| Ball Mill Performance & Efficiency |
| S. |
Description |
Symbol |
Formula |
Example |
| No. |
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| 1 |
Arm of gravity |
a |
|
|
0.666 * ( 1 – 4 * R2 )1.5 |
|
h |
0.583 |
|
|
– |
|
|
TAN-1 [ 0.5 / R * (1 – 4*R2)0.5] – [ 2*R * (1 – 4*R2)0.5 ] |
|
Deff |
4.18 |
|
|
|
|
h |
Centre Distance (from mill centre to media top layer), mts |
|
R |
0.139 |
|
|
|
|
Deff |
Mill effective diameter, mts |
|
a |
0.578 |
|
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|
R |
h/Deff, ratio of centre distance to mill effective diameter |
|
Target |
– |
| 2 |
Torque factor matrix |
u |
|
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|
– |
– |
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– |
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– |
– |
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– |
– |
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– |
– |
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– |
– |
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– |
– |
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– |
– |
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– |
– |
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– |
– |
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– |
– |
| 2 |
Power consumption, net |
Pn |
|
|
0.514 * F * u * n * Deff * a |
|
F |
175 |
|
|
kW |
|
F |
Grinding media weight, tons |
|
u |
0.73 |
|
|
|
|
u |
Torque factor |
|
n |
16 |
|
|
|
|
n |
Mill speed, rpm |
|
Deff |
4.18 |
|
|
|
|
Deff |
Mill effective diameter, mts |
|
a |
0.578 |
|
|
|
|
a |
Arm of gravity, – |
|
Pn |
2538 |
|
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|
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|
Target |
– |
| 3 |
Power consumption, gross |
Pg |
|
|
Pn * 100 * 100 |
|
Pn |
2450 |
|
|
kW |
|
|
Em * Eg |
|
Em |
95 |
|
|
|
|
Em |
Motor efficiency, % |
|
Eg |
95 |
|
|
|
|
Eg |
Gearbox/girth gear efficiency, % |
|
Pg |
2715 |
|
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|
Target |
– |
| 4 |
New production rate |
NPB |
Formula-1 |
|
OPB |
118 |
|
(Mill output Vs. Blaine) |
tph |
|
|
OPB |
|
OB |
4000 |
|
|
|
|
|
Exp ( ( NB – OB ) * 0.49 / 1000 ) |
|
NB |
5000 |
|
|
|
|
OPB |
Old production rate, tph |
|
NPB |
72 |
|
|
|
|
OB |
Old blaine, cm2/gm |
|
Target |
– |
|
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|
NB |
New blaine, cm2/gm |
|
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Formula-2 |
|
OPB |
118 |
|
|
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|
|
OPB * ( OB / NB )1.3 |
|
OB |
4000 |
|
|
|
|
OPB |
Old production rate, tph |
|
NB |
5000 |
|
|
|
|
OB |
Old blaine, cm2/gm |
|
NPB |
88 |
|
|
|
|
NB |
New blaine, cm2/gm |
|
Target |
– |
| 5 |
New production rate |
NPR |
|
|
OPR * ( 2 – log ( OR ) ) |
|
OPR |
150 |
|
(Mill output Vs. Residue) |
tph |
|
|
( 2 – log ( NR ) ) |
|
OR |
11.5 |
|
|
|
|
OPR |
Old production rate, tph |
|
NR |
9.5 |
|
|
|
|
OR |
Old residue, % |
|
NPR |
138 |
|
|
|
|
NR |
New residue, % |
|
Target |
– |
| 6 |
Gypsum set point |
GSP |
|
|
21500 * ( Scem – Sclk ) |
|
Scem |
2.1 |
|
(at weigh feeder) |
tph |
|
|
Pu * ( 100 – Fgyp ) |
|
Pu |
90 |
|
|
|
|
Scem |
Target SO3 content in cement, % |
|
Sclk |
0.3 |
|
|
|
|
Pu |
Gypsum purity, % |
|
Fgyp |
4.8 |
|
|
|
|
Sclk |
SO3 content in clinker, % |
|
GSP |
4.52 |
|
|
|
|
Fgyp |
Free moisture in gypsum, % |
|
Target |
– |
| 7 |
Maximum ball size |
MBS |
|
|
36 * F0.5 * { ( SG * Wi ) / ( %C * Deff0.5 ) }0.333 |
|
F |
15 |
|
|
mm |
|
F |
Feed size (sieve size in mm which retains 20% material), mm |
SG |
3 |
|
|
|
|
SG |
Specific weight of feed material, gm/cm3 |
|
Wi |
15 |
|
|
|
|
Wi |
Bond’s work index, kWh/t |
|
%C |
75 |
|
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|
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%C |
Mill speed as %critical, % |
|
Deff |
5.1 |
|
|
|
|
Deff |
Mill effective diameter, mts |
|
MBS |
90 |
|
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|
Target |
– |
| 8 |
%Filling |
%F |
|
|
112.5 – ( 125 * h / Deff ) |
|
h |
2.5 |
|
|
% |
|
h |
Free height, mts |
|
Deff |
4.155 |
|
|
|
|
Deff |
Mill effective diameter, mts |
|
%F |
37.3 |
|
|
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|
Target |
– |
|
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| 9 |
Circulation factor |
C |
Formula-1 |
|
FF |
150 |
|
|
– |
|
|
F + G |
|
CR |
170 |
|
|
|
|
|
F |
|
C |
2.13 |
|
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|
F |
Fresh feed rate, tph |
|
Target |
2-3 |
|
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|
G |
Coarse return, tph |
|
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|
Formula-2 |
|
Rg |
