Vor den Toren der Stadt Dresden wurde im Döhlener Becken ohne Unterbrechung seit dem 16. Jahrhundert bis zum Jahr 1989 Steinkohle im Tiefbau gewonnen. In den Jahren von 1945 bis 1989 wurde mit Unterbrechungen auch uranhaltige Steinkohle abgebaut. Die Region wird von der Weißeritz durchflossen. Westlich der Weißeritz befindet sich das Grubenfeld Zauckerode. Auf der östlichen Seite spricht man vom Burgker Revier. Bereits in den 1980er Jahren wurde an Konzepten zur Verwahrung der Bergwerke gearbeitet. Ein zentrales Element der Verwahrung der bergbaulichen Hinterlassenschaften im Bereich westlich und östlich der Weißeritz war die dauerhafte Ableitung der Grubenwässer über den 6 km langen Tiefen Elbstolln in die Elbe. Zwischen 1991 und 2014 unternahm die Wismut GmbH erhebliche Anstrengungen zur umweltverträglichen Verwahrung der Bergbaubetriebe. So wurde der Versuch unternommen, den Grubenwasseranstieg im östlichen Revier auf einem Niveau oberhalb des Tiefen Elbstollns nahe der Tagesoberfläche zu stabilisieren. Die dabei gewonnenen Erfahrungen führten zum Rückgriff auf „Plan B“. Damit ist die Auffahrung des sogenannten Wismut-Stolln gemeint, der den hydraulischen Anschluss der Grubenbetriebe östlich der Weißeritz an das untertägige System westlich der Weißeritz und damit an den Tiefen Elbstolln realisiert. Im Zeitraum der Verwahrung hat die Wismut GmbH im Döhlener Becken insbesondere bei der Anhebung des Grubenwasser-Niveaus eine Vielzahl wertvoller Erfahrungen gesammelt, die von wesentlicher Bedeutung sind. Dies gilt auch für die Abschlussarbeiten an Schächten und Bergehalden. Mit der Fertigstellung der Auffahrung des Wismut-Stollns ist das Revier erfolgreich und umweltverträglich verwahrt. Das Forschungszentrum Nachbergbau an der Technischen Hochschule Georg Agricola zu Bochum ist von der Wismut GmbH beauftragt worden, den Grubenwasseranstiegsprozess zu evaluieren. Ziel ist es, den Lernprozess im Zuge des Grubenwasseranstiegs im Döhlener Becken in seinen wissenschaftlichen Aspekten zu bewerten und die Erkenntnisse für zukünftige Projekte verfügbar zu machen. Die Ergebnisse dieser Arbeiten sind zentraler Bestandteil des Vortrages. / In the southwest of Dresden within the area of the „Doehlen basin“ hard coal was continuously mined from the 16th century until 1989. The long-term drainage of mine water along the 6 km long deep drainage adit „Tiefer Elbstolln“ into the receiving river Elbe is the central issue of the mine closure process. During this process the Wismut GmbH gained a multitude of valuable experience, especially concerning the rising mine water table.

Magister Scientiae - MSc / This study evaluated SO4 2- removal from circumneutral mine water (CMW) collected from Middleburg coal mine using coal FA collected from Hendrina power station. The following parameters were investigated: the effect of the amount of FA, the effect of the final pH achieved during treatment, the effect of the initial pH of the mine water and the effect of Fe and Al on SO4 2- removal from mine water. The precipitation of ettringite at alkaline pH was evaluated to further reduce the SO4 2- concentration to below the DWAF limit for potable water. Removal of SO4 2- from mine water was found to be dependent on: the final pH achieved during treatment, the amount of FA used to treat the mine water and the presence of Fe and Al in the mine water. Treatment of CMW using different CMW:FA ratios; 5:1, 4:1, 3:1, and 2:1 resulted in 55, 60, 70 and 71 % SO4 2- removal respectively. Treatment of CMW to pH 8.98, 9.88, 10.21, 10.96, 11.77 and 12.35 resulted in 6, 19, 37, 45, 63 and 71 % SO4 2- removal respectively. When the CMW was modified by adding Fe and Al by mixing with Navigation coal mine AMD and treated to pH 10, 93 % SO4 2- removal was observed. Further studies were done to evaluate the effects of Fe and Al separately. Treatment of simulated Fe containing AMD (Fe-AMD) to pH 9.54, 10.2, 11.8, and 12.1 resulted in 47, 52, 65, and 68 % SO4 2- removal respectively. When Al containing AMD was treated to pH 9.46, 10.3, 11.5 and 12 percentage SO4 2- removal of 39, 51, 55 and 67 % was observed respectively. / South Africa

