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Pilot‐scale evaluation of concentrated piperazine for CO 2 capture at an Australian coal‐fired power station: duration experiments

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  • Ashleigh Cousins
  • Paul Nielsen
  • Sanger Huang
  • Aaron Cottrell
  • Eric Chen
  • Gary T Rochelle
  • Paul H M Feron

Abstract

Duration operation was completed as the final stage of evaluating concentrated piperazine as a CO 2 capture solvent at the Tarong pilot plant. For the duration tests, a single operating set‐point was maintained for an extended period of time. The purpose of the duration tests was to monitor the formation of degradation products and the robustness of the solvent. Two duration tests were conducted that differed only in the regeneration temperature used (125 or 155 °C). Four hundred twenty‐five hours of operation were achieved on the solvent with a regeneration temperature of 125 °C. This was followed by a further 421 h of operation with a regeneration temperature of 155 °C, giving a total operating time on the solvent of 1700 h by the end of the project. For the duration experiments, roughly 500 tonnes of flue gas was treated, and approximately 70 tonnes of CO 2 captured. The heat stable salt (HSS) measured in highest concentration was formate, with the rate of formation increasing with regeneration temperature. The effect of pre‐treatment could be seen with sulfate concentration in the solvent increasing sharply when caustic supply to the pre‐treatment column was interrupted. Despite the formation of degradation products in the solvent regeneration energy requirements were not notably effected. For operation up to 1700 h on a real coal flue gas, no loss of plant performance was observed. © 2015 Society of Chemical Industry and John Wiley & Sons, Ltd

Suggested Citation

  • Ashleigh Cousins & Paul Nielsen & Sanger Huang & Aaron Cottrell & Eric Chen & Gary T Rochelle & Paul H M Feron, 2015. "Pilot‐scale evaluation of concentrated piperazine for CO 2 capture at an Australian coal‐fired power station: duration experiments," Greenhouse Gases: Science and Technology, Blackwell Publishing, vol. 5(4), pages 363-373, August.
  • Handle: RePEc:wly:greenh:v:5:y:2015:i:4:p:363-373
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    File URL: http://hdl.handle.net/10.1002/ghg.1507
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    References listed on IDEAS

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    1. Ashleigh Cousins & Sanger Huang & Aaron Cottrell & Paul H.M. Feron & Eric Chen & Gary T. Rochelle, 2015. "Pilot‐scale parametric evaluation of concentrated piperazine for CO 2 capture at an Australian coal‐fired power station," Greenhouse Gases: Science and Technology, Blackwell Publishing, vol. 5(1), pages 7-16, February.
    2. Ashleigh Cousins & Aaron Cottrell & Anthony Lawson & Sanger Huang & Paul H.M. Feron, 2012. "Model verification and evaluation of the rich‐split process modification at an Australian‐based post combustion CO 2 capture pilot plant," Greenhouse Gases: Science and Technology, Blackwell Publishing, vol. 2(5), pages 329-345, October.
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    1. Yu, Cheng-Hsiu & Chen, Ming-Tsz & Chen, Hao & Tan, Chung-Sung, 2016. "Effects of process configurations for combination of rotating packed bed and packed bed on CO2 capture," Applied Energy, Elsevier, vol. 175(C), pages 269-276.
    2. Paul H.M. Feron & Ashleigh Cousins & Shiwang Gao & Lianbo Liu & Jinyi Wang & Shiqing Wang & Hongwei Niu & Hai Yu & Kangkang Li & Aaron Cottrell, 2017. "Experimental performance assessment of a mono‐ethanolamine‐based post‐combustion CO 2 ‐capture at a coal‐fired power station in China," Greenhouse Gases: Science and Technology, Blackwell Publishing, vol. 7(3), pages 486-499, June.

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