Gevo Inc's Business Segments
Gevo Inc's reported revenue by business segment and by geographic region, quarterly and annual, normalized against the consolidated income statement. Free below: the top 3 rows per table, this quarter and this fiscal year. Subscriber access adds the full segment history and operating income by segment.
Revenue Share by Reportable Segment - Q1 FY2026
- Gevo North Dakota Segment88.5%
- Renewable Natural Gas Segment10.6%
- Gevo Segment0.8%
Revenue by Reportable Segment - Q1 FY2026
| Segment | Revenue (Millions) | % of Total |
|---|---|---|
| Gevo North Dakota Segment | $ 38 | 88.5% |
| Renewable Natural Gas Segment | $ 5 | 10.6% |
| Gevo Segment | $ 0 | 0.8% |
Revenue by Product & Service Category - Q1 FY2026
- Ethanol66.6%
- Ethanol related products21.7%
- Environmental Attributes9.6%
- Renewable Natural Gas Commodity1.2%
- Other Revenue Sale of Isooctane and Software Services0.8%
Revenue by Product & Service Category - Q1 FY2026
| Category | Revenue (Millions) | % of Total |
|---|---|---|
| Ethanol | $ 29 | 66.6% |
| Ethanol related products | $ 9 | 21.7% |
| Environmental Attributes | $ 4 | 9.6% |
Product and service categories are a supplemental disclosure and are not required to sum to consolidated revenue or to the reportable segments above.
Description of Gevo Inc
Biocatalyst Overview
Our biocatalysts are microorganisms that have been designed to metabolize sugars
to produce isobutanol. Our technology team developed these proprietary biocatalysts
to efficiently convert fermentable sugars of all types into isobutanol by engineering
isobutanol pathways into the biocatalysts. We designed our biocatalysts to equal
or exceed the performance of the yeast currently used in commercial ethanol
production in yield (percentage of the theoretical maximum percentage of isobutanol
that can be made from a given amount of feedstock) and rate (how fast the sugar
fed to the fermentation is converted to isobutanol). We initially achieved our
target fermentation performance goals with our research biocatalyst at our GIFT®
mini-plant and then replicated this performance in a retrofitted one MGPY ethanol
demonstration facility located at ICM’s St. Joseph, Missouri site. We
select biocatalysts for their projected performance in the GIFT® process,
targeting lower cost isobutanol production. We continue to seek to improve the
performance parameters of our biocatalyst with a goal of reducing projected
capital and operating costs, increasing operating reliability and increasing
the volume of isobutanol production.
Continuous improvement of biocatalyst performance is achieved using a variety
of synthetic biology and conventional biotechnology tools to minimize the production
of unwanted by-products to improve isobutanol yield and rate, thereby reducing
capital and operating costs. With our biocatalysts, we have demonstrated that
we can produce isobutanol at commercial scale with rates and yields which we
believe validate our biotechnology pathways and efficiencies. Our commercial
biocatalyst is designed to produce isobutanol from common commercial fermentation
ethanol feedstocks, including grains (e.g., corn, wheat, sorghum and barley),
sugar cane, and molasses. This feedstock flexibility supports our initial deployment
in the U.S. and is designed to enable our future expansion into international
markets for production of isobutanol.
Although development work continues, we have shown at laboratory scale and at
our one MGPY demonstration facility located at ICM’s St. Joseph, Missouri
facility that we can convert hydrolyzed wood feedstocks into isobutanol. We
are further improving biocatalysts to efficiently produce isobutanol from cellulosic
feedstocks, including crops that are specifically cultivated to be converted
into fuels (e.g., switchgrass), forest residues (e.g., waste wood, pulp and
sustainable wood), agricultural residues (e.g., corn stalks, leaves, straw and
grasses) and municipal green waste (e.g., grass clippings and yard waste). We
carefully select our biocatalyst platforms based on their tolerance to isobutanol
and other conditions present during an industrial fermentation process, as well
as their known utility in large-scale commercial production processes.
