2012
DOI: 10.1016/s1001-0742(11)60799-7
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Sulfide oxidation in fluidized bed bioreactor using nylon support material

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Cited by 16 publications
(13 citation statements)
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“…Production of S 0 was reduced when DO concentration increased. With inoculation under DO concentration of 0.05-0.15 mg/L, S 0 production was higher than remaining SO 4 2--S. However, when DO concentration was up to 0.15-0.30 mg/L, the main sulfur compound in batch experiment was SO 4 2--S. Reference [8] reported that at DO less than 0.1 mg/L, S 0 was the main product of the sulfide oxidation process. They also explained that production of S 0 by SOB decreased at high DO concentration [8].…”
Section: B Effect Of Do On Specific Microbial Activities and Metabolmentioning
confidence: 89%
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“…Production of S 0 was reduced when DO concentration increased. With inoculation under DO concentration of 0.05-0.15 mg/L, S 0 production was higher than remaining SO 4 2--S. However, when DO concentration was up to 0.15-0.30 mg/L, the main sulfur compound in batch experiment was SO 4 2--S. Reference [8] reported that at DO less than 0.1 mg/L, S 0 was the main product of the sulfide oxidation process. They also explained that production of S 0 by SOB decreased at high DO concentration [8].…”
Section: B Effect Of Do On Specific Microbial Activities and Metabolmentioning
confidence: 89%
“…Synthetic wastewater was prepared to simulate concentrated latex wastewater by using lactic acid, anhydrous sodium sulfate (Na 2 SO 4 ) and ammonium chloride (NH 4 Cl) as sources of carbon, sulfate and ammonium nitrogen, respectively [6], [9]. In the reactor, SO 4 2-, NH 4 + -N and COD was added to an initial concentration of 1,000, 222.2 and 4,000 mg/L respectively as shown in Table I. The influent pH value was maintained at 7.0 by dosing NaOH [9].…”
Section: A Seeding Sludge and Synthetic Wastewatermentioning
confidence: 99%
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