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Conversion of Waste Synthesis Gas to Desalination Catalyst at Ambient Temperatures

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  • David D. J. Antia

    (DCA Consultants Ltd., The Bungalow, Castleton Farm, Falkirk FK2 8SD, UK)

Abstract

In this study, a continuous flow of a synthetic, dry, and acidic waste synthesis gas (WSG) (containing N 2 , H 2 , CO, CH 4 , and CO 2 ) at ambient temperatures was first passed through a fixed bed reactor (FBR) containing halite + m-Fe 0 and then a saline bubble column diffusion reactor (BCDR) containing m-Fe 0 . The FBR converted 47.5% of the CO + CH 4 + CO 2 into n-C 0 . Passage of the n-C 0 into the BCDR resulted in the formation of the desalination catalyst (Fe 0 :Fe(a,b,c)@C 0 ) + CH 4 + CO + CO 2 + C x H y , where 64% of the feed n-C 0 was converted to gaseous products. The desalination pellets can remove >60% of the water salinity without producing a reject brine or requiring an external energy source. The gaseous products from the BCDR included: C x H y (where x < 6), CO, CO 2 , and H 2 .

Suggested Citation

  • David D. J. Antia, 2023. "Conversion of Waste Synthesis Gas to Desalination Catalyst at Ambient Temperatures," Waste, MDPI, vol. 1(2), pages 1-29, May.
    • Handle: RePEc:gam:jwaste:v:1:y:2023:i:2:p:26-454:d:1137788
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    References listed on IDEAS

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