Philosophiae Doctor - PhD / In South Africa, almost 90 % of the country’s electricity is generated from coal combustion. This reliance on coal for energy production is projected to continue in the near and medium term due to the increasing demand for industrial and domestic energy. During coal combustion, a large quantity of fly ash is produced as the main waste product and in South Africa approximately 36 - 37 million tons of fly ash is produced on a yearly basis. The management of huge quantities of fly ash has been and still is a continuing challenge that requires urgent intervention. In this regard, there exists an urgent need to maximize fly ash beneficiation, thus forming the motivation for this research. The overall objectives of this thesis was to synthesize high pure phase zeolites A and X from South African fly ash, study their formation mechanism, and explore the potential of mine waters during the synthesis process as well as developing new and efficient zeolite synthetic protocols by the use of ultrasound. In order to address these objectives, the research was designed in a sequential manner so that the preceding results could act as a platform for the attainment of the next objective. In this case, the identification and optimization of synthesis conditions for producing zeolite A and X acted as a basis for understanding the influence of use of mine waters as a substitute for pure water. This further laid the foundation for the in-situ ultrasonic monitoring of the formation process of zeolite A and X from fly ash. The final stages of the study involved use of ultrasonic energy as an ageing tool to improve the conditions obtained during the hydrothermal synthesis of zeolite A as well as investigate the potential to synthesize zeolites directly by use of ultrasound without the need for the fusion, aging or conventional hydrothermal treatment step. The result of the optimized synthesis conditions for producing zeolite A starting either from clear extract of fused fly ash or unseparated, fused South African class F fly ash slurry were molar regimes of 1 Al2O3 : 30.84 Na2O : 4 SiO2 : 414.42 H2O or 1 Al2O3 : 5.39 Na2O : 2.75 SiO2 : 111.82 H2O respectively and at a hydrothermal synthesis temperature of 100 °C for 2 hours. The optimized procedure was simple, efficient and resulted in a considerable improvement of the quality and phase purity of the zeolite A product when the clear extract of fused fly ash was used instead of starting from unseparated, fused fly ash slurry. On the other hand, the optimized synthesis conditions for preparing the typical octahedral shaped zeolite X from South African fly ash was found to be a molar regime of 1 Al2O3 : 4.90 Na2O : 3.63 SiO2 : 115.92 H2O at a hydrothermal synthesis temperature of 80 ºC for hours.

Mine wastewaters generated during active production operations, and decanting streams following mine closure have major environmental impacts, and volumes requiring treatment are expected to increase substantially as the South African mining industry matures. Biological treatment of mine waters has been the subject of increasing interest, where sulphate reducing bacteria are employed for the reduction of sulphate to sulphide, precipitation of metals and the production of alkalinity. However, the sulphide if not removed from the system can be oxidised back to sulphate. As a result there have been limitations especially in the provision of technological options that are sustainable over the long-term, where the total sulphur (in its different forms) can be removed from the system. These, however, are the subject of a number of constraints including, importantly, the process capability to remove reduced sulphur from the treated stream, in one of its oxidation states, and thus linearise the biological sulphur cycle. This remains a major bottleneck in the development of biological wastewater treatment technology. Floating sulphur biofilms are observed as surface layers in numerous aquatic sulphide-rich environments, and it has been suggested that they play a role in the biological cycling of sulphur. The use of sulphur biofilms for the removal of elemental sulphur was identified in this study as a possible means for addressing the technological bottleneck, especially in passive wastewater treatment systems. There is, however, little documented information in the literature on the structure of floating sulphur biofilms, the microbial species responsible for their occurrence or bio-process applications of the system. A linear flow channel reactor was developed to simulate natural conditions and enabled the study of floating sulphur biofilm under controlled laboratory conditions. It was observed that these biofilms developed through three distinct stages termed Thin, Sticky and Brittle films. A microprobe study showed the presence of a steep Redox gradient established across (260 to 380 μm) depth of the floating sulphur biofilm of ~ 0 to -200 mV (top to bottom), which correlated with pH and sulphide gradients across the system. Structural investigations embedded in an exopolymeric matrix containing clearly defined channels and pores. Sulphur crystals were found to develop within the biofilm and above a certain size these disengaged and then settled in the liquid phase below the biofilm. These features, together with the ability of the biofilm to remain suspended at the air/water interface thus provide the surface requirement, and indicate that these structures may be understood as “true” biofilms. In order to study an apparent functional differentiation within the floating sulphur biofilm system, a method was developed to expand its various components over a 13 cm length of agarose tube and across which an oxygen/sulphide gradient was established. This was done by inserting a sulphide plug in the bottom of the tube, overlaying this with the biofilm mixed and suspended in agarose and leaving the tube to open air. After allowing for growth, the different components of the microbial population occurring at various levels across the oxygen/sulphide gradient were sampled. The microbial population was found to resort in distinct functional layers. Aerobes including Acidithiobacillus and Azoarcus, Acidithiobacillus, Thiothrix, Thiovirga and Sulfurimonas were found in the upper oxidised layer. Aerobe and facultative anaerobes such as Chryseobacterium, Bacteroides and Planococcus were found in the middle and heterotrophic anaerobes such as Brevundimonas and uncultured anaerobes were found in the bottom anoxic layer. This enabled the development of a first descriptive structural/functional model accounting for the performance of floating sulphur biofilms. The potential of the floating sulphur biofilm for use as a bioprocess unit operation for sulphide removal in lignocellulose-based low-flow passive systems for acid mine drainage wastewater treatment was investigated. The linear flow channel reactor was scaled up and it was shown that the optimum sulphide removal of 74 % and sulphur recovery of 60 % could be achieved at 20 °C. In a further scale up of the linear channel reactor, the floating sulphur biofilm reactor was developed and operated. Sulphide removal and sulphur recovery of 65 and 56 % respectively was measured in the process. An understanding of the nature and function of floating sulphur biofilms and the further development of their potential application in sulphide removal in aquatic systems may provide a useful contribution to the treatment of acid mine drainage and other sulphidic wastewaters.

