Executive Summary
Scaling carbon capture, utilisation and storage (CCUS) requires a rapid build-out of CO₂ transport infrastructure. Repurposing existing natural gas pipelines can significantly reduce lead time and upfront CAPEX relative to new CO₂ corridors where assets meet integrity and routing requirements, but it is not universally suitable. In practice, technical feasibility and economics depend on detailed assessments of materials, pressure regimes, impurities and regulatory classifications, drawing on benchmark CO₂ transport studies in Europe and other regions.
At
Energy Solutions,
we evaluate when repurposing provides a technically robust, cost-efficient option and when new-build CO₂ pipelines remain the lower‑risk choice for long-term CCUS networks.
- Indicative transport costs for large-diameter onshore CO₂ pipelines are typically in the range of 10–25 USD/tCO₂ over distances of 100–300 km for well-utilised lines, broadly consistent with cost bands reported in recent European CCUS transport assessments; offshore routes and low-utilisation projects can sit significantly higher.
- Repurposing gas pipelines can reduce CAPEX by 20–50% relative to new-build lines in favourable cases, with some studies indicating higher savings for specific configurations, but substantial modifications (valves, compressors, materials upgrades and conditioning systems) are often required to safely handle dense-phase CO₂ and impurities.
- Technical feasibility is highest for relatively young, well-documented pipelines with suitable steel grades, weld qualities, coatings and rights-of-way, and where operating pressure envelopes can accommodate dense-phase conditions typically in the 80–150 bar range for large-volume transport.
- Key risks include material degradation from CO₂ and water (corrosion), running ductile fracture in dense-phase operation, and potential changes in regulatory classification when moving from hydrocarbon to CO₂ service, including new requirements for monitoring and liability allocation.
- Energy Solutions modelling suggests that in mature gas networks with declining throughput, carefully selected pipeline segments can be repurposed to create cost-efficient CO₂ corridors—provided that integrity assurance, gas-quality management and long-term liability frameworks are addressed from the outset.
Basics: CO₂ Transport Needs in a CCUS World
Large-scale CCUS deployment requires moving tens to hundreds of millions of tonnes of CO₂ per year from capture sites to storage or utilisation locations, in line with net-zero pathways that foresee multi‑gigaton deployment of CCUS by mid-century. In some systems, point-to-point projects can rely on dedicated pipelines, but many regions are planning shared CO₂ backbones collecting flows from multiple industrial clusters and power plants.
Existing natural gas networks often have spare capacity due to efficiency improvements, demand shifts or energy transition dynamics. This raises a practical question for system operators: can some of these pipelines be converted to CO₂ service to reduce the cost and lead time of creating CO₂ corridors, while meeting safety and regulatory requirements?
Technical Foundation: CO₂ vs Natural Gas Pipeline Behaviour
CO₂ has very different physical properties from natural gas, particularly when transported in dense-phase (supercritical) conditions to maximise capacity and reduce compression costs. Design envelopes therefore differ from legacy gas service and must reflect phase behaviour, impurities and fracture control for the expected operating window.
- Phase behaviour: Dense-phase CO₂ behaves more like a liquid than a gas, affecting pressure drop, leak behaviour and fracture propagation.
- Impurities: Water, H₂S, O₂ and other components can significantly influence corrosion and phase envelope, requiring strict specification and conditioning at entry points.
- Temperature/pressure envelopes: To stay in dense phase, CO₂ is typically transported at pressures between 80–150 bar, depending on temperature and composition; this often differs from prior gas operating regimes and may exceed original design conditions for some assets.
Indicative Operating Envelopes: Natural Gas vs Dense-Phase CO₂ Pipelines
| Parameter |
Typical Natural Gas Pipeline |
Dense-Phase CO₂ Pipeline |
| Operating Pressure |
30–80 bar |
80–150 bar |
| Fluid State |
Compressible gas |
Dense-phase (near liquid-like) |
| Key Integrity Concern |
Fatigue, corrosion |
Corrosion with water, running fracture |
Stylised Pressure-Temperature Envelope for CO₂ Transport
The chart below illustrates a simplified view of operating envelopes for gaseous vs dense-phase CO₂ and typical pipeline operating windows. It is indicative rather than a substitute for project-specific thermodynamic analysis.