Feedstocks
We have designed our biocatalyst platform to be capable of producing isobutanol
from any fuel ethanol feedstock currently in commercial use, which we believe,
in conjunction with our proprietary isobutanol separation unit, will permit
us to Retrofit any existing fuel ethanol facility. We have demonstrated that
our biocatalysts are capable of converting the types of sugars in grains and
sugar cane to isobutanol at our commercial targets for fermentation time and
yield and we believe that they will have the ability to convert these sugars
into isobutanol at a commercial scale. The vast majority of fuel ethanol currently
produced in the U.S. is produced from corn feedstock, which is abundant according
to data from the U.S. Department of Agriculture and the Renewable Fuels Association.
Although development work continues to be done, we have shown at laboratory
scale and at our one MGPY demonstration facility located at ICM’s St.
Joseph, Missouri site that we can convert certain cellulosic sugars into isobutanol.
We expect that our feedstock flexibility will allow our technology to be deployed
worldwide and will enable us to offer our customers protection from the raw
material cost volatility historically associated with petroleum-based products.
In June 2015, Agri-Energy, our wholly-owned subsidiary, entered into a Price
Risk Management, Origination and Merchandising Agreement (the “Origination
Agreement”) with FCStone Merchant Services, LLC (“FCStone”)
and a Grain Bin Lease Agreement with FCStone (the “Lease Agreement”).
Pursuant to the Origination Agreement, FCStone will originate and sell to Agri-Energy,
and Agri-Energy will purchase from FCStone, the entire volume of corn grain
used by our plant in Luverne, Minnesota. The initial term of the Origination
Agreement will continue for a period of eighteen months and will automatically
renew for additional terms of one year unless Agri-Energy gives notice of non-renewal
to FCStone. FCStone will receive an origination fee for purchasing and supplying
Agri-Energy with all of the corn used by Agri-Energy’s plant in Luverne,
Minnesota. As security for the payment and performance of all indebtedness,
liabilities and obligations of Agri-Energy to FCStone, Agri-Energy granted to
FCStone a security interest in the corn grain stored in grain storage bins owned
and operated by Agri-Energy (“Storage Bins”) and leased to FCStone
pursuant to the Lease Agreement. Pursuant to the Lease Agreement, FCStone will
lease Storage Bins from Agri-Energy to store the corn grain prior to title of
the corn grain transferring to Agri-Energy upon Agri-Energy’s purchase
of the corn grain. FCStone agrees to lease Storage Bins sufficient to store
700,000 bushels of corn grain and agrees to pay to Agri-Energy $175,000 per
year. The term of the Lease Agreement will run concurrently with the Origination
Agreement, and will be extended, terminated, or expire in accordance with the
Origination Agreement. The Company also entered into an unsecured guaranty (the
“Guaranty”) in favor of FCStone whereby the Company guaranteed the
obligations of Agri-Energy to FCStone under the Origination Agreement. The Guaranty
shall terminate on the earlier to occur of (i) April 15, 2020 or (ii) termination
of the Origination Agreement.
GIFT® Improves Fermentation Performance
Our experiments show that the GIFT® fermentation and recovery system provides
enhanced fermentation performance as well as efficient recovery of isobutanol
and other alcohols. The GIFT® system enables continuous separation of isobutanol
from the fermentation tanks while fermentation is in process. Isobutanol is
removed from the fermentation broth using a low temperature distillation to
continuously remove the isobutanol as it is formed without the biocatalyst being
affected. Since biocatalysts have a low tolerance for high isobutanol concentrations
in fermentation, the ability of our process to continuously remove isobutanol
as it is produced allows our biocatalyst to continue processing sugar into isobutanol
at a high rate without being suppressed by rising levels of isobutanol in the
fermenter, reducing the time to complete the fermentation. Using our biocatalysts,
we have demonstrated that GIFT® enables isobutanol fermentation times equal
to, or less than, those achieved in the current conventional production of ethanol,
which allows us to fit our technology into existing ethanol fermenters reducing
capital expenditures. We have designed a proprietary engineering package to
carry out our isobutanol fermentation and recovery process.
