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™.
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.
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.
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.
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.
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.
Each plant is one more step off imported gas.
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.
Urea made from crop ethanol, not fossil gas. From the field, back to the field.
No war, shipping strait or LNG price decides what Indian food costs.
Green ethyl acetate, green hydrogen and green ammonia give industry inputs with no fossil gas behind them.
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.
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.
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.
What one complex is worth
The full working behind each number is under How It Works, Plants & Profit and Why India Needs It.
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.
| Route | L Ethanol / t Cane | Cane Required | Acreage | Sugar Co-Produced | Verdict |
|---|---|---|---|---|---|
| C-Heavy Molasses | 10.8 | 1.83M t | 56,559 ac | 210,800 t | Sugar-dominant, mill ~7× larger |
| B-Heavy Molasses — SELECTED | 21.75 | 910,345 t | 28,097 ac | 86,483 t | Balanced — our choice |
| Full Juice / Syrup | 84 | 235,714 t | 7,272 ac | 0 t | No sugar business at all |
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.
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.
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.
| Scenario | Cost/tonne | Farmer Pays | Subsidy Gap | Govt. 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% |
What one plant saves the government
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.
Application rate — verified for sugarcane
| Application Rate | Acreage Fertilized | Source |
|---|---|---|
| 150 kg/acre/yr | 40,700 acres | Mid-range Indian agronomy for cane — matches visual |
| 250 kg/acre/yr | 24,420 acres | Heavier dose for high-yield cane |
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.
| Avoided Pathway | Low | Mid | High | Basis |
|---|---|---|---|---|
| Ethyl acetate vs. fossil route | 26,800 | 34,200 | 41,700 | 14,883t × 1.8–2.8 kgCO₂e/kg |
| BioUrea™ vs. grey urea | 11,000 | 15,300 | 19,500 | 6,108t × 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 only | 48,900 | 60,600 | 72,300 | |
| + Urea field hydrolysis (biogenic C) | +4,500 | 6,108t × 0.733 (IPCC) | ||
| Total, all boundaries | 53,400 | ~65,100 | 76,800 | |
Ethanol goes in. Fertiliser comes out.
Every step, every tonne and every unit of energy is shown here, with nothing hidden.
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.
Block 3 — Catalytic Dehydrogenation
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
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
HP reactor, carbamate condenser + stripper, decomposer, evaporator, vacuum concentrator, prilling. Output 46% N BioUrea™, identical spec to conventional urea — drop-in for the farmer.
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.
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.
| Section | Fab. Steel | Key equipment |
|---|---|---|
| 1. ETHANABER reactor train | 40.3 t | Dehydrogenation reactors (×2), Cu-Cr catalyst |
| 2. Separation / distillation | 77.4 t | Recycle + purification columns (azeotrope duty) |
| 3. Hydrogen purification | — | PSA package + H₂ compressor to 150–200 bar |
| 4. Ammonia synthesis | 89.5 t | Syngas compressor, Fe-catalyst converter, ASU |
| 5. Urea synthesis & finishing | 57.9 t | Ti-clad reactor + stripper, granulator |
| 6. CO₂ recovery & liquefaction | 62.6 t | Scrubber, compressor, food-grade bottling |
| 7. Storage & utilities | 163.2 t | Tankage, cooling tower, DCS/PLC |
| Total Purchased Equipment | 490.8 t | ₹31.11 Cr |
| Total Installed (Lang 3.5–4.5×) | ~1,915–2,514 t | incl. structural + piping steel — cost pending vendor quotes |
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.
