Biological sulphide oxidation in a fed-batch reactor
- Agricultural Univ. Wageningen (Netherlands)
This study shows that, in a sulphide-oxidizing bioreactor with a mixed culture of Thiobacilli, the formation of sulphur and sulphate as end-products from the oxidation of sulphide can be controlled instantaneously and reversibly by the amount of oxygen supplied. It was found that at sulphide loading rates of up to 2.33 mmol/L {center_dot} h, both products can be formed already at oxygen concentrations below 0.1 mg/L. Because the microorganisms tend to form sulphate rather than forming sulphur, the oxygen concentration is not appropriate to optimize the sulphur production. Within less than 2 h, the system can be switched reversibly from sulphur to sulphate formation by adjusting the oxygen flow. This is below the minimum doubling time (2.85 h) of, e.g., Thiobacillus neapolitanus and Thiobacillus O,{sup 18} which indicates that one metabolic type of organism can probably perform both rations. Under highly oxygen-limited circumstances, that is, at an oxygen/sulphide consumption ratio below 0.7 mol {center_dot} h{sup {minus}1}/mol {center_dot} h{sup {minus}1}, thiosulphate is abundantly formed. Because the chemical sulphide oxidation results mainly in the formation of thiosulphate, it is concluded that, under these circumstances, the biological oxidation capacity of the system is lower than the chemical oxidation capacity. The oxidation rate of the chemical sulphide oxidation can be described by a first-order process (k = {minus}0.87 h{sup {minus}1}).
- Sponsoring Organization:
- USDOE
- OSTI ID:
- 99397
- Journal Information:
- Biotechnology and Bioengineering, Vol. 47, Issue 3; Other Information: PBD: 5 Aug 1995
- Country of Publication:
- United States
- Language:
- English
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