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Author |
Rajaram, V. |
Title |
Methodology for estimating the costs of treatment of mine drainage |
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Journal Article |
Year |
2001 |
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Proceedings of the Seventeenth International Mining Congress and Exhibition of Turkey |
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191-201 |
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mine water treatment |
Abstract |
Tetra Tech developed worksheets for the U.S. Department of the Interior, Office of Surface Mining (OSM) to allow a consistent, accurate, and rapid method of estimating the costs of long-term treatment of mine drainage at coal mines, in accordance with the Surface Mining Control and Reclamation Act (SMCRA) of 1977. This paper describes the rationale for the worksheets and how they can be used to calculate costs for site-specific conditions. Decision trees for selection of alternative treatments for acidic or alkaline mine drainage are presented. |
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Methodology for estimating the costs of treatment of mine drainage; Isip:000171428500021; Times Cited: 0; ISI Web of Science |
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CBU @ c.wolke @ 17065 |
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163 |
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Jong, T. |
Title |
Microbial sulfate reduction under sequentially acidic conditions in an upflow anaerobic packed bed bioreactor |
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Journal Article |
Year |
2006 |
Publication |
Water Research |
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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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Microbial sulfate reduction under sequentially acidic conditions in an upflow anaerobic packed bed bioreactor; Wos:000239469400012; Times Cited: 0; ISI Web of Science |
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CBU @ c.wolke @ 16929 |
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108 |
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Kauffman, J.W. |
Title |
Microbiological Treatment Of Uranium-Mine Waters |
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Journal Article |
Year |
1986 |
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Environ Sci Technol |
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20 |
Issue |
3 |
Pages |
243-248 |
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mine water treatment |
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Microbiological Treatment Of Uranium-Mine Waters; Wos:A1986a219600007; Times Cited: 26; ISI Web of Science |
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CBU @ c.wolke @ 14751 |
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93 |
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Lovell, H.L. |
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Mine Water Treatment Control |
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Journal Article |
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1971 |
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Min. Congr. J. |
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57 |
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6 |
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83-& |
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mine water treatment |
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Mine Water Treatment Control; Wos:A1971j677200018; Times Cited: 0; ISI Web of Science |
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CBU @ c.wolke @ 9264 |
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102 |
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Author |
Benkovics, I.; Csicsák, J.; Csövári, M.; Lendvai, Z.; Molnár, J. |
Title |
Mine Water Treatment – Anion-exchange and Membrane Process |
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Journal Article |
Year |
1997 |
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Proceedings, 6th International Mine Water Association Congress, Bled, Slovenia |
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1 |
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149-157 |
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uranium mining Hungary Mecsek Ore Mining Company waste water mine water chemistry nano-filtration reverse osmosis pilot plant mine water treatment treatment |
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Mine Water Treatment – Anion-exchange and Membrane Process; 1; FG 6 Abb., 2 Tab.; AMD ISI | Wolkersdorfer |
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CBU @ c.wolke @ 9530 |
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455 |
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