step before commercial scale.
Studies Completed
Reaction kinetics and scale-up data already in hand — the step most competitors haven't reached — worth a 3-month lead on its own.
Why this compounds the lead: most competing concepts at this stage are still on paper — process design without validated kinetics. Having both a twin pilot reactor's kinetics data and a half-built commercial plant simultaneously is unusual. Combined, these two facts put this project a full 9 months ahead of a typical competing proposal starting from the same point today — 6 months from physical construction already in the ground, plus 3 months from kinetics and scale-up data already in hand.
Our Leadership

The Minds Engineering the Future

One leadership team, one mission — combining process engineering, commercial execution, and sustainability strategy to build technologies that redefine water, chemicals, energy, and industrial decarbonization.

The Team

Meet the people behind ECOICE

Vikrant Indulkar
02 · Commercialize
Managing Partner
Vikrant Indulkar, MBA
The Growth Strategist
"Great technology changes nothing until the world adopts it."
Signature Persona
Market BuilderPartnership CreatorStrategic CommunicatorBusiness LeaderCommercial Expansion Specialist
Expertise
  • Business Development & Market Strategy
  • Strategic Partnerships & Tech Commercialization
  • Go-to-Market Strategy & Investment Readiness
  • Brand, Corporate Relations & Client Acquisition
Impact

Driving commercialization strategies that connect engineering innovation with industry adoption. Building markets. Creating value. Scaling impact.

Dr. Karan Chavan
01 · Ideate
CEO & Founder
Dr. Karan Chavan, Ph.D.
The Sustainability Architect
"Where others see environmental regulations, he sees billion-dollar engineering opportunities."
Signature Persona
VisionaryBuilderSustainability StrategistSystems ThinkerTechnology Commercializer
Expertise
  • Lifecycle Assessment (LCA) & Carbon Strategy
  • Process Development & Green Chemistry
  • Industrial Decarbonization & Circular Economy
  • Net-Zero Roadmaps, ESG Strategy & Climate Tech
  • Biorefineries & Advanced Water Systems
Impact

12+ years experience · multiple proprietary technologies · cross-industry projects across water, energy, chemicals & manufacturing · Founder, ECOICE.

"Turning climate challenges into scalable industrial opportunities."

0
Years Combined Experience
0
Industrial & Sustainability Projects
Global
Cross-Industry Impact
Lab → Market
Technology Commercialization
Founder Deep Dive

Why Dr. Karan Chavan is a rare combination

Nine things worth knowing about the person leading Project BioUrea™ — each independently verifiable, each unusual on its own.

01
National policy impact. PACE PET LCA work fed into a National Green Tribunal proceeding that helped set India's EPR recycling policy — engineering work that changed national policy for 1.4 billion people's plastic waste management. Extremely rare for an individual engineer's LCA to reach that level of policy influence.
02
11 million tonnes CO₂e/year. The NALCO decarbonisation roadmap LCA is the largest number in the portfolio — roughly the annual emissions of 2.4 million cars, NPC-stamped and government-accepted.
03
A rare credential combination. Ph.D. (Tech.) from ICT Mumbai — India's top chemical engineering institute — combined with an imminent Canadian P.Eng. and a 90% score on the specialist LCA technical exam. This exact combination is uncommon in Canada.
04
Remote turnkey delivery. Netsurf Biofit — a 45 KLPD biofertilizer plant — designed and delivered turnkey in India while managed remotely from Toronto, successfully commissioned. A genuine feat of remote industrial project management.
05
Opened a market. VoDCa technology validated across all 21 streams with stream-specific design rules — Baramati +17% biogas (+4,000 m³/day), Jubilant ~21%, Dhampur >10%. VSI certification secured for distillery biogas enhancement — VSI is the only body of its kind in the world for this purpose — opening the affiliated-distillery market and unlocking access across 220+ cooperative distilleries in Maharashtra.
06
Academic credibility alongside delivery. 3 peer-reviewed papers, 1 Elsevier book chapter, 55+ citations. Most consultants don't publish; most academics don't deliver large commercial engineering projects. This track record does both.
07
Unusual public engagement. Organizer of 5 climate hackathons and the BioPolicyX event, plus Climate Roast — reaching 1,000+ people across Climate Roast 2026 Pune ("Climate Rap") and Toronto ("Climate Comedy"), and ranked #2 at Toronto Climate Week 2026 (@crack4climate). Also presented "No Open Land Policy" at ICPP 6, the 6th International Conference on Public Policy, Toronto, June 2023. Genuinely unusual and memorable as a communication vehicle for climate engineering.
08
Three world-first technologies in development. Trayambakam (emissionless decentralised pyrolysis), Jalshuddhi (off-grid sewage-to-potable water), and Project Droplet (air-propulsion autonomous solar marine vessel) — each addressing a genuine gap in existing commercial solutions.
09
International research fellowships. Visiting Research Fellow at the University of Oulu, Finland (LCA of water treatment) and the University of Cantabria, Spain (LCA of arsenic treatment), under the GreenTech New INDIGO Project, European Commission, 2013. Presented at the 9th World Congress of Chemical Engineering, Seoul, 2013, and the 20th Annual Green Chemistry & Engineering Conference, Portland, 2016.
From concept to commercialization, ECOICE's leadership integrates sustainability vision, engineering excellence, and strategic execution to deliver industrial technologies with measurable environmental and economic impact.
Engineering Capability

