Chemical and Biological Treatment of Acid Mine Drainage for the Removal of Heavy Metals and Acidity

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dc.contributor.authorDiz, Harry Richarden
dc.contributor.committeechairNovak, John T.en
dc.contributor.committeememberCherry, Donald S.en
dc.contributor.committeememberKnocke, William R.en
dc.contributor.committeememberLove, Nancy G.en
dc.contributor.committeememberRimstidt, J. Donalden
dc.contributor.departmentCivil Engineeringen
dc.date.accessioned2014-03-14T20:22:34Zen
dc.date.adate1997-09-16en
dc.date.available2014-03-14T20:22:34Zen
dc.date.issued1997-08-11en
dc.date.rdate1998-09-16en
dc.date.sdate1997-08-11en
dc.description.abstractThis dissertation reports the design of a process (patent pending) to remove iron from acid mine drainage (AMD) without the formation of metal hydroxide sludge. The system includes the oxidation of ferrous iron in a packed bed bioreactor, the precipitation of iron within a fluidized bed, the removal of manganese and heavy metals (Cu, Ni, Zn) in a trickling filter at high (>9) pH, with final neutralization in a carbonate bed. The technique avoided the generation of iron oxyhydroxide sludge. In the packed bed bioreactor, maximum substrate oxidation rate (R<sub>,max</sub>) was 1500 mg L⁻¹ h⁻¹ at dilution rates of 2 h⁻¹, with oxidation efficiency at 98%. The half-saturation constant (similar to a Ks) was 6 mg L⁻¹. The oxidation rate was affected by dissolved oxygen below 2 mg L⁻¹, with a Monod-type Ko for DO of 0.33 mg L⁻¹. Temperature had a significant effect on oxidation rate, but pH (2.0 to 3.25) and supplemental CO₂ did not affect oxidation rates. Iron hydroxide precipitation was not instantaneous when base was added at a OH/Fe ratio of less than 3. Induction time was found to be a function of pH, sulfate concentration and iron concentration, with a multiple R² of 0.84. Aqueous [Al (III)] and [Mn (II)] did not significantly (α = 0.05) affect induction time over the range of concentrations investigated. When specific loading to the fluidized bed reactor exceeded 0.20 mg Fe m⁻² h⁻¹, dispersed iron particulates formed leading to a turbid effluent. Reactor pH determined the minimum iron concentration in the effluent, with an optimal at pH 3.5. Total iron removals of 98% were achieved in the fluidized bed with effluent [Fe] below 10 mg L⁻¹. Further iron removal occurred within the calcium carbonate bed. Heavy metals were removed both in the fluidized bed reactor as well as in the trickling filter. Oxidation at pH >9 caused manganese to precipitate (96% removal); removals of copper, nickel, and zinc were due primarily to sorption onto oxide surfaces. Removals averaged 97% for copper, 70% for nickel and 94% for zinc. The treatment strategy produced an effluent relatively free of iron (< 3 mg/L), without the formation of iron sludge and may be suitable for AMD seeps, drainage from acidic tailings ponds, active mine effluent, and acidic iron-rich industrial wastewater.en
dc.description.degreePh. D.en
dc.identifier.otheretd-81697-135443en
dc.identifier.sourceurlhttp://scholar.lib.vt.edu/theses/available/etd-81697-135443/en
dc.identifier.urihttp://hdl.handle.net/10919/30713en
dc.publisherVirginia Techen
dc.relation.haspartetd.pdfen
dc.rightsIn Copyrighten
dc.rights.urihttp://rightsstatements.org/vocab/InC/1.0/en
dc.subjectiron biooxidationen
dc.subjectiron precipitationen
dc.subjectiron removal technologyen
dc.subjectacid mine drainageen
dc.titleChemical and Biological Treatment of Acid Mine Drainage for the Removal of Heavy Metals and Acidityen
dc.typeDissertationen
thesis.degree.disciplineCivil Engineeringen
thesis.degree.grantorVirginia Polytechnic Institute and State Universityen
thesis.degree.leveldoctoralen
thesis.degree.namePh. D.en

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