Increasing the Selectivity for Sulfur Formation in Biological Gas Desulfurization

Journal Article (2019)
Authors

Rieks De Rink (Paqell B.V., Wageningen University & Research)

Johannes B.M. Klok (Paqell B.V., Wetsus, European Centre of Excellence for Sustainable Water Technology)

Gijs J. Van Heeringen (Paqell B.V.)

D. Sorokin (Russian Academy of Sciences, OLD BT/Cell Systems Engineering, TU Delft - BT/Environmental Biotechnology)

Annemiek ter Heijne (Wageningen University & Research)

Remco Zeijlmaker (Det Norske Veritas)

Yvonne M. Mos (Wageningen University & Research)

Vinnie De Wilde (Wageningen University & Research)

Karel J. Keesman (Wageningen University & Research)

Cees J.N. Buisman (Wetsus, European Centre of Excellence for Sustainable Water Technology, Wageningen University & Research)

Research Group
BT/Environmental Biotechnology
Copyright
© 2019 Rieks De Rink, Johannes B.M. Klok, Gijs J. Van Heeringen, Dimitry Y. Sorokin, Annemiek Ter Heijne, Remco Zeijlmaker, Yvonne M. Mos, Vinnie De Wilde, Karel J. Keesman, Cees J.N. Buisman
To reference this document use:
https://doi.org/10.1021/acs.est.8b06749
More Info
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Publication Year
2019
Language
English
Copyright
© 2019 Rieks De Rink, Johannes B.M. Klok, Gijs J. Van Heeringen, Dimitry Y. Sorokin, Annemiek Ter Heijne, Remco Zeijlmaker, Yvonne M. Mos, Vinnie De Wilde, Karel J. Keesman, Cees J.N. Buisman
Research Group
BT/Environmental Biotechnology
Issue number
8
Volume number
53
Pages (from-to)
4519-4527
DOI:
https://doi.org/10.1021/acs.est.8b06749
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Abstract


In the biotechnological desulfurization process under haloalkaline conditions, dihydrogen sulfide (H
2
S) is removed from sour gas and oxidized to elemental sulfur (S
8
) by sulfide-oxidizing bacteria. Besides S
8
, the byproducts sulfate (SO
4

2-
) and thiosulfate (S
2
O
3

2-
) are formed, which consume caustic and form a waste stream. The aim of this study was to increase selectivity toward S
8
by a new process line-up for biological gas desulfurization, applying two bioreactors with different substrate conditions (i.e., sulfidic and microaerophilic), instead of one (i.e., microaerophilic). A 111-day continuous test, mimicking full scale operation, demonstrated that S
8
formation was 96.6% on a molar H
2
S supply basis; selectivity for SO
4

2-
and S
2
O
3

2-
were 1.4 and 2.0% respectively. The selectivity for S
8
formation in a control experiment with the conventional 1-bioreactor line-up was 75.6 mol %. At start-up, the new process line-up immediately achieved lower SO
4

2-
and S
2
O
3

2-
formations compared to the 1-bioreactor line-up. When the microbial community adapted over time, it was observed that SO
4

2-
formation further decreased. In addition, chemical formation of S
2
O
3

2-
was reduced due to biologically mediated removal of sulfide from the process solution in the anaerobic bioreactor. The increased selectivity for S
8
formation will result in 90% reduction in caustic consumption and waste stream formation compared to the 1-bioreactor line-up.