The target of the diploma thesis is balance of energy usage within the property of company Uniman Englis. There is at the beginning description of heat pump for different principles of use. Then there is described geothermal energy and the possibility of gaining energy from mine water found on the company property. This thesis describes the various design options for the use of mine water and revitalization of industrial buildings. These proposals are then designed and assessed in terms of thermal energy by using the heat pump. Afterward there is provided the energy audit for chosen solutions.

>Magister Scientiae - MSc / South African power stations generate large amounts of highly alkaline fly ash (FA). This waste product has a serious impact on the environment. Acid mine drainage (AMD) is another environmental problem associated with mining. AMD has high heavy metal content in addition to high SO/- concentrations. Several studies have shown that 80-90 % of SO/- can be removed when FA is codisposed with AMD rich in Fe and AI. In South Africa, many sources of contaminated mine waters have circumneutral pH and much lower concentrations of Fe and Al (unlike AMD), but are rich in Ca, Mg and SO2-4. This study evaluated sol removal from circumneutral mme water (CMW) collected from Middleburg coal mine using coal FA collected from Hendrina power station. The following parameters were investigated: the effect of the amount of FA, the effect of the final pH achieved during treatment, the effect of the initial pH of the mine water and the effect of Fe and Al on SO/- removal from mine water. The precipitation of ettringite at alkaline pH was evaluated to further reduce the SO/- concentration to below the DWAF limit for potable water. Removal of sol from mine water was found to be dependent on: the final pH achieved during treatment, the amount of FA used to treat the mine water and the presence of Fe and Al in the mine water. Treatment of CMW using different CMW:FA ratios; 5:1, 4:1, 3:1, and 2:1 resulted in 55, 60, 70 and 71 % SO/- removal respectively. Treatment of CMW to pH 8.98, 9.88, 10.21, 10.96, 11.77 and 12.35 resulted in 6, 19, 37, 45, 63 and 71 % SO/- removal respectively. When the CMW was modified by adding Fe and Al by mixing with Navigation coal mine AMD and treated to pH 10, 93 % SO/- removal was observed. Further studies were done to evaluate the effects of Fe and Al separately. Treatment of simulated Fe containing AMD (Fe-AMD) to pH 9.54, 10.2, 11.8, and 12.1 resulted in 47, 52,65, and 68 % SO/- removal respectively. When Al containing AMD was treated to pH 9.46, 10.3, 11.5 and 12 percentage SO/- removal of 39, 51,55 and 67 % was observed respectively. Ion chromatography (IC), inductively coupled plasma-mass spectrometry (ICPMS) and inductively coupled plasma-atomic emission (ICP-AES) analysis of the product water, x-ray diffraction (XRD) and x-ray fluorescence (XRF) spectrometry analysis of FA and solid residues collected after treatment of mine water complemented with PHREEQC thermodynamic modelling have shown that the mechanism of S042 - removal from mine water depends on the composition of the mine water. The sol- removal mechanism from CMW was observed to depend on gypsum precipitation. On the other hand sol- removal from mine water containing Fe and Al was dependent on the precipitation of gypsum and Fe and Al oxyhydroxysulphates. The oxyhydroxysulphates predicted by PHREEQC as likely to precipitate were alunite, basaluminite, ettringite, jarosites and jurbanite. Treatment of CMW with FA to pH 12.35 removed sol- from 4655 ppm to approximately 1500 ppm. Addition of amorphous AI(OH)3 to CMW that was treated to pH greater than 12 with FA was found to further reduce the sol concentration to 500 ppm which was slightly above the threshold for potable water of 400 ppm. The further decrease of sol concentration from 1500 to 500 ppm was due to ettringite precipitation. Mine water treatment using FA was found to successfully remove all the major elements such as Fe, AI, Mn and Mg to below the DWAF limit for drinking water. The removal of the major elements was found to be pH dependent. Fe and Al were removed at pH 4-7, while Mn and Mg were removed at pH 9 and 11 respectively. The process water from FA treatment followed by gypsum seeding and addition of AI(OH)3 had high concentration of Ca, Cr, Mo and B and a pH of greater than 12. The pH of the process water from FA treatment followed by gypsum seeding and addition of AI(OH)3 was reduced by reacting the process water with CO2 to 7.06. The process water from the carbonation process contained trace elements such as Cr, Mo and B above the DWAF effluent limit for domestic use. Carbonation of the process water reduced the water hardness from 5553 ppm to 317 ppm due to CaC03 precipitation, thereby reducing the Ca concentration from 2224 ppm to 126 ppm.

