19
23-4-2012 Economical recovery of base metals from leach streams after gold recovery Date: Place: Author: In collaboration with:

Economical recovery of base metals from leach streams … · Economical recovery of base metals from leach streams after gold recovery ... Gold Iron/gypsum sludge Zinc sulfide Copper

  • Upload
    vumien

  • View
    218

  • Download
    1

Embed Size (px)

Citation preview

23-4-2012

Economical recovery of base metals from leach streams

after gold recovery

Date:

Place:

Author:

In collaboration with:

2

• Background

• Metal sulfide precipitation

• Thioteq process

• Case 1

• Case 2

• Economics

• Conclusions

Content

3

Common sight near mining operations

4

Has been, and still is, accepted treatment, but:

• Moderate effluent sulfate (1500 - 2000 mg/L SO4)

• High Dissolved Solids output

• Long-term environmental liabilities

• Increasing costs for reagents and sludge storage

• Resources are wasted (metals & chemicals)

Reason: Simple lime treatment

5

• Acid mine drainage treatment

Consumes 30% of total lime consumption for

wastewater treatment

• Results in approx. 80 Mton/a of heavy metal

polluted gypsum

• Conversion of CaCO3 + fuel to CaO releases CO2

Sustainability?!

6

Step 1: Metals

• Metal removal as metal sulfide (not hydroxide)

– Low solubility

– Recovery of metals

– Compact sludge

Step 2: Sulfate

• Removal of dissolved sulfate as:

– Clean gypsum (construction material) or

– Elemental biosulfur

Solution ?

7

(In-)Solubility of Metal Sulfides

CdS

PbS

NiS

As2S3

Zn(OH)2

Cd(OH)2

Ni(OH)2

NiS

Ni(OH)2

Cu(OH)2

Pb(OH)2

CuS PbS

ZnS

ZnS

pH

Soluble metal concentration [mg/L]

8

• Buy it: Transport and storage

– Dangerous and expensive

• Make it: Chemical production on-site

– High investment costs

– Dangerous

Sulfide!? Where from??

Safe & Reliable biotechnology makes it possible

9

• What is Thioteq™ process?

– Safe and economic base metal recovery from low-concentrated (50 ~ 1000 mg/l) leach & bleed streams

• What does Thioteq™ produce?

– Pure & compact high quality sulfide precipitate

• What does Thioteq™ consume?

– Elemental sulfur, ethanol (or equivalent) and fertiliser-like nutrients

THIOTEQ™ PROCESS

10

Advantages: Cheap and safe H2S production Water conditions no issue Selective MeS recovery possible Better than settling & dewatering, and

lower costs than with NaSH

Block diagram

Disadvantages: No sulfate removal pH drops

Sulfur-feed

E-donor (Alcohol, acetate

or H2)

Rich gas Metal sulfides

product

Process stream with

dissolved metals

Lean gas

23-4-2012

Biologically produced H2S

Solid

elemental

sulfur (S80)

-

Hydrogen

sulfide

(H2S)

- H

Dissolved elemental

sulfur (polysulfide)

- H

Sulfur

reducing

bacteria

Overall conversion:

S0(s) + H2(g->l) -> H2S(l->g)

Mechanism:

23-4-2012

Example: Copper recovery

INFLUENT (mg/l) EFFLUENT (mg/l) Leach water Copper 200 < 1 Ground water Zinc 82 < 0.2 Aluminium 2412 < 2 Calcium 450 50 Copper 44 < 0.1 Iron 512 < 0.1 Magnesium 2640 990 Manganese 200 < 0.4 Sulfate 25000 < 500

13

Example of selective metal recovery

Sulfur-feed

E-donor (Alcohol, acetate

or H2)

Rich gas As2S3

Lean gas

CuS

23-4-2012

POX at gold mine

15

Case 1: Base metal recovery after pressure leach

PAL Gold

recovery Iron

removal

THIOTEQ

Copper & zinc

recovery

Final

neutralisatio

n

Gold Iron/gypsum

sludge

Zinc

sulfide Copper

sulfide

Gypsum

Water

recycle /

discharge

• Recovery of 50 kton/yr copper as CuS

• Elemental sulfur & ethanol as main consumables

16

• CCD wash solution: 1,900 m3/hr

• Zn: ~870mg/L, Cu ~ 285 mg/L

• Base water treatment case:

• Assume metal net back • Zn (38 ton/d) @ 0.65 $/lb & Cu (5.9 ton/d) @ 2.13 $/lb

Base metal revenue possible: 30 M$/yr

Example 2: Mine with POX

17

• Optimal solution: Combination of Thioteq with lime/gypsum

Mine with oxidative leach

Iron removal Copper precipitation Zinc precipitation Final neutralisation

CaCO3 CaCO3 / Ca(OH)2

Optional : Air CaSO4 CuS ZnS CaSO4

Fe(OH)3 Al(OH)3

AsO4 H2S gas recycle Fe(OH)2

THIOTEQ bioreactor

Sulphur H2 gas from reforming LPG

Iron removal Copper precipitation Zinc precipitation Final neutralisation

18

Economics

18

• Effluent: 1,200 m3/hr with Zn: ~880 mg/l & Cu ~ 110 mg/L

• Zn: 24 tpd @ 1.19 US$/lb & 55% Net back

• Cu: 3.2 tpd @ 2.5 US$E/lb & 85% Net back

• Estimated capital investment: 23 million US$

Revenue Zn recovery $ 12,605,505 Cu recovery $ 5,535,297

Chemicals Sulfur $ -698,676

E-donor $ -973,090

Other $ -206,590 Power

Bioreactor $ -185,274 Contactors $ -19,710 Others $ -74,110

Labor $ -700,000

Maintenance $ -690,000 Earnings $ 14,593,352 Depreciation (10 years) $ -3,743,144 Nett annual earnings $ $10,850,208

19

• Biobased process enable efficient recovery of low

concentrated metal-containing streams

• Selective recovery of base metals

• High grade concentrate-like products

• Better effluent quality, increase sustainability

• Cleaner gypsum product

• THIOTEQ is flexible, reliable & safe

Conclusions