SAVRN.Imperial Valley · CO₂-to-Graphene · Financial model
Financial model

850,000 tonnes of CO₂ a year, and only one way it pays for itself.

This is the financial model for deploying the CO₂-to-graphene business at Imperial Valley, California, on 850,000 t/yr of biogenic CO₂ captured from the biomass plant. It is built on two published pages, with the sizing model supplying the physics and the commercial strategy supplying the discipline, and on the capital record of the three capture projects of this size that have actually been built. That record is what changes the answer: capture and wells cost more than the sizing page carries, and the credit stack does not cover them.

Site Mesquite Lake Energy Park, Imperial Valley, CACO₂ input 850,000 t/yrHorizon 25 years, all equityEstimate class AACE Class 5
CO₂ captured
850,000 t/yr
From the biomass plant flue gas
Credit stack over 12 years
$679–778M
Covers about a third of the capture blocks
Physical yield cap
173,864 t/yr
Carbon available at 75 percent conversion, about 46x world graphene demand
Peak capital, base case
$1.27B
Rises to $2.10B at full conversion

01Two engines, and which one actually pays

The project has two revenue engines and they behave differently. The instinct is to treat the CO₂ side as a safe floor with product revenue as upside on top. The comparables do not support that reading.

How the carbon is routed, and what each route earnsBiomass plantMesquite Lake Energy ParkImperial Valley, CACO₂ captured850,000 t/yrEngine 1 · CO₂Capture, compression, injection.Runs whether or not graphene sells.§45Q utilization on carbon into product,sequestration on the balance.§45Q over 12 years$679M–$778MEngine 2 · GrapheneCarbon converted and sold.Gated by signed offtake, not by nameplate.Case A year 25$750M/yrInjectionBalance of the stream to the well.Case A year 25810,000 t/yrthe published industry record: producers with 100+ t/yr of capacity book under $1M of revenue
The CO₂ engine is volume-certain, since it depends on capture and injection running rather than on selling a kilogram of anything. The product engine is demand-gated. Volume-certain is not the same as sufficient.

The CO₂ engine does not carry the project. Every tonne captured earns §45Q, at the utilization rate where carbon goes into product and the sequestration rate where the balance goes into the well. On 850,000 t/yr that is roughly $66M a year for twelve years. Against capture blocks that cost about $1.0B all in, it services roughly a third of the capital. Run the CO₂ side alone and it never pays back on §45Q, and it still does not clear with a certified LCFS pathway and a carbon removal attribute stacked on top. Breakeven on the CO₂ blocks alone is about $300 per tonne of effective credit value, in a range of $254 to $353 across the capital comparables.

So the product engine is the condition, not the upside. The commercial strategy page documents the industry record, which is that producers with more than 100 t/yr of installed capacity book under $1M of annual revenue. This model therefore drives tonnage from a contracted ramp and sizes conversion capacity to follow it, so capital is never committed ahead of a signed contract. What it does not do is treat that engine as optional. Without a book of business the capture project does not finance.

02Mass balance

The carbon splits two ways. What is sold becomes graphene; the balance of the stream is injected. Both halves earn a credit.

LineValueBasis
CO₂ captured850,000 t/yrBiomass flue gas at Mesquite Lake
Conversion efficiency75%Sizing model default; the range is 40 to 95 percent
Carbon yield0.2727 t C / t CO₂Stoichiometry, 12/44
Physical yield cap173,864 t/yrThe most graphene the stream can produce at 75 percent conversion
CO₂ consumed as feedstock3.67 t per t soldDrives the §45Q utilization tier
CO₂ injectedbalance of the streamDrives the §45Q sequestration tier
O₂ coproduct2.67 t per t CSold at the merchant rate on the share the market absorbs
Electrical load6.0 MWh/t + 1.0 MWh/t CO₂Electrolysis plus capture parasitic, behind the meter

Conversion consumes a minority of the stream in every case. At the phase 1 book the plant converts about 183,000 t of CO₂ into product and injects about 667,000 t, so the credit stack stays dominated by the sequestration tier and shifts toward utilization only as tonnage grows. The injected balance is what earns the sequestration tier and the removal attribute, which is why the sequestration floor is a design constraint rather than a leftover.