Where India's ethanol actually comes from
Through August 2026, Ethanol Supply Year 2025–26.
| Feedstock | Supply | Share |
|---|---|---|
| Maize | 345 crore L | 38.5% |
| Surplus FCI rice | 214 crore L | 23.9% |
| Damaged food grains | 64 crore L | 7.2% |
| Sugarcane juice | 149 crore L | 16.6% |
| B-heavy molasses | 107 crore L | 12.0% |
| C-heavy molasses | 15 crore L | 1.7% |
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-Heavy | Cane Direct Juice | Maize (Grain) | Surplus Rice (Grain) | |
|---|---|---|---|---|
| Yield per tonne feedstock | 21.75 L | 70–84 L | 380 L | 440–450 L |
| Feedstock required | 910,345 t/yr | 235,714 t/yr | 52,105 t/yr | 44,494 t/yr |
| Land required | 28,097 acres | 7,272 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-product | Sugar (86,500 t/yr) | None | DDGS (~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 loop | Sugarcane (B-Heavy) | Maize (Grain) |
|---|---|---|
| Crop in | 910,345 t/yr | 52,105 t/yr |
| Land growing it | 28,097 acres | ~37,760 acres |
| Food / feed co-product | Sugar 86,483 t/yr | DDGS ~14,300 t/yr |
| BioUrea™ back out | 6,108 t/yr | 6,108 t/yr |
| Land fertilised at 150 kg/acre | 40,700 acres | 40,700 acres |
| Fertiliser made vs. own land | 1.45× | 1.08× cane dose basis |
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.
B-Heavy chain — cane to ethanol
| Stream | Value | Calculation | Status |
|---|---|---|---|
| Sugarcane crushed | 910,345 t/yr | 19.8M L ÷ 21.75 L/t cane | Cross-checked |
| Sugar co-produced | 86,483 t/yr | 910,345 × 95 kg/t cane | Cross-checked |
| Ethanol plant capacity | 15,622 t/yr | 60,000 L/d × 0.789 × 330 d | 330-day basis |
| Cane acreage required | 28,097 ac | 910,345 ÷ 32.4 t/acre | Cross-checked |
ETHANABER™ → BioUrea™ — the full chain
| Stream | Value | Calculation | vs. Visual |
|---|---|---|---|
| Ethyl acetate | 14,883 t/yr | 50,000 L/d × 0.902 × 330 d | Matches exactly |
| Ethanol required | 15,881 t/yr | 14,883 × (2×46.07÷88.11) ÷ 0.98 | 259 t/yr (1.7%) above distillery capacity |
| Hydrogen, gross | 681 t/yr | 14,883 × (2×2.016÷88.11) | Visual: 677 t / 2.05 TPD — matches |
| Hydrogen, usable | 647 t/yr | 681 × 95% PSA recovery | PSA loss applied |
| Fermentation CO₂, recovered | 13,431 t/yr | 14,923 gross × 90% capture | Capture eff. applied |
| Green ammonia | 3,534 t/yr | 647 × (2×17.03÷3×2.016) × 0.97 | Visual: 11.6 TPD — uses gross H₂ |
| BioUrea™ | 6,108 t/yr | 3,534 × (60.06÷2×17.03) × 0.98 | Visual: 6,105 t — matches |
| CO₂ to urea | 4,567 t/yr | 3,534 × (44.01÷2×17.03) | — |
| CO₂ surplus (food grade / dry ice) | 8,864 t/yr | 13,431 − 4,567 | Visual: 9,940 — likely omits capture eff. |
Circularity — it grows more than it consumes
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.
| Consumer | Basis | MWh/yr |
|---|---|---|
| Ethyl acetate — thermal (steam) | 14,883 t × 1,200 kWh-th/t | 17,860 |
| Ethyl acetate — electrical | 14,883 t × 150 kWh-e/t | 2,232 |
| Ammonia loop + ASU | 3,534 t × 750 kWh-e/t | 2,651 |
| Urea granulation | 6,108 t × 180 kWh-e/t | 1,099 |
| CO₂ liquefaction | 8,864 t × 100 kWh-e/t | 886 |
| Total thermal demand | 17,860 | |
| Total electrical demand | 6,869 |
Is the bagasse enough?
Total bagasse energy pool
910,345 t × 29% yield = 264,000 t bagasse/yr. At 7.37 GJ/t and 80% boiler efficiency:
New cascade needs
The whole ETHANABER + ammonia + urea + CO₂ cascade, together:
Net energy position
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.
