Poster Karowe Comminution Circuit upgrade 27-07-2015

1
Karowe Comminution Circuit Upgrade P. Morgan 1 , L. van Niekerk 1 , M. Duddy 1 , G. Underwood 2 and A. Paz 3 1. DRA Global, Johannesburg, No. 3 Inyanga Close, Sunninghill, 2157, South Africa, [email protected], [email protected], [email protected] 2. Minopex, 7 Pinswood Office Park, 33 Riley Rd, Woodmead, 2196, [email protected] 3. Outotec Australia, 40 Kings Park Road, 6005 WA West Perth, Australia, [email protected] Boteti are due to begin treating the significantly more competent (Unit13) kimberlites at their Karowe Diamond plant, Botswana & wish to continue with AG milling as the “heart” of their process flow sheet. Aim: Assess current performance of the AG mill; Assess impact of treating harder kimberlites & increased throughput in the new/modified flowsheet; A Turbo-Pulp Lifter (TPL TM ) system is anticipated to improve upon the original mill grate/pan lifter operation. Interpreted Abrasion Factor, t a Interpreted ta 13 FK S2 S1 y = 2.4x -1 Apparent Dwi (kW/m 3 ) Observed Relative Grinding Rates Relative Grinding Rates & DWi Relationship Relative Hardness (Energy Basis) 13 S1 S2 FK U1 SL New Circuit Design Outotec will provide their innovative Turbo Pulp Lifter (TPL TM ) system to improve the discharge & grate efficiency; Two TPL™ designs will be incorporated: 90mm pebble ports for treatment of fragmented kimberlites (FK); 115mm pebble ports for hard kimberlites (Unit 13), early 2015. Turbo-Pulp Lifter (TPL™) DRA used an ‘in-house’ modelling tool to compare against Outotec’s JKSimMet to assess the proposed circuit; Two surveys (S1 & S2) indicated that grate ports were ‘clogging up& pan lifters were ‘retaining material’ that should escape the mill; Minerals being processed: Unusually hard for a kimberlite; Very abrasive, high DMS yields; Have high crushing strength; Low amenability to scrubbing; Large degree of variability (soft sandstones & weathered kimberlites, to more competent kimberlites, mudstones & basalts). Using this relationship it was possible to simulate the mill-crusher circuit performance when ‘treating’ the harder ores; Initial design trial simulations indicated that partial pre-crushing, modified grate design & bypass screening was necessary to control the mill overloading; Less fines were going to be produced, potentially overloading the existing DMS circuit; High DMS yields are also anticipated on harder ores. Simulation Results Circuit Benefits Back- ground Weathered & soft Bulk Sample Milling plant sampling audit 2 Milling plant sampling audit 1 Fragmented Kimberlite Unit 13 Hard Kimberlite Deeper material is more competent The fully- autogenous mill: offers flexibility for high variability in the ore; combines crushing & scrubbing steps; A secondary gyratory crusher will crush a proportion of jaw crusher product for a consistent feed to the AG mill; Mill discharge screen recycles +60mm directly & combines with -60mm+32mm LDR tails to the existing pebble crusher; Pebble crusher product can be partially split to bypass mill recycle; XRT bulk sorting for Large Diamond Recovery (LDR); -8mm+1.5mm fraction will be treated in the existing DMS; TPL™ for improved mill capacity & efficiency. Benchmarking showed that the mill would receive material significantly harder in the future (Unit 13) than seen in the past (S1 & S2). Good Attrition Good Impact Slurry Pool Poor Impact Improper Attrition Turbo Pulp Lifter™ Radial Pulp Lifter Sample Population Dwi (kW/m 3 ) Karowe Drop Weight Testwork SMC Karowe Data PopulationDistributionModel FK 13 S2 S1 A significant degree of hardness variation is shown, that prescribes virtually the complete spectrum of DWi values. Published DWi database distribution superimposed PEBBLE CRUSHER MILL FEED STOCKPILE MILL FEED PRE-CRUSHER EXISTING MILL +60mm +1.5x60mm FINES DMS JAW CRUSHER -1.5mm LARGE DIAMOND RECOVERY (LDR) LARGE DIAMOND RECOVERY (LDR) CONCENTRATE PEBBLE BLEED SPLITTER - 32mm +32x60mm +20x32mm LARGE DIAMOND RECOVERY (LDR) MIDDLES BULK SORTER LARGE DIAMOND RECOVERY (LDR) FINES BULK SORTER -20mm +1.5x8mm TERTIARY CRUSHER and DEWATERING +8x14mm +14x32mm 1 7 8 14 15 16 17 12 20 18 +8x60mm 19 4 2 5 6 9 10 11 13 ROM FEED THICKENER FEED GRITS TAILS RECOVERY FEED CONCENTRATE Current Circuit Constraints (-8mm) Legend: T = Tails C = Concentrate T T C C +32mm +1.25x8mm -1.25mm +1.25x8mm BLEED SCREENING T C

Transcript of Poster Karowe Comminution Circuit upgrade 27-07-2015

Page 1: Poster Karowe Comminution Circuit upgrade 27-07-2015

Karowe Comminution Circuit Upgrade

P. Morgan1, L. van Niekerk1, M. Duddy1 , G. Underwood2 and A. Paz3

1. DRA Global, Johannesburg, No. 3 Inyanga Close, Sunninghill, 2157, South Africa, [email protected], [email protected], [email protected]

2. Minopex, 7 Pinswood Office Park, 33 Riley Rd, Woodmead, 2196, [email protected]

3. Outotec Australia, 40 Kings Park Road, 6005 WA West Perth, Australia, [email protected]

Boteti are due to begin treating the significantly more competent (Unit13) kimberlites at their Karowe Diamond plant, Botswana &

wish to continue with AG milling as the “heart” of their process flow sheet.