Source: Energy Solutions interpretation of CO₂ phase behaviour (indicative only).
Benchmarks & Cost Data: New-Build vs Repurposed Lines
Cost comparisons between new-build and repurposed pipelines depend heavily on context, but some indicative benchmarks are possible and broadly align with ranges reported in major European CO₂ transport cost studies for onshore networks of comparable scale.
Indicative Cost Benchmarks for Onshore CO₂ Pipelines (2027, Stylised)
| Option |
Capacity |
Distance |
CAPEX Range |
Indicative Transport Cost |
| New-Build CO₂ Pipeline |
5–10 MtCO₂/year |
150–300 km |
400–900 million USD |
15–30 USD/tCO₂ |
| Repurposed Gas Pipeline (Favourable Case) |
3–8 MtCO₂/year |
150–300 km |
200–500 million USD |
10–20 USD/tCO₂ |
| Repurposed Network Segment (Complex Upgrades) |
2–6 MtCO₂/year |
150–300 km |
300–700 million USD |
15–28 USD/tCO₂ |
Values exclude compression at capture sites and injection wells. Actual costs vary widely with terrain, permitting, material upgrades and utilisation, and should be cross-checked against regional benchmarks from recent CO₂ network studies before investment decisions.
Transport Cost per tCO₂ vs Utilisation (Stylised)
The bar chart below shows how under-utilisation can increase transport costs for both new-build and repurposed pipelines, illustrating the importance of securing stable throughput for cost-effective backbone development.
Source: Energy Solutions CO₂ transport cost model (illustrative).
Integrity & Safety: Corrosion, Fracture and Impurity Management
Material integrity is a central concern when converting gas pipelines to CO₂ service. Operators must address the interaction between CO₂, water and impurities, and verify that steel toughness and wall thickness are adequate for dense-phase operating envelopes and potential decompression events.
- Corrosion with water: CO₂ and water form carbonic acid; even low water content can lead to accelerated internal corrosion without appropriate materials selection and dehydration.
- Running ductile fracture: Dense-phase CO₂ releases large amounts of stored energy; fracture arrest requires careful analysis of steel toughness, wall thickness and crack propagation behaviour, often using dedicated fracture control models.
- Impurities: H₂S, SOx and NOx can exacerbate corrosion and influence phase envelope; strict gas quality management, dehydration and, where needed, corrosion-resistant materials are mandatory.
Case Studies: Onshore Gas Network Conversion and Industrial Clusters
Case Study 1 – Partial Conversion of a Regional Gas Pipeline
A declining onshore gas region with an existing 250 km, 36" gas transmission pipeline explores repurposing one parallel string for CO₂ transport from industrial clusters to a storage hub.
- Initial findings: Steel grade and weld quality considered acceptable; limited historical corrosion; rights-of-way suitable for CO₂ service.
- Upgrades: Valve replacements, installation of crack arrestors, additional block valves and enhanced monitoring.
- Economics: CAPEX estimated at 260–350 million USD vs 450–650 million USD for new-build, yielding transport costs of 12–20 USD/tCO₂ at 75% utilisation.
Case Study 2 – Industrial Cluster CO₂ Network Using Mixed New-Build and Repurposed Segments
A coastal industrial cluster (steel, cement, chemicals) aggregates CO₂ volumes of 8–10 MtCO₂/year for offshore storage. The project uses a repurposed onshore gas trunk for part of the route and a new-build offshore segment.
- Onshore segment: Repurposed 40 km pipeline, moderate upgrades required.
- Offshore segment: New 120 km CO₂ line to storage site.
- Overall transport cost: 18–26 USD/tCO₂, with repurposed section contributing ~30% of combined CAPEX savings relative to full new-build.
