QLD Coal Mines - Waterlogged Presented by Greg Tobin BTX Group Pty - - PowerPoint PPT Presentation

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QLD Coal Mines - Waterlogged Presented by Greg Tobin BTX Group Pty - - PowerPoint PPT Presentation

QLD Coal Mines - Waterlogged Presented by Greg Tobin BTX Group Pty Ltd Contents Introduction What is the problem? Water What is in it? Options Where can we use it? Treatment methods discussed Cost Comparison RO


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QLD Coal Mines - Waterlogged Presented by Greg Tobin BTX Group Pty Ltd

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Contents

  • Introduction – What is the problem?
  • Water – What is in it?
  • Options – Where can we use it?
  • Treatment methods discussed
  • Cost Comparison
  • RO cost benefit analysis
  • Conclusion
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INTRODUCTION

  • Problem - too much water stored on site.

– 2010/2011 Floods; – DERM maintain strict release criteria; – Typically creeks need to be running for release – Total Dissolved Solids (TDS) above DERM guidelines It is estimated that QLD coal mines hold approximately 300 gigalitres

  • f locked up water, the equivalent of half of Sydney Harbour (ref

QRC). It has been suggested that the locked up water is holding up 25 million tonnes of coal production (Ref John McCarthy, Syd Telegraph)

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Water - What is in it?

  • Ec or total dissolved solids
  • Leached from groundwater/coal
  • DERM water discharge guidelines

– TDS <1000 mg/l (Ec 1500 microsiemens) – Turbidity <300 NTU, pH <8.8 – Sulphates, chlorides, cations, heavy metals limits

  • Why is it difficult to treat?

– Solubility of Sulphates and Chlorides in the presence of Sodium, Potassium and other metals

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Typical Pit Water Analysis

Test Units Result pH pH unit 8.67 Electrical Conductivity microsiemens 9051 Total Alkalinity as CaCO3 mg/L 545 Sulphate mg/L 438 Chlorides mg/L 2810 Calcium mg/L 47 Magnesium mg/L 86 Sodium mg/L 1910 Cadmium mg/L <0.0001 Lead mg/L <0.001

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Water use/reduction options

  • Irrigate
  • Road dust suppression
  • Evaporate
  • CHPP use
  • Precipitate impurities
  • Deionization/Softening
  • Reverse Osmosis
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Treatment methods

  • Irrigate

– High salts can damage top soil for farming/vegetation; – Real estate requirements;

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DUST SUPPRESSION

  • ACARP report C14040 covers this area.
  • Need to consider impact of salts on road users.
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Evaporation

Evaporation rates in central Queensland are in the area of 2 metres annually. Depending on surface area in a dam, water loss is 5 to 10 % PA. Rates dependent on temperature humidity, wind speed. Now, pumps and evaporators are controlled by mini weather stations so they only operate when the temperature and wind direction is suitable. Rates are increased but depends on spray coverage and droplet size.

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  • CHPP use

– High dissolved solids will increase corrosion and scale potential significantly – Can treat scaling or corrosion separately or together. – Typical Corrosion or Antiscalant treatment program cost $300,000 to $500,000 p.a. – Scale control - Acrylate, polyphosphates, PMA – Corrosion control – Zinc, polyphosphates, molybdates

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Control Corrosive Waters

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Corrosion Rate

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Control Scaling Waters

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Precipitation Softening

  • Reduces hardness, alkalinity, silica and other

constituents

  • Treat with Lime, Soda Ash and Lime
  • Calcium Bicarbonate converts to Calcium Carbonate
  • Magnesium forms insoluble Magnesium Hydroxide
  • Permanent hardness more difficult to remove
  • Sodium Aluminate can reduce Magnesium and Silica
  • Soda Ash can reduce permanent Calcium hardness
  • Heavy metal removal
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Sulphate Reduction

  • Many options available depending on level
  • Reverse osmosis
  • SPARRO – Slurry precipitation followed by RO
  • EDR- Electrodialysis Reversal
  • Precipitation of Gypsum with Lime addition
  • Biological Sulphate Reduction or Bioreactors
  • Depending on Sulphate level Bioreactors are very

cost effective after Lime precipitation

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Sulphate reduction plant costs for 1 meg/day plant

  • RO – Capex – $1.15M, Opex -$1.22/m3
  • SPARRO - Capex – $1.2M, Opex -$0.42/m3
  • EDR - Capex – $1.0M, Opex -$0.67/m3

– High maintenance, 99% removal

  • Lime - Capex – $.0325M, Opex -$.085/m3

– Low maintenance, 50% sulphate removal

  • Bioreactor - Capex – $0.45M, Opex -$0.425/m3

– Moderate maintenance, <90% removal

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Reverse Osmosis Selectivity

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Reverse Osmosis (cont’d)

  • Reverse Osmosis

– Reduces the amount of dissolved solids in water; – Process that separates H20 from salts; – Produce a permeate and brine;

  • RO Cost (produce 500kL/day of permeate)

– New plant installation - $0.75M upfront & 25K/month to run – Hire RO plant installation - $150K upfront & 45K/month to run

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RO Elements Removed

Elements and the Percent R.O. Membranes will remove

  • Sodium
  • Sulfate
  • Calcium
  • Potassium
  • Nitrate
  • Iron
  • Zinc
  • Mercury
  • Selenium
  • Phosphate
  • Lead
  • Arsenic
  • Magnesium
  • Nickel
  • Fluoride
  • Manganese
  • Cadmium
  • Barium
  • Cyanide
  • Chloride

85 - 94% 96 - 98% 94 - 98% 85 - 95% 60 –75% 94 – 98% 95 – 98% 95 – 98% 94 – 96% 96 – 98% 95 – 98% 92 – 96% 94 – 98% 96 – 98% 85 - 92% 94 – 98% 95 – 98% 95 – 98% 84 – 92% 85 – 92%

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Typical RO setup at a mine

Pit Water Waste Drying Cell Feed Tank 40m3 Permeate Tank 30m3 Waste Tank 30m3

Discharge off site or use to dilute other pit water (500kL per day) Filtration RO plant in a shipping container

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Example of blending RO water with Pit Water

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Deionization vs RO

Deionization

  • Capex similar to RO
  • Removes all anions and cations

by resin beds

  • Purity progressively worse
  • Ion exchange chemicals

expensive

  • Uses Hydrochloric and Caustic
  • Requires hazardous disposal

permit for resin

  • Pure water is 1 microsiemens
  • Regeneration waste to deal with

Reverse Osmosis

  • Membrane filtration
  • RO purity continuous
  • Lower Opex on chemicals
  • Can remove SS, viruses
  • Lower cost of operation
  • Membrane life similar to beds
  • Membranes require cleaning
  • Chemical addition required
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Conclusions

  • Need to work closely with DERM to get reasonable

Environmental Agreement.

  • Method of treatment dependent on the water

quality.

  • Each mine site is different and you need a detailed

study initially.

  • With the water analysis presented RO would appear

most suitable for approach.

  • Managing brine needs further consideration.
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Acknowledgements

  • Many thanks to the Queensland Branch of the

ACPS for inviting me to give this talk.