crusher investigation report name of investigators

12
CRUSHER INVESTIGATION REPORT Report No; 01 Contract; Kasane Airport Contract No; 60948 Location; Lesoma Quarry Date of Investigation; From Tue 05/06/2012 to Sun 10/06/2012 Name of Investigators; Benard T Ruwona & Shawn A Potgieter 1

Upload: independent

Post on 08-Jan-2023

0 views

Category:

Documents


0 download

TRANSCRIPT

CRUSHER INVESTIGATION REPORTReport No; 01

Contract; Kasane Airport Contract No; 60948

Location; Lesoma Quarry

Date of Investigation; From Tue 05/06/2012 to Sun 10/06/2012

Name of Investigators; Benard T Ruwona & Shawn A Potgieter

1

Problem statement

• The Crushers at Lesoma Quarry were producing coarse 26.5mm G2. There was need to produce more fines to meet tospecification of SATCC 3602/2.i.e.

Sieve Size % Passing

26.5 mm 100

19.0 mm 85-95

13.2 mm 71-84

4.75 mm 42-60

2.00 mm 27-45

0.425 mm 13-27

0.075 mm 5-12

Pan

2

Objectives of Investigation• Evaluate All stages of Crushing process i.e.

– Drilling and Blasting methods– Load and Haul from Pit to Crusher Feeder– Crushing & Type of Crushers used– Screening process

• Laboratory Grading Results• Conclusion of Findings

3

1. Drilling and Blasting

Figure 1; Drilling Hammer-DHD or DTH-Above shows DHD or DTH used with Drill rig and Air Compressor.

Activity Recommendations

Drilling done using; 89 mm Ø bit Ok

Burden & Spacing ; 2 m by 3 m Reduce to 2 m by 2 m to create more fines

Type of Explosives; ANFEX Ok

4

2. Load and Haul from Pit to Crusher Feeder

Figure 2; Sequence of Load, Haul and Crushing

Activity Recommendations

Loading Large rock and Small rock Mix the loading of Large and Small rock

Loading overburden material Do not load overburden to reduce PI in end product

Dust suppression at crusher feeder Ok

5

3. Crushing & Type of Crushers used

Figure 3; Primary Crusher

Parameters Before Current Manufacturer’s Recommendation

Max Feed size 500 mm 500 mm X<500 mm

Discharge size 170 mm 115 mm 65-160 mm

Gap size 150 mm 95 mm Min 65 mm

Reduction Ratio 1:3.3 1:5 1:7-1:3

Lining Condition Finished one side Used Good one side Keep under observation

3.1 Primary Crusher (Single Toggle Jaw Crusher)

6

Figure 4; Secondary Crusher

Parameters Before Current Manufacturer’s Recommendation

Max Feed size 170 mm 115 mm 300 mm

Discharge size 80 mm 52 mm 15-50 mm

Gap size 50 mm 32 mm Min 15 mm

Reduction Ratio 1:3.4 1:3.5 1:20-1:6

Lining Condition Finished one side Used Good one side Keep under observation

3.2 Secondary Crusher (Single Toggle Jaw Crusher)-2 no. side by side

7

Figure 4; Tertiary Crusher

3.3 Tertiary Crusher (Horizontal Shaft Impactor)-H.S.I

HSI Primary Crusher

HSI Secondary Crusher

8

Parameters Before Current Manufacturer’s Recommendation

Max Feed size 80 mm 52 mm 250 mm

Discharge size 60 mm 45 mm 10-60 mm

Gap size 50 mm 42 mm Min 40 mm

Reduction Ratio 1:1.6 1:1.2 1:25-1:4

Hammer Condition Finished one side Used Good one side Keep under observation

Parameters Before Current Manufacturer’s Recommendation

Max Feed size 60 mm 45 mm 60 mm

Discharge size 40 mm 26.5 mm 10-60 mm

Gap size 42 mm 20 mm Min 10 mm

Reduction Ratio 1:1.4 1:2.3 1:25-1:4

Hammer Condition Finished one side Used Good one side Keep under observation

3.3.a. H.S.I Primary Crusher

3.3.b. H.S.I Secondary Crusher

9

4. Screening Process

Before Recommendation

Inclined four Deck Screen used Ok

Motor running in direction of gradient Ok

Gradient of screens @ +-200 horizontal Ok

Before Recommendation

Gradient Gradient

4.2 Characteristics of Screening Deck

4.1 Layout of Screening Deck

Figure 5; Screen Layout by Aperture size

10

5. Laboratory Grading Results

Average Grading Before Average Grading After

0

20

40

60

80

100

120

0.075 0.425 2 4.75 13.2 19 26.5 37.5

% P

assi

ng

Particle size (mm)

Product; 26.5 mm G2

UpperG2Lower

0

20

40

60

80

100

120

0.075 0.425 2 4.75 13.2 19 26.5 37.5%

Pas

sing

Particle size (mm)

Product; 26.5 mm G2

UpperG2Lower

Sampling under conveyor beltOf +- 20 kg

Sampling under Conveyor beltOf +- 5 kg

11

Conclusion of Findings

• G2 Grading has improved i.e. quantity of fines produced increased by average of +-18%.

• G2 Grading can be further improved if the Quarry personnel cooperate better during investigation trials e.g. During regulation of gap sizes to maximise reduction ratios.

• Sample to be +-20 kg to obtain better representation of product.

• Stepped stock pilling should be implemented to reduce material segregation.

12