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Author (up) Jones, D.R.; Chapman, B.M. openurl 
  Title Wetlands to treat AMD – facts and fallacies. Wetlands zur Sanierung saurer Grubenwässer – Fakten und Irrtümer Type Conference Article
  Year 1995 Publication Second Australian Acid Mine Drainage Workshop, Charters Towers, AU, 28 31 March 1995 Abbreviated Journal  
  Volume Issue Pages 127-145  
  Keywords Bergbau Geochemie anaerober-Prozess Verrieselungsfeld Kläranlage biologischer-Abbau Schwermetall Schwefelsäure Abwasserbehandlung Durchlaufverfahren Kosten Bauart Modulbauweise Funktionsprinzip Funktionswahrscheinlichkeit Literaturübersicht Betriebserfahrung Versuchsergebnis Acid mine drainage Wetland Wasseraufbereiten  
  Abstract Nach einer Definition der Wetlands wird ihre zunehmende Bedeutung als kostengünstige, ästhetische und nahezu wartungslose Alternative zur chemischen Aufbereitung saurer und schwermetallbelasteter Grubenwässer erläutert. Es werden die physikalischen Voraussetzungen behandelt und unter Bezugnahme auf ein umfangreiches Schrifttum die chemischen und mikrobiologischen Prozesse, die in Wetlands ablaufen, tabellarisch aufgelistet und detailliert unter Angabe der möglichen Reaktionen erläutert. Anschließend werden der Aufbau und die Funktionsweise der einzelnen Komponenten eines Wetlandsystems vorgestellt und die unterschiedlichen Typen der möglichen Ausführungsvarianten erläutert, was durch bildliche Darstellungen illustriert wird. Es wird ein Überblick zur Anwendung von Wetlands in Australien vermittelt. Die bei diesen Anwendungsfällen erzielten Ergebnisse werden diskutiert. Es werden Hinweise zur Planung sowie zur Anordnung der Wetlands gegeben, die auch grobe Kostenabschätzungen enthalten.  
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  Notes Wetlands to treat AMD – facts and fallacies. Wetlands zur Sanierung saurer Grubenwässer – Fakten und Irrtümer; BERG, Copyright FIZ Technik e.V.; EN Englisch; 0-646-24771-9; U9609 0034 586; 11338, BERG , 07.09.96; Words: 463; 19 Seiten, 7 Bilder, 3 Tabellen, 35 Quellen 3UXX *Belastung von Wasser, Wasserreinhaltung, Abwasser* 3BW *Geowissenschaften, physik* 3PZ *Bioverfahrenstechnik, Biotechnologie* Approved no  
  Call Number CBU @ c.wolke @ 17608 Serial 335  
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Author (up) Jong, T. url  openurl
  Title Microbial sulfate reduction under sequentially acidic conditions in an upflow anaerobic packed bed bioreactor Type Journal Article
  Year 2006 Publication Water Research Abbreviated Journal  
  Volume 40 Issue 13 Pages 2561-2571  
  Keywords mine water treatment  
  Abstract The aim of this study was to operate an upflow anaerobic packed bed reactor (UAPB) containing sulfate reducing bacteria (SRB) under acidic conditions similar to those found in acid mine drainage (AMD). The UAPB was filled with sand and operated under continuous flow at progressively lower pH and was shown to be capable of supporting sulfate reduction at pH values of 6.0, 5.0, 4.5, 4.0 and 3.5 in a synthetic medium containing 53.5 mmol l(-1) lactate. Sulfate reduction rates of 553-1052 mmol m(-3) d(-1) were obtained when the influent solution pH was progressively lowered from pH 6.0 to 4.0, under an optimal flow rate of 2.61 ml min(-1). When the influent pH was further lowered to pH 3.5, sulfate reduction was substantially reduced with only about 1% sulfate removed at a rate of 3.35 mmol m(-3) d(-1) after 20 days of operation. However, viable SRB were recovered from the column, indicating that the SRB population was capable of surviving and metabolizing at low levels even at pH 3.5 conditions for at least 20 days. The changes in conductivity in the SRB column did not always occur with changes in pH and redox potential, suggesting that conductivity measurements may be more sensitive to SRB activity and could be used as an additional tool for monitoring SRB activity. The bioreactor containing SRB was able to reduce sulfate and generate alkalinity even when challenged with influent as low as pH 3.5, indicating that such treatment systems have potential for bioremediating highly acidic, sulfate contaminated waste waters. (c) 2006 Elsevier Ltd. All rights reserved.  