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 Plant
- 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.
Semi-Commercial Plant
- 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.
Commercial Complex
- Be the market leader. You start 9 months ahead of anyone beginning today.
- Makes about 13,570 t ethyl acetate and 5,820 t BioUrea™ a year.
- Earns about ₹64 Cr a year on your own ethanol. Pays for itself in under a year.
- Invest, co-own or license a complex — for a cane mill, a cooperative or a grain distillery.
- Your part: you make green urea for about 40,000 acres and lead the switch.
What each plant is, and what it makes
| 100 L Pilot | 1,000 L Semi-Commercial | 60 KLPD Full Scale | |
|---|---|---|---|
| Role | Proof of concept | Scale-up demo, first sales | Commercial complex |
| Ethanol feed | 132 L/day | 1,316 L/day | 60,000 L/day |
| Ethyl acetate | 100 L/day (90 kg) | 1,000 L/day (902 kg) | 45,580 L/day (41.1 t) |
| Green hydrogen | 4.1 kg/day | 41 kg/day | 1,869 kg/day |
| Ethyl acetate per year | 29.8 t | 298 t | 13,568 t |
| Hydrogen per year | 1.35 t (15,150 Nm³) | 13.5 t (1.52 lakh Nm³) | 617 t (69 lakh Nm³) |
| Byproduct per year | 3.5 t | 34.6 t | 1,576 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 |
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/L | 100 L Pilot | 1,000 L Semi-Commercial | 60 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 payback | 7.4 years | 1.2 years | 0.5 years |
| Hydrogen turned into BioUrea™ instead | — | — | ₹6.4 Cr (+₹1.5 Cr) |
| Bought ethanol at ₹70/L | 100 L Pilot | 1,000 L Semi-Commercial | 60 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 payback | none | 3.5 years | 1.2 years |
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 price | 100 L Pilot needs | 1,000 L Semi needs | 60 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 |
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.
| Ethyl acetate price → | ₹80 | ₹90 | ₹100 | ₹110 | ₹120 |
|---|---|---|---|---|---|
| Ethanol ₹45/L | 4.5 yr | 2.4 yr | 1.6 yr | 1.2 yr | 1.0 yr |
| Ethanol ₹52/L | 56 yr | 4.6 yr | 2.4 yr | 1.6 yr | 1.2 yr |
| Ethanol ₹60/L | loss | loss | 5.5 yr | 2.6 yr | 1.7 yr |
| Ethanol ₹70/L | loss | loss | loss | 10.9 yr | 3.5 yr |
| Ethyl acetate price → | ₹80 | ₹90 | ₹100 | ₹110 | ₹120 |
|---|---|---|---|---|---|
| Ethanol ₹45/L | 1.4 yr | 0.9 yr | 0.7 yr | 0.5 yr | 0.4 yr |
| Ethanol ₹52/L | 3.1 yr | 1.4 yr | 0.9 yr | 0.7 yr | 0.5 yr |
| Ethanol ₹60/L | loss | 4.0 yr | 1.5 yr | 1.0 yr | 0.7 yr |
| Ethanol ₹70/L | loss | loss | 14.6 yr | 2.1 yr | 1.2 yr |
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 Pilot | 1,000 L Semi-Commercial | 60 KLPD Full Scale | |
|---|---|---|---|
| Ethanol used per year | 43,400 L | 4.34 lakh L | 198 lakh L |
| Sugarcane crushed (B-heavy) | 1,997 t | 19,971 t | 910,345 t |
| Cane land | 62 acres | 616 acres | 28,097 acres |
| Sugar still produced | 190 t | 1,897 t | 86,483 t |
| Or maize (grain) | 114 t | 1,143 t | 52,105 t |
| Maize land | 83 acres | 829 acres | ~37,760 acres |
| DDGS feed co-product | 31 t | 314 t | ~14,300 t |
| BioUrea™ back to the land (150 kg/acre) | — | — | 38,800 acres |
Each plant is one more step off imported gas.
