A continuous process for the biological treatment of heavy metal contaminated acid mine water

dc.contributor.authorvan Hille, R P
dc.contributor.authorBoshoff, G A
dc.contributor.authorRose, P D
dc.contributor.authorDuncan J R
dc.date.accessioned2016-08-17T07:34:05Z
dc.date.available2016-08-17T07:34:05Z
dc.date.issued1999
dc.date.updated2016-08-16T11:46:55Z
dc.description.abstractAlkaline precipitation of heavy metals from acidic water streams is a popular and long standing treatment process. While this process is efficient it requires the continuous addition of an alkaline material, such as lime. In the long term or when treating large volumes of effluent this process becomes expensive, with costs in the mining sector routinely exceeding millions of rands annually. The process described below utilises alkalinity generated by the alga Spirulina sp., in a continuous system to precipitate heavy metals. The design of the system separates the algal component from the metal containing stream to overcome metal toxicity. The primary treatment process consistently removed over 99% of the iron (98.9 mg/l) and between 80 and 95% of the zinc (7.16 mg/l) and lead (2.35 mg/l) over a 14-day period (20 l effluent treated). In addition the pH of the raw effluent was increased from 1.8 to over 7 in the post-treatment stream. Secondary treatment and polishing steps depend on the nature of the effluent treated. In the case of the high sulphate effluent the treated stream was passed into an anaerobic digester at a rate of 4 l/day. The combination of the primary and secondary treatments effected a removal of over 95% of all metals tested for as well as a 90% reduction in the sulphate load. The running cost of such a process would be low as the salinity and nutrient requirements for the algal culture could be provided by using tannery effluent or a combination of saline water and sewage. This would have the additional benefit of treating either a tannery or sewage effluent as part of an integrated process.en_ZA
dc.identifierhttp://dx.doi.org/10.1016/S0921-3449(99)00010-5
dc.identifier.apacitationvan Hille, R. P., Boshoff, G. A., Rose, P. D., & (1999). A continuous process for the biological treatment of heavy metal contaminated acid mine water. <i> Resources, Conservation and Recycling</i>, http://hdl.handle.net/11427/21276en_ZA
dc.identifier.chicagocitationvan Hille, R P, G A Boshoff, P D Rose, and "A continuous process for the biological treatment of heavy metal contaminated acid mine water." <i> Resources, Conservation and Recycling</i> (1999) http://hdl.handle.net/11427/21276en_ZA
dc.identifier.citationVan Hille, R. P., Boshoff, G. A., Rose, P. D., & Duncan, J. R. (1999). A continuous process for the biological treatment of heavy metal contaminated acid mine water. Resources, Conservation and Recycling, 27(1), 157-167.en_ZA
dc.identifier.issn0921-3449en_ZA
dc.identifier.ris TY - Journal Article AU - van Hille, R P AU - Boshoff, G A AU - Rose, P D AU - Duncan J R AB - Alkaline precipitation of heavy metals from acidic water streams is a popular and long standing treatment process. While this process is efficient it requires the continuous addition of an alkaline material, such as lime. In the long term or when treating large volumes of effluent this process becomes expensive, with costs in the mining sector routinely exceeding millions of rands annually. The process described below utilises alkalinity generated by the alga Spirulina sp., in a continuous system to precipitate heavy metals. The design of the system separates the algal component from the metal containing stream to overcome metal toxicity. The primary treatment process consistently removed over 99% of the iron (98.9 mg/l) and between 80 and 95% of the zinc (7.16 mg/l) and lead (2.35 mg/l) over a 14-day period (20 l effluent treated). In addition the pH of the raw effluent was increased from 1.8 to over 7 in the post-treatment stream. Secondary treatment and polishing steps depend on the nature of the effluent treated. In the case of the high sulphate effluent the treated stream was passed into an anaerobic digester at a rate of 4 l/day. The combination of the primary and secondary treatments effected a removal of over 95% of all metals tested for as well as a 90% reduction in the sulphate load. The running cost of such a process would be low as the salinity and nutrient requirements for the algal culture could be provided by using tannery effluent or a combination of saline water and sewage. This would have the additional benefit of treating either a tannery or sewage effluent as part of an integrated process. DA - 1999 DB - OpenUCT DP - University of Cape Town J1 -  Resources, Conservation and Recycling LK - https://open.uct.ac.za PB - University of Cape Town PY - 1999 SM - 0921-3449 T1 - A continuous process for the biological treatment of heavy metal contaminated acid mine water TI - A continuous process for the biological treatment of heavy metal contaminated acid mine water UR - http://hdl.handle.net/11427/21276 ER - en_ZA
dc.identifier.urihttp://hdl.handle.net/11427/21276
dc.identifier.vancouvercitationvan Hille RP, Boshoff GA, Rose PD, . A continuous process for the biological treatment of heavy metal contaminated acid mine water.  Resources, Conservation and Recycling. 1999; http://hdl.handle.net/11427/21276.en_ZA
dc.languageengen_ZA
dc.publisherElsevieren_ZA
dc.publisher.institutionUniversity of Cape Town
dc.rightsCreative Commons Attribution-NonCommercial-NoDerivatives 4.0 International (CC BY-NC-ND 4.0)*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/en_ZA
dc.source Resources, Conservation and Recyclingen_ZA
dc.source.urihttp://www.journals.elsevier.com/resources-conservation-and-recycling/
dc.subject.otherBiological treatment
dc.subject.otherHeavy metal
dc.subject.otherAcid mine water
dc.subject.otherAlkaline precipitation
dc.titleA continuous process for the biological treatment of heavy metal contaminated acid mine wateren_ZA
dc.typeJournal Articleen_ZA
uct.type.filetypeText
uct.type.filetypeImage
uct.type.publicationResearchen_ZA
uct.type.resourceArticleen_ZA
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