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Oxy-Fuel Combustion

Burning fuel in pure oxygen to produce a concentrated COβ‚‚ flue stream β€” eliminating the need for post-combustion separation. Particularly compelling for India's cement kilns and coal boilers, where the high COβ‚‚ concentration in the flue gas directly reduces capture cost.

How It Works

Pure Oxygen Combustion β€” A Concentrated COβ‚‚ Stream Without Separation

TRL 7–8. Cement kilns and power boilers. Air separation unit is the key capital item.

Oxy-fuel combustion replaces the air used in conventional combustion with pure oxygen (95–99% Oβ‚‚ purity) produced by an Air Separation Unit (ASU). When fuel is burned in pure oxygen rather than air, the nitrogen that typically dilutes the flue gas to 10–15% COβ‚‚ is absent. The result is a flue gas consisting predominantly of COβ‚‚ and water vapour β€” typically 80–95% COβ‚‚ after water condensation β€” which requires no chemical separation step. The COβ‚‚ is simply dried and compressed for transport and storage.

A portion of the flue gas (typically 60–70%) is recycled back to the combustion chamber to moderate the flame temperature, which would otherwise be excessively high in pure oxygen. This recycle flue gas replaces the temperature-moderation function that nitrogen provides in air combustion. The net result is a process that produces a near-pure COβ‚‚ stream at essentially the same energy output as the original air-fired process, with an oxygen production energy penalty rather than a solvent regeneration energy penalty.

The primary capital cost driver for oxy-fuel combustion is the Air Separation Unit β€” a cryogenic distillation system that separates atmospheric air into oxygen, nitrogen, and argon streams. For large plants, the ASU is a proven, commercially available technology from Linde, Air Products, Air Liquide, and Praxair. The cost of oxygen production under Indian electricity prices β€” which vary significantly between grid power and captive coal generation β€” is the dominant economic variable in oxy-fuel feasibility assessments.

Oxy-Fuel for Cement Kilns
Cement kilns are particularly well-suited to oxy-fuel because the rotary kiln configuration allows retrofitting with an oxy-fuel burner while maintaining the existing kiln shell, pre-heater, and clinker cooler. The calcination COβ‚‚ from limestone is naturally co-captured in the concentrated flue stream.
Oxy-Fuel for Coal Boilers
Coal power boilers can be retrofitted for oxy-fuel by replacing burners and modifying the flue gas recycle system. The technology is closer to commercial scale than cement oxy-fuel, with the Callide Oxy-fuel Project in Australia providing the most comprehensive operational dataset.
Chemical Looping Combustion
An advanced variant of oxy-fuel where a metal oxide oxygen carrier transfers Oβ‚‚ to the fuel in a chemical loop β€” eliminating the ASU entirely. TRL 5–6 but approaching demonstration scale. NCM monitors development for Indian applicability.
Calcination Looping
Specifically designed for cement β€” captures COβ‚‚ from both the calcination reaction and fuel combustion in a single calcium looping process. Heidelberg Materials reference installation in Germany. High applicability to Indian dry-process cement kilns.
The Cement Case

Why Oxy-Fuel Is Compelling for India's Cement Industry

India is the world's second-largest cement producer at approximately 380 MT/year, and cement production is growing at 5–7% annually to support India's infrastructure development programme. Cement's COβ‚‚ emissions are uniquely challenging: approximately 60% comes from the chemical decomposition of limestone (calcination) β€” CaCO₃ β†’ CaO + COβ‚‚ β€” a reaction that cannot be avoided by fuel switching, electrification, or efficiency improvement. The only way to eliminate calcination COβ‚‚ is to capture it.

Oxy-fuel combustion is particularly attractive for cement because it captures both the calcination COβ‚‚ and the fuel combustion COβ‚‚ in a single concentrated stream, without requiring two separate capture systems. The Heidelberg Materials ANRAV project in Brevik, Norway β€” the world's first full-scale carbon capture plant at a cement factory β€” uses oxy-fuel-adjacent technology to capture 400,000 tonnes/year and provides the primary reference design that NCM uses for Indian cement feasibility assessments.

India's major cement producers β€” UltraTech (120 MT/year capacity), ACC, Shree Cement, Ambuja, Dalmia Bharat, and JK Cement β€” collectively represent one of the world's largest concentrations of cement production. The CBAM exposure for Indian cement exporters is significant, and NCM has conducted preliminary oxy-fuel screening assessments for facilities in Rajasthan, Andhra Pradesh, and Madhya Pradesh β€” India's primary cement production clusters.

380 MT

India's annual cement production β€” second largest globally and growing at 5–7%/year

60%

Share of cement COβ‚‚ from limestone calcination β€” unavoidable without carbon capture

95%

COβ‚‚ concentration in oxy-fuel flue gas after water removal β€” vs. 14–33% in conventional flue gas

TRL 7–8

Technology readiness at industrial demonstration scale β€” approaching commercial readiness

Global Reference

Oxy-Fuel Projects NCM Draws From

Each project provides specific lessons applied to Indian oxy-fuel feasibility and design.

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Callide Oxy-Fuel Project, Australia

The world's most comprehensive oxy-fuel coal power demonstration. 30 MW thermal oxy-fuel boiler. Demonstrated full cycle operability, ASU integration, and COβ‚‚ compression train performance. NCM's Australian operational team includes engineers who worked on Callide β€” lessons directly applied to Indian coal boiler assessments.

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Heidelberg Materials Brevik, Norway

World's first full-scale cement carbon capture installation. 400,000 t/year COβ‚‚ captured. Demonstrates industrial-scale oxy-fuel-adjacent technology for the global cement sector β€” primary reference for NCM's Indian cement oxy-fuel feasibility work.

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Schwartze Pumpe, Germany

Vattenfall's oxy-fuel pilot plant β€” the first demonstration of oxy-fuel technology on a coal power plant connected to the electricity grid. Key data source for NCM's coal power oxy-fuel retrofit assessments.

NCM Approach

Oxy-Fuel Feasibility for Indian Industrial Sites

NCM's oxy-fuel feasibility assessments begin with a detailed energy integration study β€” because the ASU electricity consumption is the dominant variable in oxy-fuel economics under Indian conditions. We evaluate three electricity supply scenarios for each site: grid power at state industrial tariff, dedicated captive coal power, and waste heat recovery from the host industrial process. The optimal scenario varies significantly by site and location.

For cement plants, NCM evaluates both full oxy-fuel kiln retrofit and partial oxy-fuel options β€” where the kiln calciner is converted to oxy-fuel (capturing the 60% calcination COβ‚‚) while the main kiln continues on air-fired operation. This partial oxy-fuel approach can reduce capital cost by 35–45% compared to full kiln conversion while still capturing the majority of cement's unavoidable process emissions.

All oxy-fuel assessments are integrated with NCM's storage advisory β€” because oxy-fuel produces a high-purity COβ‚‚ stream with minimal impurities, it has specific compression train design requirements and COβ‚‚ quality specifications that differ from post-combustion capture streams. Our end-to-end advisory ensures that capture, compression, transport, and storage system specifications are consistent from the outset.

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