03Three cases

The constraint that decides the shape of this business is that world graphene demand is about 3,800 tonnes a year and this plant's carbon yield is forty six times that. No case sells one product into one market, so each case is a book of business across ten segments rather than a tonnage forecast.

Tonnage: three cases against the plant's physical yield caplog scale · world graphene demand today is 3,800 t/yr, so every case here is a multiple of the entire market1101001,00010,000100,000Y1Y5Y10Y15Y20Y25t/yryield cap 173,864 t/yr at 75% conversionCase A · anchor book25,000 t/yr across ten segmentsCase B · phase 1 as scoped50,000 t/yr, five to eight anchor customersCase C · full conversion150,000 t/yr, every segment near its ceiling
All three cases are built from the same ten-segment map, with each segment ramping only after its qualification cycle. They differ in how much of each segment's published absorbable volume the project wins.
CaseWhat it assumesFull bookBlended priceMultiple of world demand
A · Anchor bookA short list of anchor contracts, weighted to the segments that qualify fastest. Enough to prove the process and lock the §45Q utilization tier.25,000 t/yr$38,619/t6.6x
B · Phase 1 as scopedFive to eight anchor customers across every tier. Battery-grade graphite and concrete admixture carry the volume, specialty carries the margin.50,000 t/yr$31,033/t13.2x
C · Full conversionEvery segment at or near the volume the market map says it can absorb. This is what full conversion of the available carbon requires, not a demand forecast.150,000 t/yr$14,127/t39.5x

Price is an output here, not an input. Each segment carries a price today and a price at full-conversion volume, and the model interpolates between them in proportion to how much of that segment the project is filling. Case B lands at $39,300 per tonne at its published mix, which is the same blended figure the sizing model reaches independently. That agreement is a check on the mix, not a coincidence.

The book of business is editable. The live product mix model lets you reshape it segment by segment and watch the capital, the credits and the returns move with it.

04Results

All three cases, 25 years, all equity, computed in the workbook and reproduced line for line by the live model page.

MetricA · Anchor bookB · Phase 1C · Full conversion
Full book25,000 t/yr50,000 t/yr150,000 t/yr
Peak capital deployed$1,270M$1,436M$2,096M
Peak cash shortfall$982M$918M$724M
Revenue, year 10$1,167M$1,752M$2,314M
EBITDA, year 25$742M$1,179M$1,531M
Project IRR, unlevered38.5%51.5%70.0%
NPV at 15 percent$1,833M$3,196M$4,467M
PaybackYear 5Year 4Year 3
Credit stack over the credit period$778M$758M$679M

Underwrite case A. The returns rise with volume because the fixed CO₂ blocks are already paid for in every case, so incremental tonnage carries only its conversion capital. That is a real effect, and it is also why the higher cases should not be read as the plan: case C requires every one of ten segments to reach the top of its published absorbable range, and each of those segments carries its own qualification cycle measured in years. Case A clears a fifteen percent hurdle on a book small enough to name the customers.

05Capital

The CO₂ blocks are built once for the whole stream. Conversion capacity is added only as tonnage is contracted.

BlockCostTiming rule
Capture island and injection wells$800MBuilt once, 60 percent in year one and 40 percent in year two. Sized for the full 850,000 t/yr stream, so it does not scale with graphene demand.
O₂ cryogenic recovery$100M
220 kV substation$80M
Oxygen recovery$100M
Admin, control, safety$25M
Kiln potlines$5,222 per annual tonneAdded only when capacity is contracted. Derived from the sizing model's $940M, $110M and $30M for a 180 kt/yr build.
Purification and spec$611 per annual tonne
Rail spur and loadout$167 per annual tonne
Contingency10 percentOn everything above, per the sizing model's own stack

This is the capital discipline the strategy page asks for, expressed as a formula. Capacity built never falls and never runs ahead of the tonnage under contract, so the capital that produced the industry's defining failure, kilns installed against demand that never arrived, cannot be spent by this model.

06What has to be true

Each of these is a condition the model depends on, with the consequence if it fails.

