Mixed Culture Of Sulfate-reducing Bacteria Research Articles

An integrated microbial process for the bioremediation of soil contaminated with toxic metals.

Microbially catalyzed reactions, which occur in the natural sulfur cycle, have been integrated in a microbiological process to remove toxic metals from contaminated soils. Bioleaching using sulfuric acid produced by sulfur-oxidizing bacteria was followed by precipitation of the leachate metals as insoluble sulfides by sulfate-reducing bacteria. Metal contaminants including Cd, Co, Cr, Cu, Mn, Ni, and Zn were efficiently leached from an artificially contaminated soil. Mn, Ni, and Zn were the only target elements that were significantly leached from soil minerals. Pb leaching was slow and remained incomplete over a period of 180 days. Mineral components such as Fe, Ca and Mg were also leached but the eventual reduction in soil mass was only approximately 10%. An industrially contaminated soil was also efficiently leached and approximately 69% of the main toxic metals present, Cu, Ni, and Mn, were removed after 175 days. The leachate that resulted from the action of sulfur-oxidizing bacteria on contaminated soil was stripped of metals using an anaerobic bioreactor containing a mixed culture of sulfate-reducing bacteria which precipitated soluble metal species as solid metal sulfides. More than 98% of the metals were removed from solution with the exception of Mn, Ni, and Pb, where 80-90% were removed. The metal content of the resultant effluent liquor was low enough to meet European criteria for discharge into the environment.

Accumulation and effects of cadmium on sulphate-reducing bacterial biofilms.

Biofilms comprising a pure and a mixed culture of sulphate-reducing bacteria (SRB) were grown in continuous culture. When exposed to 20 or 200 μM Cd, both cultures accumulated Cd but the mixed culture accumulated more and continued to accumulate Cd during the experiment, whereas accumulation by the pure cultures ceased after 4-6 d. Unlike the pure culture, the mixed culture also accumulated both protein and carbohydrate throughout the experiment proportionally to Cd which showed that accumulation required the production of biofilm material. Electron microscopy showed the presence of polysaccharide and particulates in both pure and mixed cultures, irrespective of the presence of Cd. However, energy-dispersive X-ray analysis (EDXA) showed that accumulation of Cd in the form of CdS occurred in biofilms exposed to Cd while back-scattered electron imaging of sections indicated that the accumulation of Cd was localized in a superficial layer of the biofilm. The mechanism of uptake, therefore, appeared to be entrapment and/or precipitation of CdS at the biofilm surface. The relatively low Cd uptake by the pure culture biofilm was attributed to its less efficient growth and polysaccharide production. These results indicate that mixed SRB cultures are more effective than pure cultures for metal removal and underlines significant differences between the biology of pure and mixed cultures.

Biodesulfurization of flue gases and other sulfate/sulfite waste streams using immobilized mixed sulfate-reducing bacteria.

Sulfur dioxide (SO2) is one of the major pollutants in the atmosphere that cause acid rain. Microbial processes for reducing SO2 to hydrogen sulfide (H2S) have previously been demonstrated by utilizing mixed cultures of sulfate-reducing bacteria (SRB) with municipal sewage digest as the carbon and energy source. To maximize the productivity of the bioreactor for SO2 reduction in this study, various immobilized cell bioreactors were investigated: a stirred tank with SRB flocs and columnar reactors with cells immobilized in either potassium-carrageenan gel matrix or polymeric porous BIO-SEP beads. The maximum volumetric productivity for SO2 reduction in the continuous stirred-tank reactor (CSTR) with SRB flocs was 2.1 mmol of SO2/(h.L). The potassium-carrageenan gell matrix used for cell immobilization was not durable at feed sulfite concentrations greater than 2000 mg/L (1.7 mmol/(h.L)). A columnar reactor with mixed SRB cells that had been allowed to grow into highly stable BIO-SEP polymeric beads exhibited the highest sulfite conversion rates, in the range 16.5 mmol/(h.L) (with 100% conversion) to 20 mmol/(h.L) (with 95% conversion). The average specific activity for sulfite reduction in the column, in terms of dry weight of SRB biomass, was 9.5 mmol of sulfite/(h.g). In addition to flue gas desulfurization, potential applications of this microbial process include the treatment of sulfate/sulfite-laden wastewater from the pulp and paper, petroleum, mining, and chemical industries.

A biological process for the reclamation of flue gas desulfurization gypsum using mixed sulfate-reducing bacteria with inexpensive carbon sources

A combined chemical and biological process for the recycling of flue gas desulfurization (FGD) gypsum into calcium carbonate and elemental sulfur is demonstrated. In this process, a mixed culture of sulfate-reducing bacteria (SRB) utilizes inexpensive carbon sources, such as sewage digest or synthesis gas, to reduce FGD gypsum to hydrogen sulfide. The sulfide is then oxidized to elemental sulfur via reaction with ferric sulfate, and accumulating calcium ions are precipitated as calcium carbonate using carbon dioxide. Employing anaerobically digested municipal sewage sludge (AD-MSS) medium as a carbon source, SRBs in serum bottles demonstrated an FGD gypsum reduction rate of 8 mg/L/h (10(9) cells)(-1). A chemostat with continuous addition of both AD-MSS media and gypsum exhibited sulfate reduction rates as high as 1.3 kg FGD gypsum/m(3)d. The increased biocatalyst density afforded by cell immobilization in a columnar reactor allowed a productivity of 152 mg SO(4) (-2)/Lh or 6.6 kg FGD gypsum/m(3)d. Both reactors demonstrated 100% conversion of sulfate, with 75-100% recovery of elemental sulfur and chemical oxygen demand utilization as high as 70%. Calcium carbonate was recovered from the reactor effluent on precipitation using carbon dioxide. It was demonstrated that SRBs may also use synthesis gas (CO, H(2), and CO(2) in the reduction of gypsum, further decreasing process costs. The formation of two marketable products-elemental sulfur and calcium carbonate-from FGD gypsum sludge, combined with the use of a low-cost carbon source and further improvements in reactor design, promises to offer an attractive alternative to the landfilling of FGD gypsum.

