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Ball Mill Operation & Ball Mills Audits
Name : Shailesh Katare UE No : 1000814 Date : 13.10.2017 Time : 02.30 pm to 05.30 pm Venue : Kiln CCR Conference hall
Content • “A” level cement mill audit
What is an “A” Level Audit? Targets of the “A” level audit
• “B” level cement mill audit
What is a “B” Level Audit? Targets of a “B” Level Audit Requirements for the “B” level audit “B” level audit realization “B” level audit for VRM (vertical roller mill)
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What is a « A » level Audit?
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Long and short term data analysis • Production
• Evaluation and Potential estimation based on:
• Operation
• Quality
KPI
Comparison with other grinding systems Theoretical calculations
12 months 1 month 1 day
time 4 CMS – MPT – Grinding Technology
What is a “B” Level Audit? KPI
Standard measurements
time 5 CMS – MPT – Grinding Technology
Systematic Approach
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Standard Measurements – Tasks & Frequency one year 1. Circuit mat. granulometry
2. Mill longitudinal sieving 3. Ball charge filling degree 4. Mill material level 5. Mill ventilation 6. Separator Tromp curve
B-level audit
7. Separator ventilation 8. Mill internal conditions
9. Weigh feeder calibration 10. Instrument verification 11. Control loop verification
yearly stop
7
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Targets of a “B” Level Audit
kWh/t
t/h
- 5 - 15 %
%R45 um T [°C]
R 28
cm2/g
R2
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Logical realisation order 1. Define the cement type(s) for the audit 2. Gather the main machines design data
3. Central Control Room visit 4. Circuit visual inspection 5. Field activities:
= standard measurements done simultaneously
Counters reading Sampling Measuring Mill, separator and auxiliaries internal visual inspection
6. Data compilation and analysis
7. Conclusions and report 9 CMS – MPT – Grinding Technology
Main machines design data t, t/h, kW, kJ/h, ºC, m3/h, mbar, m/s, m, m2, min-1,
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Mill Control System, Strategy and Trends • Information on:
Available information at the CCR First contact with circuit layout Control system Control strategy First impression on operation Circuit stability
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Circuit / Visual inspection during operation
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Material and liquids sampling and measurements
A
temperature
Grinding aid
SF
CF
MF F
R
K
G
L
S
Water injection
C
SSR
MO 13 CMS – MPT – Grinding Technology
Material sample analysis A
Clinker
10 [kg]
1x per test 50, 25, 16, 8, 4, 2, 1, [mm], temperature
B
Gypsum
10 [kg]
1x per test 50, 25, 16, 8, 4, 2, 1, [mm] + %H2O
C
Limestone
10 [kg]
1x per test 50, 25, 16, 8, 4, 2, 1, [mm] + %H2O
S
Slag
10 [kg]
1 x per test 50, 25, 16, 8, 4, 2, 1, [mm] + %H2O
MO
Mill outlet
0.5 [kg]
200 [µm] Alpine Sieb pre-screening 1 x per 1/2 - ~1- 200 [µm] Laser 1.0 h (6x) Blaine [cm2/g] temperature (at least MO & R)
SSR Static. Sep. return A
Separator feed
CF
Sep. cyclones fines
SF
Sep. filter dust
F
Separator fines
R
Separator returns
MF
Mill filter dust
C
Cement 14 CMS – MPT – Grinding Technology
Power measurement Separator filter fan
Separator fan
Separator rotor
Mill fan Elevator
2 main groups:
Mill motor Auxiliaries
Fuel
Mill motor
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Mill air measurements Static pressure, temperature Airflow, static pressure & temperature
MFC MFO
MFI MO HGSA HGFA MI HGPA
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Mill material sampling = longitudinal sieving 1.1
1.2
20 cm 0.5 1m
1m
Mill cross section 1m
0.5
0.5 1m
1m
1m
1m
0.5
1.1
2.1
2.2
2.3
2.4
2.5
20 cm 17 CMS – MPT – Grinding Technology
Mill material samples analysis % residue accumulated
Sieve [mm]
Sample 1. Chamber
16
8
Blaine 4
2
1
0.5
0.2
0.12
0.09 0.063 0.045 cm2/g
1.1 1.2 1.3 1.4
2. Chamber
2.1 2.2 2.3 2.4 2.5 2.6 2.7 18 CMS – MPT – Grinding Technology
Mill internals: inspection and measurement Ball filling degree
