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Author Van Hille, R.P.; Boshoff, G.A.; Rose, P.D.; Duncan, J.R.
Title A continuous process for the biological treatment of heavy metal contaminated acid mine water Type Journal Article
Year 1999 Publication Resour. Conserv. Recycl. Abbreviated Journal
Volume (down) 27 Issue 1-2 Pages 157-167
Keywords mine water treatment biological treatment heavy metal acid mine water alkaline precipitation green-algae chlorella
Abstract 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.
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ISSN 0921-3449 ISBN Medium
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Notes Jul; A continuous process for the biological treatment of heavy metal contaminated acid mine water; Isi:000081142100017; file:///C:/Dokumente%20und%20Einstellungen/Stefan/Eigene%20Dateien/Artikel/9937.pdf; AMD ISI | Wolkersdorfer Approved no
Call Number CBU @ c.wolke @ 9937 Serial 26
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Author Li, L.; Jiang, Y.; Guo, Y.
Title Research on a comprehensive industrialization technology for the treatment of mining water containing sulfate ions Type Journal Article
Year 1999 Publication Meitian Dizhi Yu Kantan = Coal Geology & Exploration Abbreviated Journal
Volume (down) 27 Issue 6 Pages 51-53
Keywords acid mine drainage; coal mines; mines; pollution; purification; sulfate ion; technology; water pollution; water treatment 22, Environmental geology
Abstract A method using a barium reagent was developed for the purification of the higher-sulphate mine water.
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ISSN 1001-1986 ISBN Medium
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Notes Research on a comprehensive industrialization technology for the treatment of mining water containing sulfate ions; 2005-057894; References: 5 China (CHN); GeoRef; Chinese Approved no
Call Number CBU @ c.wolke @ 6097 Serial 316
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Author Juby, G.J.G.; Schutte, C.F.
Title Membrane Life in a Seeded-slurry Reverse Osmosis System Type Journal Article
Year 2000 Publication Water Sa Abbreviated Journal
Volume (down) 26 Issue 2 Pages 239-248
Keywords mine water treatment desalination
Abstract Membrane replacement can be a major operating cost of a membrane plant. During the development of a novel desalination technique (the SPARRO process) for treating calcium sulphate scaling mine waters the expected life of tubular cellulose acetate membranes operating in the seeded-slurry mode was investigated.During four operating phases of the plant over a five-year period more than 9 000 h of operating data were obtained. Performance data showed that each operating phase was dominated by either membrane fouling or membrane hydrolysis. Membrane fouling was observed to begin near the front-end of the membrane stack and proceed towards the back. Hydrolysis, on the other hand, occurred first in the tail end of the stack and moved backwards towards the Front end modules. Although two detailed membrane autopsies were carried out no definitive statement can be made in respect of the causes of either membrane hydrolysis or membrane fouling. However, suggestions are presented to explain the observed fouling phenomenon in relation to the turbidity of the pretreated feed water and the presence of chlorine. It is proposed that the presence of radioactive isotopes in the mine water which become concentrated in the process contributes to the observed membrane hydrolysis. A membrane life of up to two years is projected for an improved pretreatment arrangement.
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ISSN 0378-4738 ISBN Medium
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Notes Membrane Life in a Seeded-slurry Reverse Osmosis System; Isi:000087101400013; file:///C:/Dokumente%20und%20Einstellungen/Stefan/Eigene%20Dateien/Artikel/9715.pdf; AMD ISI | Wolkersdorfer Approved no
Call Number CBU @ c.wolke @ 9715 Serial 8
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Author Zhuang, J.M.
Title Lignor(TM) process for acidic rock drainage treatment Type Journal Article
Year 2004 Publication Environ. Technol. Abbreviated Journal
Volume (down) 25 Issue 9 Pages 1031-1040
Keywords mine water treatment
Abstract The process using lignosulfonates for acidic rock drainage (ARD) treatment is referred to as the Lignor(TM) process. Lignosulfonates are waste by-products produced in the sulfite pulping process. The present study has shown lignosulfonates are able to protect lime from developing an external surface coating, and hence to favor its dissociation. Further, the addition of lignosulfonates to ARD solutions increased the clotting and settling rate of the formed sludge. The capability of lignosulfonates to form stable metal-lignin complexes makes them very useful in retaining metal ions and thus improving the long-term stability of the sludge against leaching. The Lignor(TM) process involves metal sorption with lignosulfonates, ARD neutralization by lime to about pH 7, pH adjustment with caustic soda to 9.4 – 9.6, air oxidation to lower the pH to a desired level, and addition of a minimum amount of FeCl3 for further removal of dissolved metals. The Lignor(TM) process removes all concerned metals (especially Al and Mn) from the ARD of the Britannia Mine (located at Britannia Beach, British Columbia, Canada) to a level lower than the limits of the B.C. Regulations. Compared with the high-density sludge (HDS) process, the Lignor(TM) process has many advantages, such as considerable savings in lime consumption, greatly reduced sludge volume, and improved sludge stability.
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Notes Lignor(TM) process for acidic rock drainage treatment; Wos:000224971800006; Times Cited: 0; ISI Web of Science Approved no
Call Number CBU @ c.wolke @ 16998 Serial 117
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Author Holtzhausen, L.
Title Minewater treatment technology revved up Type Journal Article
Year 2005 Publication Water Sewage and Effluent Abbreviated Journal
Volume (down) 25 Issue 2 Pages 24-26
Keywords Geobase: Related Topics geobase: related topics (901) water treatment
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ISSN 0257-8700 ISBN Medium
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Notes Trade- Note; Minewater treatment technology revved up; 2710582; South-Africa; Geobase Approved no
Call Number CBU @ c.wolke @ 10344 Serial 348
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