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Integration of gas switching combustion in a humid air turbine cycle for flexible power production from solid fuels with near‐zero emissions of CO2 and other pollutants

Sammendrag

This work presents a novel plant configuration for power production from solid fuels with integrated CO2 capture. Specifically, the Gas Switching Combustion (GSC) system is integrated with a Humid Air Turbine (HAT) power cycle and a slurry fed entrained flow (GE‐Texaco) gasifier or a dry fed (Shell) gasifier with a partial water quench. The primary novelty of the proposed GSC‐HAT plant is that the reduction and oxidation reactor stages of the GSC operation can be decoupled allowing for flexible operation, with the oxygen carrier serving as a chemical and thermal energy storage medium. This can allow the air separation unit, gasifier, gas clean‐up, CO2 compressors and downstream CO2 transport and storage network to be downsized for operation under steady state conditions, while the reactors and the power cycle operate flexibly to follow load. Such cost‐effective flexibility will be highly valued in future energy systems with high shares of variable renewable energy. The GSC‐HAT plant achieves 42.5% electrical efficiency with 95.0% CO2 capture rate with the Shell gasifier, and 41.6% efficiency and 99.2% CO2 capture with the GE gasifier. An exergy analysis performed for the GE gasifier case revealed that this plant reached 38.9% exergy efficiency, only 1.6%‐points below an inflexible GSC‐IGCC benchmark configuration, while reaching around 5%‐points higher CO2 capture rate. Near‐zero SOx and NOx emissions are achieved through pre‐combustion gas clean‐up and flameless fuel combustion. Overall, this flexible and efficient near‐zero emission power plant appears to be a promising alternative in a future carbon constrained world with increasing shares of variable renewables and more stringent pollutant (NOx, SOx) regulations.

Kategori

Vitenskapelig artikkel

Oppdragsgiver

  • Research Council of Norway (RCN) / 276321

Språk

Engelsk

Forfatter(e)

Institusjon(er)

  • Universidad Politécnica de Madrid
  • SINTEF Industri / Prosessteknologi

År

2020

Publisert i

International Journal of Energy Research

ISSN

0363-907X

Forlag

John Wiley & Sons

Årgang

44

Side(r)

7299 - 7322

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