The case shows that hybrid solutions can leverage existing infrastructure where appropriate while acknowledging that new-build offshore lines are often unavoidable for access to deep storage.
Regulation & Liability: Reclassification and Long-Term Stewardship
Repurposing pipelines requires navigating regulatory frameworks that were often written with hydrocarbon transport in mind. Key questions include how CO₂ is classified, which codes apply, and how monitoring and verification obligations evolve over the asset life.
- How is CO₂ classified (hazardous substance, gas, waste) in the relevant jurisdiction?
- Which safety codes and design standards apply to converted lines, and do they explicitly cover dense-phase CO₂?
- Who holds long-term liability for potential leaks or damage after storage sites are closed and pipelines are mothballed or re-used?
Clear frameworks for permitting, monitoring and liability transfer are critical for investment decisions, particularly for cross-border projects and multi-user networks.
Indicative Allocation of CO₂ Transport Cost Components
The chart below shows a stylised breakdown of pipeline CAPEX, compression, OPEX and monitoring contributions to total transport cost; in many real projects, pipeline CAPEX dominates even more strongly, especially for long onshore routes.
Source: Energy Solutions CO₂ infrastructure cost breakdown (illustrative).
Devil's Advocate: Lock-in, Capacity Mismatch and Social Acceptance
There are strong reasons to be cautious about widespread repurposing, even where individual assets appear technically suitable.
- Infrastructure lock-in: Converting gas pipelines to CO₂ service may foreclose other uses (e.g., hydrogen) or complicate future network reconfiguration.
- Capacity mismatch: Pipelines sized and routed for gas flows may not optimally match emerging CO₂ source–sink patterns and may underperform if volumes remain below design.
- Public perception: Communities may view CO₂ pipelines differently from gas pipelines; safety incidents or poor communication could undermine social licence.
- Data limitations: Older assets may lack comprehensive records of materials and defects, increasing uncertainty in safety assessments and driving conservative assumptions on allowable operating windows.
These factors imply that repurposing is best targeted to assets with strong data quality and clear long‑term roles in regional decarbonisation plans, rather than being a blanket strategy for entire gas networks.
Outlook to 2030/2035: CO₂ Backbone Networks and Hydrogen Overlaps
By 2035, several regions are likely to have established multi-user CO₂ transport networks, with corridor designs increasingly co-optimised with hydrogen backbones, high-voltage cables and other critical infrastructure. This creates opportunities to use rights-of-way efficiently but also raises competition between energy carriers.
Strategic planning at the national and regional level can help minimise regret investments, for example by:
- Designing corridors that can accommodate multiple lines (CO₂, hydrogen, power cables).
- Prioritising repurposing for sections unlikely to be needed for hydrogen or other higher-value uses.
- Embedding flexibility into route design and capacity planning, including options for twinning or staged expansion.
Implementation Guide: Screening Framework for Pipeline Repurposing
For TSOs, midstream companies and industrial clusters, a structured screening framework improves decision quality and clarifies where repurposing is justified relative to new-build options.
- Asset inventory: Catalogue candidate pipelines with data on age, materials, wall thickness, weld quality, pressure history and inspection records.
- Preliminary suitability scoring: Screen assets against high-level criteria (diameter, route relevance, regulatory constraints).
- Detailed integrity assessment: For shortlisted assets, perform fracture control studies, corrosion assessments and impurity management analysis.
- Scenario comparison: Compare repurposing vs new-build options under different utilisation and policy scenarios, including hydrogen corridor considerations.
- Stakeholder alignment: Engage regulators, communities and potential users early to clarify safety expectations, access rules and governance.
- Phased implementation: Consider pilot segments to validate assumptions and measurement methodologies before large-scale network conversion.
Methodology note: All cost and performance values in this article are stylised and indicative, based on public CO₂ transport studies (including major European cost assessments for onshore and offshore networks), gas pipeline benchmarks and Energy Solutions modelling. Project-specific engineering, regulatory and market assessments are essential before committing capital and should reference the most recent regional studies where available.