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  Notes Microbial sulfate reduction under sequentially acidic conditions in an upflow anaerobic packed bed bioreactor; Wos:000239469400012; Times Cited: 0; ISI Web of Science Approved no  
  Call Number CBU @ c.wolke @ 16929 Serial 108  
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Author (up) Juby, G.J.G. url  openurl
  Title Desalination of calcium sulphate scaling mine water: Design and operation of the SPARRO process Type Journal Article
  Year 1996 Publication Water Sa Abbreviated Journal  
  Volume 22 Issue 2 Pages 161-172  
  Keywords mine water treatment  
  Abstract The South African mining industry discharges relatively small quantities of mine service water to the environment, but these effluents contribute substantially to the salt load of the receiving waters. The poor quality of service water also has significant cost implications on the mining operations. Of the two main types of mine service water encountered in the gold mining industry, the so-called calcium sulphate scaling types is found in the majority of cases. Preliminary testwork on this type of water using membrane desalination processes revealed that only the seeded reverse osmosis type of process showed promise. To overcome certain process problems and high operating costs with this system, a novel membrane desalination technique incorporating seeded technology, called the SPARRO (slurry precipitation and recycle reverse osmosis) process, was developed. The novel features of the new process included; a lower linear slurry velocity in the membrane tubes, a lower seed slurry concentration, a dual pumping arrangement to a tapered membrane stack, a smaller reactor and a modified seed crystal and brine blow-down system. Evaluation of the SPARRO process and its novel features, over a five-year period, confirmed its technical viability for desalinating calcium sulphate-scaling mine water. The electrical power consumption of the process was approximately half that of previous designs, significantly improving its efficiency. Membrane performance was evaluated and was generally unsatisfactory with both fouling and hydrolysis dominating at times, although operating conditions for the membranes were not always ideal. The precise cause(s) for the membrane degradation was not established, but a mechanism for fouling (based upon the presence of turbidity in the mine water) and a hypothesis fora possible cause of hydrolysis (alluding to the presence of radionuclides in the mine water) were proposed. Product water from the SPARRO process has an estimated gross unit cost (including capital costs) of 383 c/m(3) (1994).  
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  Notes Desalination of calcium sulphate scaling mine water: Design and operation of the SPARRO process; Wos:A1996uh88100009; Times Cited: 5; ISI Web of Science Approved no  
  Call Number CBU @ c.wolke @ 17168 Serial 86  
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Author (up) Juby, G.J.G.; Schutte, C.F. url  openurl
  Title Membrane Life in a Seeded-slurry Reverse Osmosis System Type Journal Article
  Year 2000 Publication Water Sa Abbreviated Journal  
  Volume 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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  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 (up) Kalin, M.; Cairns, J.; McCready, R. url  openurl
  Title Ecological engineering methods for acid mine drainage treatment of coal wastes Type Journal Article
  Year 1991 Publication Resources, conservation and recycling Abbreviated Journal  
  Volume 5 Issue 2-3 Pages 265-275  
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  Abstract The treatment of acid mine drainage (AMD) through the utilization of alkali generating microbes has potential as an alternate approach to conventional lime treatment. Organic matter, a source of fixed carbon for the alkali generating microbial ecosystem, has been tested in 6 different types of AMD. The AMD characteristics range in acidities from 2 mg/l to 900 mg/l (CaCO3 equivalent), while sulphate concentrations range from 75 to 7300 mg/l. Alkali generating populations identified include iron reducers, sulphate reducers and ammonifiers. In coal AMD amended with organic matter, the microbial alkali generation is dominated by ammonifiers. Concentrations of Al, Fe and Zn in the AMD water decreased with concurrent increases in pH (3.2 to 6.5) in localized areas in the test cells.  
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  Notes Ecological engineering methods for acid mine drainage treatment of coal wastes; Science Direct Approved no  
  Call Number CBU @ c.wolke @ 17276 Serial 39  
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