Relevant publications from Dr Steve Morrell in the field of comminution.

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Physical and Morphological Characteristics of Iron Ore and their Routes of Comminution

Stephen Morrell

OBJECTIVE

Answer the questions:

Is there an association between the properties of iron ore deposits and the design of the comminution circuit?

If so, what is it?

CONTENT

  • Relevance of comminution
  • Common types of equipment
  • Properties of iron ore-bodies
  • Ore hardness
  • Grinding circuit designs

Comminution Relevance

  • Increasing world trend to process low grade Fe deposits
  • Comminution circuit Capex to produce a 10 mtpa Fe concentrate facility could be as high as US$ 1 billion
  • Comminution circuit operating costs can account for 65% of total costs
    • Comminution circuit is a major contributor to project financial viability

Comminution Equipment

  • Crushers
  • High Pressure Grinding Rolls
  • Tumbling mills
    • Autogenous and Semi-autogenous (AG/SAG)
    • Ball Mills
  • Stirred mills
    • Vertical
    • Horizontal

Jaw Crushers

1200-1500 tph

page 5 Picture 5
page 5 Picture 6
page 5 Picture 7

Gyratory Crushers

5000-7000 tph

Toothed Roll Crushers

5000-7000 tph

page 7 Picture 5
page 7 Picture 6
page 7 Picture 7

Cone Crushers

page 8 Picture 4
page 8 Figure 5

Secondary: 1200-1500 tph

Tertiary: 400-500 tph

High Pressure Grinding Rolls

Tertiary/quaternary: 2500-3200tph

page 9 Picture 3
page 9 Picture 4
page 9 Picture 5
page 9 Picture 8
page 9 Figure 9
page 10 Picture 3

Operating:

Up to 40ft diameter

24 MW motor

Under construction:

40ft x 36ft

28MW motor

Iron ore

On order:

42ft x 22ft

28 MW motor

Ball Mills

page 11 Picture 4

Operating:

Up to 27ft diameter 18 MW motor Under construction:

22 MW motor

28ft diameter

Tower & Vertimills

page 12 Picture 4
page 12 Picture 5
page 12 Picture 6
page 12 Picture 7
page 12 Picture 8

Up to 2.25 MW motor

Down to 20 microns

IsaMill

page 13 Picture 4
page 13 Picture 5

Up to 3MW motor

Down to 10 microns

page 13 Picture 8
page 13 Figure 9
page 13 Picture 10

Iron Ore Properties

  • What is Morphology?
  • "Characteristics, configuration and evolution of rocks"
  • "Origin, formation and mineral composition"

Structure

page 15 Picture 4
page 15 Picture 5
page 15 Picture 6
page 15 Picture 7

Weathering

page 16 Picture 4

Mineral Content

page 17 Picture 4

magnetite

page 17 Picture 6

hematite

page 17 Picture 8

limonite

page 17 Picture 10

goethite

Micro-structure

page 18 Figure 4

Relationships?

• Do any of these relate to grinding circuit design?

Relationships?

• Yes and No

Relationships?

• Yes

– they all contribute in some way

But

• No

  • not in any universal way related to morphology
  • there are other factors
  • Often several comminution routes are equally technically viable

However

  • There are some general rules
    • So what are the drivers?

DRIVERS

Grade: high and low grade have different processes

Grain size: affects number of size reduction stages

Hardness: affects size and type of equipment

Hardness variability: affects type of equipment

Capex/Opex: dictates final choice between suitable designs

Local preference (prejudice): may overrule all others

GRADE

page 23 Figure 4

GRAIN SIZE

page 24 Figure 4

To be able to concentrate low grade ore need to grind to liberate Fe oxides

The smaller the grain size of Fe oxides the finer the grind

The fineness of the grind influences circuit design, eg more stages

HARDNESS

  • Influences circuit design and equipment size
  • Need a relevant hardness measurement
    • Bond work index: crushing, rod, ball; UCS; IS50; SPI®; JK drop-weight; SMC Test ®
  • Must have proven correlation with comminution equipment performance
  • Need big data base for benchmarking
  • Must be easy to do, eg should be able to use small diameter drill core

SMC Test®

Drill Core Samples PQ, HQ, NQ

page 26 Picture 5

Break in laboratory device:

16 laboratories worldwide

page 26 Picture 8

Hardness Parameter DWi

Predict AG/SAG/Crusher/HPGR

- Crushers

page 27 Figure 4

- HPGRs

page 28 Figure 4

- AG/SAG

page 29 Figure 4

DWi DATA BASE

Over 17000 tests done to date

Over 700 different ore deposits

page 30 Figure 6

DWi Distribution

page 31 Figure 4

Magnetites (low grade)

page 32 Figure 4

Hematites (high grade)

page 33 Figure 4

Hematites

(low and high grades)

page 34 Figure 4

Comminution Circuit Designs

Blasting

• Good comminution circuit design starts with good blasting design

page 36 Picture 5

Blasting

page 37 Picture 4

Bad

page 38 Picture 4

Better

page 39 Picture 4

BLASTING

  • Needs to be tailored to process requirements eg,
    • DSO minimise fines production
    • Fine grained magnetite maximise fines production

HIGH GRADE CIRCUITS

DSO Circuit

page 42 Picture 4

Maximise lump:fines ratio:

Minimise amount of size reduction in a single step

Minimise handling

Start with highest natural lump as possible

DSO Circuit

page 43 Figure 4

Sizers maximise natural lump

Don't forget influence of blasting

Sizer vs Gyratory

page 44 Figure 4

LOW GRADE CIRCUITS

Crush-Ball

page 46 Figure 4

One of oldest circuits

Now normally only used with very hard ores and small operations

HPGR-Ball

page 47 Figure 4

Increasingly popular with harder ores

High unit capacities of HPGRs favour large scale processing

Energy saving advantage only seen with hard ores and coarse grind

Good with deposits with variable hardnesses

AG/SAG-

page 48 Figure 4

SAG circuits usually have pebble crushers for harder ores

AG circuits usually have pebble crusher

AG/SAG-

page 49 Figure 4

SAG good for very high capacity

SAG/ball particularly good for softer ores (Itabirites?)

AG/pebble favoured for fine grinding and hard ores

AG not good with deposits with high hardness variability

Not good for low grade magnetite as can't concentrate after AG/SAG

Claim by some that AG/SAGball gives more slime production than crush-ball.

Evidence(?)

SLIMES

No evidence that slimes generation is any different

page 50 Figure 5

Closed Circuit AG/SAG

page 51 Picture 3
page 51 Picture 4

Closed AG/SAG enables early gangue rejection

Secondary circuit able to reach relatively fine grinds – AG/pebble can get down to 38 mm; ball mill more comfortable at 75 mm

Need harder low variability deposits for AG.

SAG/ball better for softer and more variable ores but may need extra stage for fine grind

AG/Pebble lower Opex and higher Capex compared with SAG/ball

Fine grinding

page 52 Figure 4

Fine grinding stage needed for some ores and/or where SAG/ball or HPGR/ball used as these generally find it hard to reach very fine grinds efficiently

Verti/tower mill

Fine grinding

page 53 Figure 4

Fine grinding

page 54 Figure 4

IsaMill vs Vertimill

page 55 Figure 4

Capex/Opex

rock media steel media
$/t $/t
OPEX
Grinding media&liners 0.5 1.8
Power 3.8 3.5
Carbon tax 0.7 0.6
Other 1.8 1.9
Total 6.8 7.8
Index 0.87 1.0
CAPEX
Index 1.1 1.0

Conclusions

  • High grade crush, screen only
  • Low grade
    • Needs concentration therefore need milling
    • Finer grain size needs more stages
    • Autogenous/pebble milling better for finer grinding and harder, uniform ores
    • SAG/ball milling better for softer more variable ores and less fine grinding; Vertimill/IsaMill stage may be needed for finer grinding
    • HPGR/ball good for harder more variable ores;Vertimill/IsaMill stage may be needed for finer grinding
    • Often several circuits technically suitable for a given ore so Capex/Opex to decide
    • Autogenous routes lower on OPEX and higher on CAPEX
Physical And Morphological Characteristics Of Iron Ore And Their Routes Of Comminution

Physical And Morphological Characteristics Of Iron Ore And Their Routes Of Comminution

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