Past Projects & Process Engineering Portfolio

ECOICE does contract research, process design and turnkey equipment manufacturing — the same skills that stand behind ETHANABER™ and BioUrea™.

R&D Facility
Gas chromatography, UV-Vis, COD analysis, biotechnology & chemical technology labs
Bioreactor Range
10L–1000Lscale-up
LAF, shaker incubators, full temperature-controlled fermentation train
Product Lines
6equipment categories
Agitators, heat exchangers, evaporators, reactors, distillation columns, bio-fermenters
Turnkey Deliveries
Multiplecommissioned plants
Full process design through commissioning, including remote project delivery

Product range — equipment engineering & manufacturing

Design, fabrication and commissioning capability across the core unit operations that also underpin the BioUrea™ complex.

Agitators

Agitators & Mixing

Top & bottom entry, side entry (fixed/swivel), twin shaft dispersers, static mixers, high-speed homogenizers — hydrofoil, anchor & Ruston turbine blade designs, CFD-verified.

Heat exchangers

Heat Exchangers / Condensers / Pasteurizers

Shell & tube and plate designs across process heating, cooling and pasteurization duty.

Evaporators

Evaporators

Falling film, forced circulation and ATFE (agitated thin film evaporator) — engineering design, manufacturing and commissioning in-house.

Reactors and storage tanks

Reactors & Storage Tanks

Glass-lined and stainless process reactors with integrated agitation, plus bulk storage tankage.

Distillation column

Distillation Columns

Multi-tray column design and fabrication — directly transferable expertise to the ETHANABER™ separation train.

Bio-fermenters

Bio-Fermenters

Pharmaceutical and industrial-grade fermentation vessels, lab through commercial scale.

Delivered projects

Netsurf Biofit — 45 KLPD Biofertilizer Plant

Parwanoo, Himachal Pradesh

Full turnkey delivery: process design, procurement, ETP fabrication, cGMP cleanroom (ISO 14644-1), commissioning, and remote handover from Toronto. Bacterial fermentation plant installed on floors 3–4 of an existing industrial building, engineered around 3–6 inch ceiling clearances.

Hand Sanitizer Manufacturing Plant

Export-Grade Turnkey Line

FDA-documentation-compliant sanitizer production line, built for export to regulated markets. Delivered alongside Netsurf Biofit as one of ECOICE's turnkey manufacturing projects.

10 TPD Coconut Oil → MCT Plant

Process Development & Commercial Delivery

Medium chain triglyceride (MCT) production from coconut oil — process development and feasibility analysis, 10–13% MCT yield with >85% of remaining oil utilized as food-grade coconut oil (AV<12). Demonstrated at 20L scale, then piloted and commissioned at 10 TPD commercial scale.

MRO Purification & Recovery Optimization

Contract Research & Process Development

MRO testing and process development to increase yield and recoveries; biodiesel production from lean streams of the MRO purification process; new solvent system development for lutein ester purification; zeaxanthin purification from paprika oleoresin.

Solid-Liquid Extraction System

Rotating Disc Contactor Design

Design and implementation of a Rotating Disc Contactor (RDC) for lecithin separation and purification, plus a multi-stage solid-liquid extraction setup.

Integrated Fermentation & Filtration System

Agricultural Biotechnology

Integrated fermentation and filtration process design and delivery for an agricultural biotechnology application.

Commissioned industrial plant, ECOICE delivery
A commissioned industrial plant, as deliveredClick to zoom ↗
Why this matters for BioUrea™: the ETHANABER™ and BioUrea™ complex leans on exactly this equipment stack — reactors, distillation columns, evaporators, heat exchangers, agitated vessels. This isn't unproven engineering territory for the team; it's the same discipline scaled to a new chemistry.