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.
Urea made from crop ethanol, not fossil gas. From the field, back to the field.
No war, shipping strait or LNG price decides what Indian food costs.
Green ethyl acetate, green hydrogen and green ammonia give industry inputs with no fossil gas behind them.
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.
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 — full cost build-up
| Line | Calculation | Open Market | Fwd-Integrated |
|---|---|---|---|
| Revenue | 14,883t × ₹104,000 | ₹154.8 Cr | ₹154.8 Cr |
| Ethanol feedstock | 20.13M L × price | ₹130.8 Cr | ₹104.7 Cr |
| Utilities | steam + 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%) |
BioUrea™ — full running cost
| Item | Conservative | Adjusted | Note |
|---|---|---|---|
| Electricity | ₹2.62 Cr | ₹2.62 Cr | NH₃ loop + granulation, rebuilt |
| Labour | ₹1.60 Cr | ₹1.07 Cr | ⅓ shared with EtAc crew |
| Packaging | ₹1.50 Cr | ₹0.38 Cr | Bulk vs. retail bagging |
| Maintenance | ₹1.30 Cr | ₹0.87 Cr | Shared overhead |
| Steam | ₹1.20 Cr | ₹1.20 Cr | |
| Nitrogen (ASU) | ₹1.11 Cr | ₹1.11 Cr | |
| Carbon Dioxide | ₹0.91 Cr | ₹0.91 Cr | Corrected from a 10× error |
| Administration | ₹0.80 Cr | ₹0.53 Cr | |
| Chemicals | ₹0.60 Cr | ₹0.45 Cr | Catalyst 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%) |
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.
| Scenario | Realized Price/t | BioUrea™ Revenue | OPEX | BioUrea™ 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
Sugar, CO₂ & power — the three upside lines
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.
| Ethyl Acetate EBITDA | Urea EBITDA | Combined | |
|---|---|---|---|
| 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 |
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.
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.
~50% PHYSICAL PLANT COMPLETION · MIDC INDUSTRIAL SITE
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.
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.
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.
Meet the people behind ECOICE
- Business Development & Market Strategy
- Strategic Partnerships & Tech Commercialization
- Go-to-Market Strategy & Investment Readiness
- Brand, Corporate Relations & Client Acquisition
Driving commercialization strategies that connect engineering innovation with industry adoption. Building markets. Creating value. Scaling impact.
- Lifecycle Assessment (LCA) & Carbon Strategy
- Process Development & Green Chemistry
- Industrial Decarbonization & Circular Economy
- Net-Zero Roadmaps, ESG Strategy & Climate Tech
- Biorefineries & Advanced Water Systems
12+ years experience · multiple proprietary technologies · cross-industry projects across water, energy, chemicals & manufacturing · Founder, ECOICE.
"Turning climate challenges into scalable industrial opportunities."
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.
Past Projects & Process Engineering Portfolio
ECOICE does contract research, process design and turnkey equipment manufacturing — the same skills that stand behind ETHANABER™ and BioUrea™.
Product range — equipment engineering & manufacturing
Design, fabrication and commissioning capability across the core unit operations that also underpin the BioUrea™ complex.
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 / Condensers / Pasteurizers
Shell & tube and plate designs across process heating, cooling and pasteurization duty.
Evaporators
Falling film, forced circulation and ATFE (agitated thin film evaporator) — engineering design, manufacturing and commissioning in-house.
Reactors & Storage Tanks
Glass-lined and stainless process reactors with integrated agitation, plus bulk storage tankage.
Distillation Columns
Multi-tray column design and fabrication — directly transferable expertise to the ETHANABER™ separation train.
Bio-Fermenters
Pharmaceutical and industrial-grade fermentation vessels, lab through commercial scale.
Delivered projects
Netsurf Biofit — 45 KLPD Biofertilizer Plant
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
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
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
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
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
Integrated fermentation and filtration process design and delivery for an agricultural biotechnology application.