>Magister Scientiae - MSc / Mining has a lengthy history in South Africa, and subsequent beneficiation processes have been conducted with little regard for the environment, thus leaving the land with un-rehabilitated abandoned mines. Currently, most of these abandoned mine sites are no longer operational and they continuously contaminate soil, air and water resources in various areas where mining took place. This study looks at the treatment of contaminated mine water using the Dispersed Alkaline Substrates (DAS) which is a new South African technology that uses a variety of substrates to neutralize and raise the pH of mine water while lowering the solubility of potentially dangerous metals.

No description available.

Thesis (M. Sc. (Geography)) -- University of Limpopo, 2021 / Acid Mine Drainage (AMD) is the acidic water emanating from the mine tailing dams into the surrounding environment. AMD is regarded as a major environmental threat associated with mining. The lower Olifants River in the Kruger National Park (KNP) is considered an environmentally sensitive area, which exhibits high levels of aquatic ecosystems and supports a variety of terrestrial ecosystems within and around the KNP. The Phalaborwa mining industries have been discharging the acid mine drainage contaminated-water into the Ga-Selati River, a tributary to the Olifants River. Although the impacts in the upper Olifants River catchment have been well documented, it was the amount of AMD witnessed at KNP and the dying of fish within the lower Olifants River that raised issues of concerns. Hence, the study investigated the impact of acid mine drainage on water quality of the lower Olifants River, modelled the distribution of the dissolved heavy metals in the stream, and evaluated the applied mine wastewater management strategies at Phalaborwa mining industries. In this study, water samples were collected seasonally (winter, spring, and summer) from 2019 to 2020, and the analytical methods and procedures were optimized for the determination of selected elements in the water samples. During the study, ion chromatography (IC) was used to detect chloride (Cl), sulphate (SO4 - ), nitrate (NO3), and fluoride (F), Inductively Coupled Plasma Optical Emission Spectroscopy (ICP-OES) was used to detect pH, turbidity, electrical conductivity (EC), total dissolved solids (TDS), magnesium (Mg), manganese (Mn), sodium (Na), potassium (K), aluminium (Al) and calcium (Ca). Modelling of the distribution of dissolved heavy metals was performed using the inverse distance weighted (IDW) interpolation technique available in ArcGIS 10.8 software. The range of pH across four sampling sites was between 7.77 and 9.11, indicating an alkaline pH. The concentration of measured parameters elevated downstream points with some exceeding the target water quality range (TWQR) for aquatic ecosystems. The elevated concentration of SO4 - at sites 3 and 4 (downstream points) showed that the acid mine drainage is still a matter of concern at the lower Olifants River catchment. However, the GIS models showed a decreasing trend of the concentration of heavy metal towards the KNP.

M. Tech. Metallurgical Engineering. / Studies the tribological and electrochemical behaviour of various WC-Co, WC-Co-Cr and CrC-NiCr based thermal sprayed coatings in synthetic mine water environment. The research aims to achieve the following objectives. 1. Characterize commercially available cermet powders used during thermal spray process. 2. Explore and understand the relationship between feedstock powder parameters, the phases and microstructures generated during thermal spray process. Study the interrelationship of feedstock powder chemistry and method of powder synthesis on wear and corrosion behavior of thermally sprayed coatings. Assess the joint actions of wear and corrosion behaviour of the coatings in synthetic mine water environment.