Recycling of FGD Gypsum to Calcium Carbonate and Elemental Sulfur Using Mixed Sulfate-Reducing Bacteria with Sewage Digest as a Carbon Source

A combined chemical and biological process for the recycling of flue gas desulfurization (FGD) gypsum into calcium carbonate and elemental sulfur is demonstrated. In this process, a mixed culture of sulfate-reducing bacteria (SRB) utilizes sewage digest as its carbon source to reduce FGD gypsum to hydrogen sulfide. The sulfide is then oxidized to elemental sulfur via reaction with ferric sulfate, and accumulating calcium ions are precipitated to calcium carbonate using carbon dioxide. Employing anaerobically digested-municipal sewage sludge (AD-MSS) medium as a carbon source, SRB in serum bottles demonstrated an FGD gypsum reduction rate of 8 mg dm−3 h−1 (109 cells)−1. A chemostat with continuous addition of both AD-MSS medium and gypsum exhibited sulfate reduction rates as high as 1·3kg FGD gypsumm−3 day−1. The increased biocatalyst density afforded by cell immobilization in a columnar reactor allowed a productivity of 152 mg SO4 dm−3 h−1 or 6·6kg FGD gypsum m−3 day−1. Both reactors demonstrated 100% conversion of sulfate, with 75–100% recovery of elemental sulfur and as high as 70% COD utilization. Calcium carbonate was recovered from the reactor effluent upon precipitation using carbon dioxide. The formation of two marketable products—elemental sulfur and calcium carbonate—from FGD gypsum sludge, combined with the use of a low-cost carbon source and further improvements in reactor design, promises to offer an attractive alternative to the landfilling of FGD gypsum.

Effect on methane digestion of decreased H2 partial pressure by means of phototrophic or sulfate-reducing bacteria grown in an auxiliary reactor

H2 is a central metabolite in the process of methane digestion. In this study, the partial pressure of H2 was decreased by sparging the gas phase of the digester through an auxiliary reactor in which a Rhodomicrobium vaniellii culture or a mixed culture of sulfate-reducing bacteria was allowed to develop at the expense of H2 and CO2 present in the biogas. The decrease of the H2 concentration in the gas phase was significant. A 18–23 percent increase of the gas production rate and a concomitantly improved removal of volatile fatty acids from the mixed liquor was obtained. The sulfate-reducing bacteria appeared to be slightly more effective than the phototrophs. The results suggest that the increased biogas production rate is due to the decrease of propionic acid formation and the concomitant stimulation of propionate degradation.

The relationship between fatty acid distributions and bacterial respiratory types in contemporary marine sediments

Bacterial communities of different respiratory types were isolated from a marine sediment in a multiple chemostat system in an attempt to obtain bacterial cultures representative of the sediment. The fatty acid distribution of a mixed culture of sulphate-reducing bacteria isolated from this system showed a good correlation with the lipid distribution of the zone of maximum sulphate-reduction activity within the sediment. Both distributions had significant concentrations of C14 : 0, iso and anteiso C15 : 0, C16 : 0, C16 : 1ω7 and C18 : 1ω7. This was in contrast to the lipid profile of Desulfovibrio desulfuricans obtained by batch enrichment, which was dominated by iso C17 : 1ω7 fatty acids and correlated poorly with the sediment. The bacterial community cultured from the sediment was further differentiated according to respiratory types (aerobic, facultative aerobic and facultative anaerobic) by growth in a chemostat under defined conditions. The fatty acid distributions of these communities were sufficiently different to enable the various respiratory types to be recognized by their particular fatty acid composition. Cyclopropyl fatty acids (▿17 and ▿19) were present in significant levels only in the aerobic bacteria, while the facultative aerobes had significantly higher C18 : 1ω7 than the other cultures and the facultative anaerobic community was the only culture to have significant amounts of C12 : 0. The fatty acid distribution of Loch Eil sediment over the range C12-19 seemed to be predominantly of bacterial origin and were relatively abundant to a depth of 6 cm. The concentration of cyclopropyl fatty acids was highest in the oxidized surface sediments and decreased with depth as anaerobic conditions began to dominate, indicating that these fatty acids may only be indicative of aerobic sedimentary bacteria. In contrast to the fatty acids characteristic of bacteria, those fatty acids in the range C20-30 attributed to a terrestrial input were found in relatively constant concentrations over the whole 0–12 cm depth profile.

Interaction of aerobic and anaerobic bacteria in petroleum biodegradation

The relationships between aerobic petroleum-degrading and anaerobic sulfate-reducing bacteria in oil degradation are presented. Neither pure nor mixed cultures of sulfate-reducing bacteria were able to grow on oils under anaerobic conditions. Such cultures, however, were able to grow on the residues from the aerobic bacterial degradation of some oils. Growth of sulfate-reducers was determined in part by the nature of the aerobic population used to degrade an oil, the chemical composition of the oil and whether the sulfate-reducing bacteria were in pure or mixed cultures. If mixed cultures were grown, then a nitrate-free medium had to be used because of the production of nitrate by mixed cultures. The results presented support the hypothesis that sulfate-reducing bacteria cannot initiate degradation of oil but rather grow on the residues resulting from the aerobic degradation of oil.