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Project profile

Alberta gas-plant decarbonization

Integrated oxy-fuel generation, facility electrification, air separation and CO₂ compression for sequestration at a large natural-gas processing plant in the Western Canadian Sedimentary Basin.

In development Stage: Concept-level scope published; development stage not yet publishedC02 Page reviewed: 14 September 2026

Summary

Host facility
One of the larger natural-gas processing plants of a Calgary-based oil and gas producer. Host name not disclosed under confidentiality.
Location
Alberta, Canada — Western Canadian Sedimentary Basin. Sub-region not disclosed.
Valverde’s role
Project developer; prospective equity partner in the generation and carbon-management assets.
Technology
Clean Energy Systems Direct Steam Gas Generator (DSGG) oxy-fuel unit with gas-turbine generators, under Valverde’s master licence.
Fuel
Pipeline-quality natural gas from the plant.
Capacity basis
Not published. not publishedC05
Carbon destination
Geological sequestration after compression. Storage site and operator not published. design intent · Valverde
Power offtake
Plant operations first; surplus zero-emission electricity to the Alberta grid. design intent · Valverde
Next milestone
Not yet published.C02

The facility problem

A large gas plant runs continuous compression, refrigeration and treating loads, today driven by natural-gas engines and turbines that emit CO₂ and NOx from exhaust stacks. Its emissions exposure is rising under federal and provincial methane and carbon rules, while its power demand is not going anywhere.

The proposed project replaces that gas-driven equipment with electric drives powered by on-site oxy-fuel generation, so the plant’s own fuel becomes zero-emission electricity and the combustion CO₂ becomes a captured, compressed stream for sequestration rather than a stack emission.

Problem statement derived from the published project scope, not from host-facility data.C03

Proposed configuration

Scope of the project

As described publicly by Valverde. Each element is a design intent until feasibility confirms it.

01

Oxy-fuel generation

Install the CES Direct Steam Gas Generation unit and connect gas-turbine generators to produce electricity from the steam and CO₂ stream.

02

Facility electrification

Convert natural-gas-driven generators and compression to electric drive, removing their exhaust emissions and consolidating fuel use into the oxy-fuel unit.

03

Air separation unit

Implement a properly sized ASU to supply the oxygen the combustor requires.

04

CO₂ compression

Compress the captured CO₂ for transport and geological sequestration.

05

Grid export

Sell surplus zero-emission electricity into the Alberta grid, subject to interconnection.

06

Facility upgrades

Upgrade the affected existing facilities so that they operate with zero stack emissions. design target

Integrated oxy-fuel power and carbon-management system Fuel gas and oxygen from an air separation unit are combusted in an oxy-fuel generator. The steam and carbon dioxide drive a turbine generator that supplies the facility and exports to the grid. After condensing, water is recovered and the carbon dioxide stream is compressed for storage or enhanced oil recovery. INPUTS GENERATION POWER DELIVERY CARBON MANAGEMENT Fuel gas Pipeline gas, low-BTU or CO₂-rich streams Air separation unit Oxygen supply, sized to the site Oxy-fuel generator Combustion in oxygen, not air: no nitrogen, low NOx Output: steam + CO₂ (licensed CES design) Turbine generator Steam-driven electrical output Facility loads Electrified compression, generators, plant Grid export Dispatchable supply, where interconnected Condenser Separates the exhaust stream Water Recovered CO₂ stream High purity Compression To pipeline or injection pressure Storage or EOR Geological storage or enhanced recovery Exhaust Power CO₂
Conceptual system configuration, not an engineering drawing of this site. The Alberta project proposes this arrangement at an existing plant; the actual configuration, capacities and interfaces are set during feasibility and FEED.
Progress

Milestones and dependencies

Completed

  • Host operator engaged and project scope described at concept level (published on valverdepowersolutions.com)
  • Technology basis stated: CES Direct Steam Gas Generation unit under Valverde’s master licence (published)
  • No further completed milestones have been publishedC02

Outstanding dependencies

  • Load, gas and site data sufficient for a scoped feasibility assessment
  • Oxygen supply configuration (on-site ASU sizing or over-the-fence supply)
  • Carbon destination: storage site, transport interface, pore-space and regulatory route
  • Alberta grid interconnection and export arrangements
  • Commercial model and development agreement between the host, Valverde and partners
  • Incentive determinations (CCUS ITC, TIER, other) for the specific project — professional review required

Next decision

Not yet published. When a next gate is announced, this page will show its date and the evidence it requires.C02

Responsibilities

Who does what

ElementResponsibleStatus
Project development, structuring, partner coordinationValverdeActive
Oxy-fuel technology, DSGG unitClean Energy Systems (licensor)Licensed
Host facility, site, fuel supplyHost operatorEngaged
Engineering (feasibility / FEED)To be appointedOpen
Oxygen supplyTo be appointedOpen
CO₂ transport and storageTo be appointedOpen
Power offtake / gridHost + AESO processOpen
Development and project capitalValverde and partnersCommercial model not published

“Open” means no counterparty has been publicly named for that element.C04

Technical evidence

How to read the numbers on this project

Every figure attached to this project is one of the following. Where a number is not yet available at that standard, we say so instead of implying completion or scale.

ItemEvidence status · sourceCurrent basis
Electrical outputnot publishedNo capacity figure has been published for this project. The CES oxy-fuel solution is described by the supplier as designed for roughly 10–100 MW per installation (design range, 2023).
CO₂ captureddesign target · Valverde / CESFull capture of combustion CO₂ from the oxy-fuel unit is the design intent. Denominator, downtime and bypass treatment would be defined in feasibility. No measured figure exists for this project.
Stack emissions after conversiondesign target · ValverdeZero stack emissions from the converted equipment is the target; residual emissions from any unconverted equipment are excluded from that statement.
Capital and operating costnot publishedNo cost figures have been published for this project. Comparisons with post-combustion capture are project-specific and belong in a feasibility study.
Fuelpublished scope · ValverdePipeline-quality gas at this site, per the published scope. Wider fuel-flexibility statements do not apply to this configuration.
Independent assessmentnot establishedNo independently assessed or measured results have been published for this project.C05

Sensitive models and contracts are shared with qualified counterparties in a controlled diligence environment, not through a public download.

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