54.92 |
|
|
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|
Rg – Rf |
|
Rf |
3.52 |
|
|
|
|
|
Rg – Rm |
|
Rm |
34.16 |
|
|
|
|
Rg |
Residue of coarse return, % |
|
C |
2.48 |
|
|
|
|
Rf |
Residue of fines, % |
|
Target |
2-3 |
|
|
|
|
Rm |
Residue of separator feed, % |
|
|
|
| 10 |
Circulation load |
CL |
|
|
( C – 1 ) * 100 |
|
C |
2.48 |
|
|
% |
|
C |
Circulation factor, – |
|
CL |
148 |
|
|
|
|
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|
Target |
– |
| 11 |
Separator efficiency |
SE |
Formula-1 |
|
Ro |
100 |
|
|
% |
|
|
[log(Ro/Rf) – C * log[{Ro+(C-1)*Rg} / {Rf+(C-1)*Rg}]]*100 |
|
Rf |
3.52 |
|
|
|
|
|
log(Ro/Rf) – C * log[{Ro+(C-1)*100} / {Rf+(C-1)*100}] |
|
C |
2.48 |
|
|
|
|
Ro |
Residue of fresh feed, % |
|
Rg |
54.92 |
|
|
|
|
Rf |
Residue of fines, % |
|
SE |
68.8 |
|
|
|
|
C |
Circulation factor, – |
|
Target |
70-80 |
|
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Rg |
Residue of coarse return, % |
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Formula-2 (Fines Efficiency) |
|
Rf |
3.52 |
|
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|
|
( 100 – Rf ) * 100 |
|
Rm |
34.16 |
|
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|
|
( 100 – Rm ) * C |
|
C |
2.48 |
|
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Rf |
Residue of fines, % |
|
SEf |
59.1 |
|
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|
Rm |
Residue of separator feed, % |
|
Target |
70-80 |
|
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C |
Circulation factor, – |
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Formula-3 (Coarse Efficiency) |
|
Rg |
54.92 |
|
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|
|
Rg * ( C – 1 ) * 100 |
|
C |
2.48 |
|
|
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|
|
C * Rm |
|
Rm |
34.16 |
|
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|
Rg |
Residue of coarse return, % |
|
SEc |
95.9 |
|
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|
C |
Circulation factor, – |
|
Target |
70-80 |
|
|
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|
Rm |
Residue of separator feed, % |
|
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| 12 |
Critical speed |
nc |
|
|
42.3 / Deff0.5 |
|
Deff |
4.15 |
|
|
rpm |
|
Deff |
Mill effective diameter, mts |
|
Pn |
20.8 |
|
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|
Target |
– |
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| 1 |
New production rate |
NPR |
Formula-1 |
|
OPB |
118 |
|
(Mill output Vs. Blaine) |
tph |
|
|
OPB |
|
OB |
4000 |
|
|
|
|
|
Exp ( ( NB – OB ) * 0.49 / 1000 ) |
|
NB |
5000 |
|
|
|
|
OPB |
Old production rate, tph |
|
NPR |
72 |
|
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|
OB |
Old blaine, cm2/gm |
|
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NB |
New blaine, cm2/gm |
|
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|
Formula-2 |
|
OPB |
118 |
|
|
|
|
|
OPB * ( OB / NB )1.3 |
|
OB |
4000 |
|
|
|
|
OPB |
Old production rate, tph |
|
NB |
5000 |
|
|
|
|
OB |
Old blaine, cm2/gm |
|
NPR |
88 |
|
|
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|
NB |
New blaine, cm2/gm |
|
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| 2 |
New Specific power cons. |
|
Formula |
|
|
|
|
|
(sp. power Vs. Blaine) |
NPR |
|
E1 |
E (S1 / S)n |
|
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|
kWh/TC |
|
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|
E1 |
New specific power |
|
E |
32.5 |
|
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E |
Old specific power |
|
S1 |
5000 |
|
|
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|
S1 |
New Blaine |
|
S |
4000 |
|
|
|
|
S |
Old Blaine |
|
n |
1.3 |
|
|
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|
n |
Mill exponent for close ckt = 1.3 |
|
E1 |
43.44 |
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| 1 |
New production rate |
NPR |
Formula |
|
OPB |
118 |
|
(Mill output Vs. Blaine) |
tph |
|
|
OPB * ( OB / NB )1.3 |
|
OB |
4000 |
|
|
|
|
OPB |
Old production rate, tph |
|
NB |
5000 |
|
|
|
|
OB |
Old blaine, cm2/gm |
|
NPR |
88 |
|
|
|
|
NB |
New blaine, cm2/gm |
|
|
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| 2 |
New Specific power cons. |
|
Formula |
|
|
|
|
(sp. power Vs. Blaine) |
NPR |
|
E1 |
E (S1 / S)n |
|
|
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|
|
kWh/TC |
|
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|
E1 |
New specific power |
|
E |
32.5 |
|
|
|
|
E |
Old specific power |
|
S1 |
5000 |
|
|
|
|
S1 |
New Blaine |
|
S |
4000 |
|
|
|
|
S |
Old Blaine |
|
n |
1.3 |
|
|
|
|
n |
Mill exponent for close ckt = 1.3 |
|
E1 |
43.44 |
|
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