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Paul Eger, Global Minerals /Sovereign Consulting Peggy Jones, Doug Green, American Peat Technology Igor Kolomitsyn, Natural Resources Research Institute.

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Presentation on theme: "Paul Eger, Global Minerals /Sovereign Consulting Peggy Jones, Doug Green, American Peat Technology Igor Kolomitsyn, Natural Resources Research Institute."— Presentation transcript:

1 Paul Eger, Global Minerals /Sovereign Consulting Peggy Jones, Doug Green, American Peat Technology Igor Kolomitsyn, Natural Resources Research Institute

2  Problem  Peat Based Sorption Media  Why should it work?  Testing  Application  On going work

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4  Coal mine drainage  pH 6-9  Aluminum  Maximum 0.750 mg/l  Average 0.43 mg/l  Guilty until proven innocent  Limits enforced as total

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6 PBR to the rescue! Peat Based Remediation

7  Convert peat into engineered media  APTsorb TM  Patented peat based sorption media  Hardened granule  APTsorb TM Granule

8  Size 0.6 to 2 mm  Large surface area  High hydraulic conductivity (~1 cm/sec)  High metal affinity (1-15% max dry wgt) APTsorb TM Granule 2000x

9 Why would this work?

10  Dissolved  Adsorption  Ion Exchange  Complexation  Chelation  Particulate  Physical Filtration  Sorption

11 Fine Sand APTsorb 100 X 1000 X 1500 X

12 Case Study

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14  Closed underground iron mine  Minnesota State Park  TSS 5-10 mg/L  Mine water; 30 - 40 ug/L Cu  Permit limit:17 ug/L  75 % is suspended 8-10 ug/L dissolved < 17 ug/L

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16  Treatment tank  1000 gallon  500 gallons media  Typical flow 50 gpm  Contact time 10 min  Designed to backwash

17 APTsorb

18 Average removal = 75%

19  One year successful treatment  Remotely monitored  Minimal maintenance  Backwash every 4-6 weeks  Eliminated solids from media  Restored pressure drop to initial value  Cost < 25 cents / 1000 gallons

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21  Treated coal mine drainage  Active treatment process  Clarifier effluent  Passive system effluent  Final pond effluent  Typical water quality  pH 7-8  Al 0.5- 1.5 mg/L

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23 Series filtration Clarifier Effluent Al (ppb) Percent removal Particle size No filtration3970 25 µm1845454%>25µm 8µm18254 5 µm12569 0.8 µm10175 0.45 µm4888 0.45 µm<86% 0.1 µm3192 pH 7.7

24 Series Filtration Pond effluentAl (ppb)% removalParticle Size No filtration225.70% 25µm209.457% 8.0µm163.128% 5.0 µm26.7888%5µ<60%<8µ 88%>5 µ 0.8 µm27.0188% 0.45 µm26.8888% 0.20 µm34.9685% 0.10 µm35.1584% pH 8.9

25 Column Test Diameter 1 in Length 8 in Flow Rate 10ml/min Contact Time 10 min

26 70-80% removal

27 Semi active Passive

28 Passive filter bed Peat based sorption media

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30  Peat based sorption media effectively removes suspended metals  Removes smaller particles than typical sand filter  Cost effective  Semi active: < $0.25 per 1000 gallons

31  Altering media  Chemical modification  Addition of functional group  Target specific analytes

32 ProductsMarket niche APTsorb II Removal of heavy metals: Cd, Cu, Zn, Pb, etc. APTsorb III Removal of heavy metals: Cd, Cu, Zn, Fe. No leaching of Mn, Fe, Ca into the effluent Lower concentration of metals in the effluent APTsorb II*Na High selectivity for Cd removal in the presence of Zn. Up to 3 mg/g Cd at influent Zn > 30 ppm Still evaluation other benefits.

33 Sulfate granule

34 Global Minerals Engineering

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36 Is this finally the end of the shameless promotions?

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38 When will this end?

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43 Series filtration Clarifier Effluent Al (ppb) Percent removal Particle size No filtration3970 25 µm1845454%>25µm 8µm18254 5 µm12569 0.8 µm10175 0.45 µm4888 0.45<34%<25 0.1 µm3192 pH 7.7


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