Slot width, gaps, plugging, thickness
Ball filling degree
Slot width, flow setting
Slot width, gaps, plugging, thickness
State & thickness
State, position Liner residual lifting height
Liner type, state & rotation sense
Extreme ball size, state
Extreme ball size, classification, state
Material level & coating
Liner type, state & main dimensions
Material level & coating 19 CMS – MPT – Grinding Technology
Ball charge filling degree 1. Measure average internal diameter Di 2. Measure height h, in three different points along axis 3. Calculate h/Di and determine filling degree from diagram h Di
h/Di
D i
0,75
Di =
0,70
Mill diameter inside mill liners
0,65
0,60
filling degr
20
25
30
35
f [%]
20
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4. Material level 4.1 - 1st Compartment
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4. Material level 4.2 - 2
nd
Compartment
>> 50 [mm] bad ~ 50 [mm] good < 50 [mm] bad
<< 50 [mm] very bad
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Mill internal visual inspection
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8. Mill visual inspection
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Mill / Balls sampling
At least 4 samples Sampled balls -Sample weight kg Eq. Diameter mm Broken balls -Deformed balls -Broken balls % Deformed balls %
50 22.3 48 2 3 4 6
100 21.5 37 3 6 3 6
150 12.9 28 8 12 5 8
200 9.5 23 15 22 8 11
200 4.3 17 10 3 5 2 25
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Ball charge managementWear rate calculation on principle
Scraps S = 1t
Wear compensation WC = 24 t
Small balls SB = 3 t
Good balls GB = 79 t
Initial charge IC = 80 t 26 CMS – MPT – Grinding Technology
Net and gross wear rate
IC + WC – GB x 1’000’000
Gross wear =
[ gball / tcement ]
CP
IC + WC – (GB + SB + S) Net wear =
x 1’000’000
[gball / tcement ]
CP
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Separator / Visual inspection / 1st Generation
3
4
1
2
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Separator / Visual inspection / 2nd Generation
1
2
4
3
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Separator / Visual inspection / 3rd Generation
1
2 6 3 5
4
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Fans / Visual inspection
2
1
3
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Performance test data sheet Ball Mill Performance (Cement) Plant: Mill Nr.: Production
Date: Visa:
Cement mill 3 Mill production Cement type Fineness Feed moisture
Cement Composition
Material type Clinker Gypsum Limesone .... Total
Energy Consumption
Mill motors Separator rotor Separator fan Sepol Separator fan Stat. Press motor 1 Press motor 2 Mill fan Bucket elevators Auxiliaries Total mill system
Separator
Circulating factor Separator load - product / air ratio - feed / air ratio By-Pass Cut point Air flow rate Separator fan flap
202.3 [t/h] Type I-II 3660 [cm²/g] Blaine 1.8 [%] R 45 [µm] 0.240 [%] wet base
24.01.2003
Mill dimensions Diameter Length Motor
5.0 [m] 15.8 [m] 6000 [kW]inst.
Composit.[%] Product Moisture [%] H2O (wet base) 94.7 [%] [%] 4.3 [%] 5 [%] 1 [%] 2.5 [%] [%] [%] 100 [%] Feed moisture average 0.240 [%] 5'358 222 575 584 802 810 98 229 671 9'349
[kW]abs. [kW] [kW] [kW] [kW] [kW] [kW] [kW] [kW] [kW]
2.5 [ - ] calc 0.57 1.44 7 17.5 352000 100
[kg/m³] [kg/m³] [%] [µm] [m³/h] [%]
26.5 [kWh/t]
counter
[kWh/t] [kWh/t] [kWh/t] [kWh/t] [kWh/t] [kWh/t] [kWh/t] [kWh/t] 46.2 [kWh/t] 1.1 2.8 2.9 4.0 4.0 0.5 1.1 3.3
System Rotor
diameter height area speed Radial air speed Circumf. speed rotor
3.50 2.33 25.6 133.2 3.8 24.4
[m] [m] [m²] [min-1] [m/s] [m/s]
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Conclusion • Standard measurements give valuable information
on grinding system performance on grinding system weak points
• B-level audit is the base-line of all medium-long term actions in process optimization • Detailed and accurate interpretation of the results are the key success factors of a B-level audit • Regular B-Level audits show a historic trend of the development of a grinding system and avoid a slow, but steady slow drift in the wrong direction
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