Analysis of immobilized cell bioreactors for desulfurization of flue gases and sulfite/sulfate-laden wastewater

Sulfur dioxide (SO₂) is one of the major pollutantsin the atmosphere that cause acid rain. Microbialprocesses for reducing SO₂ to hydrogen sulfide(H₂S) have previously been demonstrated byutilizing mixed cultures of sulfate-reducing bacteria(SRB) with municipal sewage digest as the carbon andenergy source. To maximize the productivity of theSO₂-reducing bioreactor in this study, variousimmobilized cell bioreactors were investigated: a stirredtank with SRB flocs and columnar reactors with cellsimmobilized in either -carrageenan gel matrix orpolymeric porous BIO-SEP^TM beads. Themaximum volumetric productivity for SO₂reduction in the continuous stirred-tank reactor (CSTR)with SRB flocs was 2.1 mmol SO₂/h·l. The-carrageenan gel matrix used for cellimmobilization was not durable at feed sulfiteconcentrations greater than 2000 mg/l or at sulfite feedrate of 1.7 mmol/h·l. A columnar reactor withmixed SRB cells that had been allowed to grow intohighly stable BIO-SEP polymeric beads exhibited thehighest sulfite conversion rates, in the range of16.5 mmol/h·l (with 100% conversion) to20 mmol/h·l (with 95% conversion). In addition toflue gas desulfurization, potential applications of thismicrobial process include the treatment ofsulfate/sulfite-laden wastewater from the pulp and paper,petroleum, mining, and chemical industries.