Author:Pillay, K; von Blottnitz, H B; Petersen, JDate:2003Slag arising in ferrochromium and stainless steel production is known to contain residual levels of trivalent chromium. As the chromium is normally bound in the slag matrix in various silicate or spinel phases, and hence not easily mobilised, ...Read morecbnd
Author:Ogbonna, N; Petersen, J; Laurie, H D GDate:2006A mathematical model for bioleaching at the agglomerate scale is developed. The agglomerate is defined as a unit volume of a heap which contains a solid phase (a size distribution of ore particles), a liquid phase (stagnant and flowing leaching ...Read more
Author:Sheridan, C M; Glasser, D; Hildebrandt, D; Petersen, J; Rohwer, JDate:2011Winery effluent is known to have a high chemical oxygen demand (COD) and a low pH. In this study, we extensively analysed effluent from two cellars and studied the temporal changes over the duration of a harvest and the duration of a year. ...Read more
Author:Sheridan, C M; Hildebrandt, D; Glasser, D; Petersen, J; Rohwer, J Date:2011Winery effluent is known to have a high chemical oxygen demand (COD) and a low pH. In this study, we
extensively analysed effluent from two cellars and studied the temporal changes over the duration of a harvest
and the duration of a year. ...Read more
Author:Ojumu, T V; Harrison, S T L; Hansford, G S; Petersen, JDate:2008Although the kinetics of biological oxidation of ferrous to ferric iron–the key step
in any bioleaching process–have been studied for a variety of organisms, the focus has
always been on conditions typical of tank-bioleaching. In heaps, ...Read more
Author:Petersen, J; Minaar, S H; du Plessis, C ADate:2010During large-scale column tests at BHP Billiton's Johannesburg Technology Centre (JTC) on a low-grade copper ore during 2005/6, the concentrations of both oxygen and CO2 were continuously monitored in feed and exit gas as well as at various ...Read more
Author:Petersen, JDate:2010A detailed experimental study is described which was conducted to determine the rate of oxygen gas–liquid mass transfer within the packed bed of heap bioleach reactors at different temperatures (22–68 °C), using the Na2SO3 method. The raw ...Read more
Author:Tshilombo, A F; Petersen, J; Dixon, D GDate:2002Electrochemical techniques were conducted to clarify the role of solution potential and temperature under a variety of experimental conditions similar to those found during the mesophilic and thermophilic biooxidation of chalcopyrite (CuFeS2). ...Read morecbnd
Author:Ghorbani, Yousef; Becker, Megan; Petersen, J; Franzidis, Jean-PaulDate:Oct 2013Although heap leaching is by now well established in the mining industry, the process remains limited by low recoveries with different rate-limiting factors that are not clearly understood. In this study, three large particle size classes ...Read morecb
Author:Ojumu, T V; Petersen, JDate:2011The kinetics of ferrous ion oxidation by Leptospirillum ferriphilum were studied in continuous culture with a focus on the effect of solution pH (pH 0.8–2.0), assuming that the effect of pH on cell metabolism can be independently studied of ...Read more
Author:Ojumu, T V; Hansford, G S; Petersen, JDate:2009A typical bioleach heap is characterized by wide variation of temperature across the heap bed, leading to oxidation of target minerals occurring at different rates. Previous studies on the effect of temperature on the microbial oxidation of ...Read more
Author:Soleimani, M; Hosseini, S; Roostaazad, R; Petersen, J; Mousavi, S M; Vasiri, Kazemi ADate:2009The use of a draft tube fluidized bed bioreactor (DTFBB) has been successfully demonstrated for the bioleaching of a chalcopyrite concentrate (Mousavi, et. al., 2005). In the present paper this technique was used for the bioleaching of zinc ...Read more
Author:Petersen, J; Petrie, J GDate:2000The environmental impact of solid waste materials is closely linked
to their potential to produce a hazardous leachate once deposited in
a landfill. This potential is conventionally assessed with simple
laboratory batch leach tests, which ...Read morecb
Author:Petersen, JDate:2010This paper gives a brief introduction to the modelling of bioleach processes, developed from a careful analysis of the fundamental process steps at the gas–liquid, biological and mineral interfaces, and how these interact in a given reactor ...Read more
Author:Petersen, J; Dixon, D GDate:2007A comprehensive modelling study of the HydroZinc™ heap bioleach process, using the HeapSim modelling tool, is described. The model was calibrated on the basis of a small number of column leach experiments and compared against pilot heap test ...Read more
Author:Ojumu, T V; Petersen, J; Searby, G E; Hansford, G SDate:2006In view of the fact that the microbial oxidation of ferrous iron to the ferric form is an essential sub-process in the bioleaching of sulphide minerals, the development of a comprehensive rate equation for this sub-process is critical. Such ...Read more
Author:Petersen, J; Dixon, D GDate:2002Thermophiles have been shown to be the only micro-organisms to leach chalcopyrite successfully. Heap leaching may be a feasible alternative to conventional bio-reactors, providing a high temperature environment can be maintained within the ...Read morecbnd