GIFT® requires limited change to existing ethanol production infrastructure.
As with ethanol production, feedstock is ground, cooked, treated with enzymes
and fermented. Just like ethanol production, after fermentation, a primary product
(isobutanol) and a co-product (iDGs™) are recovered for sale. The main
modifications of the GIFT® system are replacing the ethanol producing yeast
with Gevo’s proprietary isobutanol producing biocatalyst, and adding low
temperature distillation equipment for continuous removal and separation of
isobutanol.
Conversion of Isobutanol into Hydrocarbons
We have demonstrated conversion of our isobutanol into a wide variety of hydrocarbon
products which are currently used to produce plastics, fibers, polyester, rubber
and other polymers and hydrocarbon fuels. Hydrocarbon products consist entirely
of hydrogen and carbon and are currently derived almost exclusively from petroleum,
natural gas and coal. Importantly, isobutanol can be dehydrated to produce butenes,
which are an intermediate product in the production of hydrocarbon products
with many industrial uses. The straightforward conversion of our isobutanol
into butenes is a fundamentally important process that enables isobutanol to
be used as a building block chemical. Much of the technology necessary to convert
isobutanol into butenes and subsequently into these hydrocarbon products is
commonly known and practiced in the chemicals industry today. For example, the
dehydration of ethanol to ethylene, which uses a similar process and technology
to the dehydration of isobutanol, is practiced commercially today to serve the
ethylene market. The dehydration of isobutanol into butenes is not commercially
practiced today because isobutanol produced from petroleum is not cost-competitive
with other petrochemical processes for generation of butenes. We believe that
our efficient fermentation technology for producing isobutanol will promote
commercial isobutanol dehydration and provide us with the opportunity to access
hydrocarbon markets. To assist in accessing these markets, we have developed
a hydrocarbon processing demonstration plant (“Hydrocarbons Demo Plant”)
near Houston, Texas, in partnership with South Hampton Resources, Inc. (“South
Hampton”). The Hydrocarbon Demo Plant can process approximately 6,000
to 7,000 gallons of our isobutanol per month into a variety of renewable hydrocarbons
for use as fuels and chemicals.
Our ETO Technology
We have also developed new technologies using ethanol as a feedstock for the
production of hydrocarbons, renewable hydrogen, and other chemical intermediates,
which we describe as our ethanol-to-olefins (“ETO”) technologies.
The process produces tailored mixes of isobutylene, propylene, hydrogen and
acetone, which are valuable as standalone molecules, or as feedstocks to produce
other chemical products and longer chain alcohols. This technology has the potential
to address additional markets in the chemicals and plastics fields, such as
renewable polypropylene for automobiles and packaging and renewable hydrogen
for use in chemical and fuel cell markets. At this time, this technology has
only been operated at a laboratory scale, but if successfully scaled up to commercial
level, this technology may provide the estimated 25BGPY global ethanol industry
a broader set of end-product market and margin opportunities.
Underpinning the ETO technology is our development of proprietary mixed metal
oxide catalysts that produce either polymer grade propylene, high purity isobutylene
or acetone in high yields in a single processing step. One of the benefits of
the technology is that we can use conventional fuel grade specification ethanol
that can be sourced from a variety of feedstocks with no apparent adverse impact
on end product yields. Water, which is co-fed with the ethanol, is able to be
recycled resulting in a process which generates minimal waste. The ethanol and
water mixture is vaporized and fed across a fixed catalyst bed resulting in
a gaseous product mix consisting of the propylene, isobutylene or acetone, in
addition to hydrogen and carbon dioxide, along with lesser amounts of methane
and ethylene. Separation of gaseous products can be achieved via conventional
process technologies and unit operations within the petroleum industry.
