Flue Gas & Capture
Duct interfaces, conditioning systems, absorber/stripper equipment, solvent piping and heat-recovery connections.
Integrated thermal insulation engineering for carbon capture and CCUS facilities—from solvent-regeneration systems and CO₂ compression trains to refrigerated liquid-CO₂ storage, export terminals and transportation pipelines.
A CCUS project may combine high-temperature heat recovery, solvent-regeneration duty, compression and intercooling, dehydration, refrigerated storage, dense-phase transport and injection facilities. Each part requires a different insulation basis.
Duct interfaces, conditioning systems, absorber/stripper equipment, solvent piping and heat-recovery connections.
Reboilers, steam and condensate, rich/lean solvent networks, exchangers, vessels and temperature-sensitive services.
Compressor discharge, interstage cooling, separators, dehydration, refrigeration and high-pressure export systems.
Refrigerated liquid-CO₂ tanks, loading systems, pipelines, terminals, booster stations and injection interfaces.
The complete pressure–temperature envelope matters. A design based only on normal operating temperature may miss the most demanding thermal or moisture-control case.
One facility can contain hot solvent regeneration, high compressor-discharge temperatures, cooled separators and low-temperature liquid-CO₂ services.
Thermal cycling and depressurisation may impose temperatures and movement different from steady-state operation.
CO₂ purity, water and impurities affect phase behaviour; insulation decisions must align with process and flow-assurance analyses.
Cold surfaces, supports and penetrations require continuous vapour control and carefully sealed weather-protection details.
Coating, insulation, cladding, drainage, removable sections and inspection planning work together to manage corrosion under insulation.
Maintainability, vibration, acoustic requirements and repeated access influence removable-cover and local support design.
Capture facilities can include flue-gas conditioning, absorber and stripper columns, reboilers, solvent heat exchangers, rich/lean solvent piping, steam and condensate systems, separators and heat-recovery interfaces. The insulation design should follow the required process temperature, energy target, condensation risk and operating mode.
Heat loss from stripper, reboiler, steam and hot-solvent services can increase the energy required by the regeneration system. Conversely, some absorber or conditioning equipment may not require full insulation in every project. The duty must be demonstrated rather than assumed.
Compression trains create several distinct insulation duties: hot compressor-discharge piping, interstage systems, intercoolers and aftercoolers, knockout drums, separators, dehydration units, regeneration equipment and high-pressure export piping.
Thermal requirements may also intersect with vibration, noise, inspection frequency and rapid component access. Removable insulation jackets can be engineered for selected valves, flanges, strainers and equipment items without treating them as generic one-size-fits-all covers.
CO₂ liquefaction units, refrigeration equipment, buffer and storage tanks, loading lines, pumps, valves, manifolds and ship-loading connections require a low-temperature system that limits heat ingress and controls condensation and vapour ingress.
Depending on the approved design conditions, potential system directions may include cellular glass, PIR/PUR, flexible aerogel-based products, suitable elastomeric systems, multi-layer cold-insulation assemblies, low-permeance vapour retarders, protective cladding and load-bearing insulation inserts.
Pipeline insulation must be justified by hydraulic, flow-assurance, integrity and transient analyses—not copied from conventional oil and gas service.
CO₂ purity, moisture and impurities influence corrosion risk, phase behaviour and the pressure–temperature envelope used by the process team.
Ambient heat transfer, pressure drop and operating cases are reviewed against the approved flow-assurance model and phase-boundary criteria.
Air, soil or seawater temperature, solar exposure, wind, burial conditions, coatings and external protection affect the thermal design.
Warm-up, cool-down, stagnant conditions, restart, turndown and pressure changes can govern the required thermal response.
Thermal expansion, shoes, anchors, field joints, water shedding, coating and inspection access are coordinated with any external insulation.
Some dense-phase CO₂ pipelines may not require external insulation. Unnecessary insulation can add cost, complexity and CUI exposure.
Rapid pressure reduction can create severe local cooling. This condition is assessed with process safety, flow-assurance, piping and materials engineering—not by insulation selection alone.
| Engineering Issue | Why It Matters | Insulation Interface | Required Coordination |
|---|---|---|---|
| Rapid Decompression Cooling | Temperature can fall sharply during blowdown, relief or loss of pressure. | Evaluate layer temperatures, contraction, local exposure and system behaviour during the defined event. | Process safety, dynamic simulation, piping and materials teams. |
| Dry-Ice Formation | Solid CO₂ may form in relevant pressure–temperature conditions and affect flow or equipment operation. | Do not claim that added insulation eliminates the risk; use approved depressurisation analysis. | Process, flow assurance, operations and relief-system design. |
| Minimum Metal Temperature | Low local metal temperature can challenge material toughness and design limits. | Thermal response may be one input, but metallurgy and code compliance govern acceptance. | Materials, mechanical integrity and equipment/piping code owners. |
| Valves and Restrictions | Pressure-drop locations can create local low-temperature zones and thermal cycling. | Use project-specific removable, vapour-controlled or protective details where approved. | Process, valve vendor, piping and maintenance teams. |
| Personnel Exposure | Cold surfaces, venting and CO₂ release can create contact and atmospheric hazards. | Surface protection is only one control within the facility’s complete HSE strategy. | HSE, process safety, ventilation and operations teams. |
Final acceptance criteria, event duration and design temperatures must come from the approved project safety and process basis.
A robust system coordinates the substrate coating, insulation, vapour retarder where required, cladding, sealants, fasteners, supports, penetrations, drainage and inspection strategy. No single insulation material can guarantee CUI prevention.
The scope can be delivered as consultancy, detail engineering, supply, installation, QA/QC or an integrated package.
Applicable editions and contractual precedence must be confirmed for each project.
ERATHERM brings industrial thermal, cold and cryogenic insulation experience to CCUS projects through engineering, material selection, detail design, application and QA/QC. The final system is developed around approved project data—not generic sustainability claims.
Share the process data, pressure–temperature cases, equipment and line lists, drawings, specifications and project objectives. ERATHERM can structure the engineering, supply, application and QA/QC package around the facility’s actual operating envelope.
Final insulation materials, thicknesses, layer sequence, vapour-control strategy, coating, cladding, support details, transient criteria, surface-temperature targets, fire or acoustic requirements, inspection plan, quality controls and applicable standards are project-specific. They must be confirmed against the contract, approved process and flow-assurance basis, equipment and piping data, drawings, manufacturer information, HSE requirements, environmental exposure and maintenance programme. References on this page provide an engineering framework and do not imply that every standard applies to every project.