  1. §45Q survives review at both tiers. The utilization tier requires an audited end use and a lifecycle analysis; the sequestration tier requires the injection permit and an MRV plan. Remove §45Q entirely and the base case loses roughly $66M a year for twelve years. A tax opinion comes before any of this is relied on.
  2. The injection path is permitted. The sequestration tier assumes the balance of the stream is injected on site. If the permit path fails, that CO₂ has to be vented, the sequestration credit disappears, and the project becomes a graphene business with a capture island attached.
  3. Power stays behind the meter. The model runs power at $45/MWh. At $90/MWh the base case loses about $41M a year at year-25 volumes, and considerably more in the capacity cases where electrolysis load dominates.
  4. Offtake is signed before capacity is built. Capacity in this model follows contracts by construction. If capital is committed ahead of offtake, the model no longer describes the project being built.
  5. Realized price holds on the declining curve. Price is the dominant driver once volume is meaningful. A 25 percent shortfall against the curve takes roughly $585M off year-25 EBITDA in the anchor case.
  6. The plant basis is settled. This model uses 850,000 t/yr of captured CO₂, which is the instruction. The sizing model page runs 840,000 t/yr, and the energy-island page describes a different biomass configuration. One project basis needs to be canonical before the model is taken to a counterparty.

07The workbook

The model is a live-formula workbook, not a picture of one. One input tab drives everything.

TabWhat it holds
AssumptionsEvery input, each with its source. The case selector is one cell. Change an input and the whole workbook reflows.
Revenue RampThe three tonnage cases, the declining price curve, and the yield-cap check.
Mass BalanceCarbon, CO₂ utilized and injected, O₂ coproduct, power and continuous load.
Capacity & CapexCapacity ratchet, capital spend by block, cumulative capital.
Credits§45Q at both tiers over the twelve-year period, transfer realization, O₂ sales.
OpexPower, conversion, injection, consumables, labor, royalty, formulation, selling and administrative.
P&L · Cash Flow · Returns25 years, all equity, with IRR, NPV, payback and peak capital.
SensitivityPrice, §45Q denial, power cost, and the case where graphene never sells at all.
SourcesEvery input traced to a published page, or marked as introduced by the model.

Download the workbook: SAVRN_Imperial_Valley_CO2_to_Graphene_Financial_Model.xlsx. Live formulas throughout; the case selector is Assumptions!B4.

Built from the sizing model and the commercial strategy. Inputs marked "model" in the Sources tab are introduced here and appear on neither page: technology royalty, selling and administrative cost, formulation and logistics, the merchant O₂ share, injection cost, and the discount rate.

Basis and disclosures

Purpose
This page is prepared by SAVRN for evaluation by the recipient. It is not an offer to sell or a solicitation of an offer to buy any security or interest, and it is not investment, legal, accounting, or tax advice. Any offering would be made only through definitive documents.
Forward-looking content
Scenarios, model outputs, ramp schedules, and pricing bands on this page are estimates built on the assumptions and sources shown. Actual results will differ. SAVRN undertakes no obligation to update this page as conditions change.
Tax credits
Amounts shown for §45Y, §45Q, §48, and §48E are estimates of eligibility under current statute and guidance. Each depends on facts not yet fixed, including prevailing wage and apprenticeship compliance, begin-construction date, domestic content, energy-community designation, prohibited-foreign-entity sourcing, and placed-in-service timing. Transfer pricing under §6418 is market-dependent. A tax opinion is required before any amount on this page is relied on.
Model outputs
Outputs move with the inputs on this page. EBITDA is stated before depreciation, amortization, interest, tax, technology license and royalty payments, selling and administrative cost, outbound logistics, and product formulation cost. Volumes assume offtake at the stated prices; the industry record on that point is set out in the commercial strategy page.
Estimate class
Capital and operating figures are AACE Class 5, order-of-magnitude (−50% / +100%), based on parametric analogies rather than engineered quantities. They are not a FEED or FEL-1 estimate.
Third parties
Companies, products, contracts, and prices named on this page are drawn from the public sources listed and are used for market reference. No affiliation, endorsement, or supply relationship is implied except where a signed agreement is stated.
Data as of
August 2026, from the sources listed on this page.
Distribution
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