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The A3C plant comprises the following steps:

  • Energy recovery uses the high temperatures of the exhaust gases to provide energy to drive the separation process.
  • Gas cleaning of gases removes traces of sulphur oxides and particulates in a low temperature scrubber.
  • Drying and cooling reduces the water content to extremely low levels followed by a high-performance recuperative heat exchanger to cool the dry gases further. Efficient heat recovery techniques minimise refrigeration duty.
  • Separation chills the gases sufficiently to freeze carbon dioxide onto a capture medium. This stage uses high intensity heat and mass transfer to capture carbon dioxide in a bed of capture medium only 200 mm deep.
  • Liquid carbon dioxide is recovered from the capture medium without a separate liquefication train.
  • An advanced and highly efficient refrigeration cascade provides the cooling for the separation process.
  • The process inherently delivers extremely pure liquid carbon dioxide, meeting the exacting requirements of geological storage and reuse processes without further treatment.
  • While the separation can achieve capture rates of up to 99%, for most applications rates above 90-95% are unlikely to be viable. Constraints on carbon dioxide storage for some applications may limit practical capture rates but this will not degrade energy efficiency.