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Selenium Removal from Mine Waters

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Low operating cost. Passive. Demonstrated Chemistries. Adsorption or co-precipitation by Fe(III) hydroxides. Biological (bacterial reduction) ... – PowerPoint PPT presentation

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Title: Selenium Removal from Mine Waters


1
  • Selenium Removal from Mine Waters
  • Raymond J. Lovett, Ph.D.
  • Environmental Chemist
  • ShipShaper, LLP
  • Morgantown, WV

2
SUPPORT
  • National Mine Land Reclamation Center, West
    Virginia University
  • United States Office of Surface Mining
  • Magnum Coal Company
  • Catenary Coal

3
Typical Southern West Virginia Mine Water
  • Se 13 ug/L
  • Fe 0.15 mg/L
  • SO4-2 980 mg/L
  • Alkalinity 235 mg/L as CaCO3
  • pH 7.1

4
Problems
  • Overriding Concern
  • Regulatory limit near 5 ug/L
  • Specific Problems for Treatment
  • Low level of Se
  • Differing chemistries
  • Selenate, SeO4-2, Se(VI)
  • Selenite, SeO3-2, Se(IV)

5
Selenium Removal Difficulties
  • Different dissolved species
  • No direct precipitation chemistries
  • Reduction of selenate is difficult (slow)
  • Sulfate may interfere

6
Treatment System Objectives
  • Effluent maximally 5 ug/L Se
  • Low installation cost
  • Low operating cost
  • Passive

7
Demonstrated Chemistries
  • Adsorption or co-precipitation by Fe(III)
    hydroxides
  • Biological (bacterial reduction)
  • Reverse osmosis
  • Reduction by Fe(0)

8
Reduction with Iron Metal
  • SeO4-2 Fe(0) gt Fe(II,III) Se(0)
  • SeO3-2 Fe(0) gt Fe(II,III) Se(0)

9
Selenium Species on Iron
10
Field TrialCatenary Coal
  • Test in a real setting
  • Real, variable input chemistry
  • Continuous Se Input

11
Field Trial System
12
Field Trial System
13
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18
Catenary Post Trial 1
19
Catenary Post Trial 2
20
Catenary Post Trial 3
21
Catenary Post Trial 4
22
Catenary Post Trial 5
23
Reduction with Iron Metal
  • Potential
  • Removal of selenate and selenite
  • Passive
  • Problems
  • Iron Oxides/ Dissolved Fe, Mn
  • Exhaustion
  • Passivation
  • Expense (surface area)

24
BacterialEstimated Cost
  • Flow 285 gpm
  • Capital Cost 7.2 to 10 million
  • OM Unknown

25
Reverse OsmosisEstimated Cost
  • Flow 200 gpm
  • Capital Costs 1.2 million
  • OM 5.85 million/year

26
Iron HydroxideEstimated Cost
  • Flow 200 gpm
  • Capital Cost 0.69 to 1.03 million
  • OM 1.39 million/year

27
Zerovalent IronEstimated Cost
  • Flow 250 gpm
  • Capital costs 478,000
  • OM 150,000 to 300,000
  • Gravity flow, includes surge

28
Conclusions
  • Iron metal removes selenate and selenite, but
    currently requires long contact times
  • Manganese and iron generated
  • Temperature sensitive (?)
  • Less expensive than other methods
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