Aim: – Assess current performance of the AG mill;

– Assess impact of treating harder kimberlites & increased throughput in the new/modified flowsheet;

– A Turbo-Pulp Lifter (TPLTM) system is anticipated to improve upon the original mill grate/pan lifter operation.

Interpreted Abrasion Factor, ta

Interpreted ta13

FK

S2

S1

y = 2.4x-1

Ap

pare

nt

Dw

i(k

W/m

3)

Observed Relative Grinding Rates

Relative Grinding Rates &DWi Relationship

Relative Hardness(Energy Basis)13

S1

S2

FK

U1

SL

New Circuit Design

• Outotec will provide their innovative

Turbo Pulp Lifter (TPLTM) system to

improve the discharge & grate efficiency;

• Two TPL™ designs will be incorporated:

• 90mm pebble ports for treatment of fragmented kimberlites (FK);

• 115mm pebble ports for hard kimberlites (Unit 13), early 2015.

Turbo-Pulp

Lifter (TPL™)

• DRA used an ‘in-house’ modelling tool to compare

against Outotec’s JKSimMet to assess the proposed circuit;

• Two surveys (S1 & S2) indicated that grate ports were ‘clogging

up’ & pan lifters were ‘retaining material’ that should escape the mill;

• Minerals being processed:

• Unusually hard for a kimberlite;

• Very abrasive, high DMS yields;

• Have high crushing strength;

• Low amenability to scrubbing;

• Large degree of variability (soft

sandstones & weathered kimberlites,

to more competent kimberlites,

mudstones & basalts).

• Using this relationship it was possible to

simulate the mill-crusher circuit

performance when ‘treating’ the

harder ores;

• Initial design trial simulations

indicated that partial pre-crushing,

modified grate design & bypass

screening was necessary to control the

mill overloading;

• Less fines were going to be produced,

potentially overloading the existing DMS circuit;

• High DMS yields are also anticipated on harder ores.

Simulation

Results

Circuit

Benefits

Back-

ground

Weathered

& soft

Bulk

Sample

Milling plant

sampling

audit 2

Milling plant

sampling

audit 1

Fragmented

Kimberlite

Unit 13 Hard

Kimberlite

Deeper material is

more competent

• The fully-

autogenous mill:

offers flexibility for high

variability in the ore;

combines crushing &

scrubbing steps;

• A secondary gyratory crusher will crush a

proportion of jaw crusher product for a consistent

feed to the AG mill;

• Mill discharge screen recycles +60mm directly & combines

with -60mm+32mm LDR tails to the existing pebble crusher;

• Pebble crusher product can be partially split to

bypass mill recycle;

• XRT bulk sorting for Large Diamond

Recovery (LDR);

• -8mm+1.5mm fraction will be

treated in the existing DMS;

• TPL™ for improved

mill capacity &

efficiency.

Benchmarking

showed that the mill

would receive material

significantly harder in the

future (Unit 13) than

seen in the past

(S1 & S2).

Good

Attrition

Good Impact

Slurry

Pool

Poor Impact

Improper

Attrition Turbo

Pulp

Lifter™

Radial

Pulp

Lifter

Sam

ple

Po

pu

lati

on

Dwi(kW/m3)

Karowe Drop Weight Testwork

SMC Karowe Data

PopulationDistributionModel

FK

13

S2

S1

A significant degree of hardness

variation is shown, that prescribes

virtually the complete spectrum

of DWi values.

Published DWidatabase

distribution superimposed

PEBBLE CRUSHER

MILL FEED STOCKPILE

MILL FEED PRE-CRUSHER

EXISTING MILL

+60mm

+1.5x60mm

FINES DMS

JAW CRUSHER

-1.5mm

LARGE DIAMOND RECOVERY

(LDR)

LARGE DIAMOND RECOVERY

(LDR)

CONCENTRATE

PEBBLE BLEED SPLITTER

- 32mm

+32x60mm

+20x32mm

LARGE DIAMOND RECOVERY

(LDR)

MIDDLES BULK

SORTERLARGE DIAMOND

RECOVERY (LDR)

FINES BULK

SORTER

-20mm

+1.5x8mm

TERTIARY CRUSHER and DEWATERING

+8x14mm

+14x32mm

1

7

8

14

15

16

17

12

20

18

+8x60mm

19

42

56

9 10

11

13

ROM FEED

THICKENER FEED

GRITS

TAILS

RECOVERY FEED

CONCENTRATE

Current

Circuit

Constraints

(-8mm)

Legend:

T = Tails

C = Concentrate

T

T

C

C

+32mm

+1.25x8mm

-1.25mm

+1.25x8mm

BLEED

SCREENING

T C