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Title: Biological sulfate reduction using gas-lift reactors fed with hydrogen and carbon dioxide as energy and carbon source

Journal Article · · Biotechnology and Bioengineering; (United States)
; ;  [1]
  1. Wageningen Agricultural Univ. (Netherlands). Dept. of Environmental Technology

Feasibility and engineering aspects of biological sulfate reduction in gas-lift reactors were studied. Hydrogen and carbon dioxide were used as energy and carbon source. Attention was paid to biofilm formation, sulfide toxicity, sulfate conversion rate optimization, and gas-liquid mass transfer limitations. Sulfate-reducing bacteria formed stable biofilms on pumice particles. Biofilm formation was not observed when basalt particles were used. However, use of basalt particles led to the formation of granules of sulfate-reducing biomass. The sulfate-reducing bacteria, grown on pumice, easily adapted to free H[sub 2]S concentrations up to 450 mg/L. Biofilm growth rate then equilibrated biomass loss rate. These high free H[sub 2]S concentrations caused reversible inhibition rather than acute toxicity. When free H[sub 2]S concentrations were kept below 450 mg/L, a maximum sulfate conversion rate of 30 g SO[sub 4][sup 2[minus]]/L [center dot] d could be achieved after only 10 days of operation. Gas-to-liquid hydrogen mass transfer capacity of the reactor determined the maximum sulfate conversion rate.

OSTI ID:
7145371
Journal Information:
Biotechnology and Bioengineering; (United States), Vol. 44:5; ISSN 0006-3592
Country of Publication:
United States
Language:
English