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Pile Design With 5 Components

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- - - - - - - - - RAWMIX DESIGN - - - - - - -

LIMESTONE CLAY LATARITE BAUXITE


ANALYSIS ANALYSIS ANALYSIS ANALYSIS

% 87.13 10.00 0.23 1.40


SiO2 9.08 45.34 28.82 28.82
Al2O3 2.25 12.10 5.09 27.65
`
Fe2O3 1.64 1.22 40.09 13.02
CaO 46.48 2.96 6.96 2.43
MgO 1.36 1.62 0.67 0.78
K2O 0.40 0.30 0.98 0.07
Na2O 0.04 0.20 0.05 0.06
SO3 0.06 0.04 0.05 0.05
L.O.I. 38.14 36.00 17.23 27.03
TOTAL 99.45 99.78 99.94 99.91
S.R.
A.R.
L.S.F.

% Coal ash absorbed in Clinker


SiO2 Al2O3 Fe2O3
clinker 23.76 8.85 3.47
raw mix 19.87 5.72 3.23
Ash 52 28.93 4.96

X1 X2 X3 X4
-21.51562914 3.5078846154 2.9322813688 -0.411209677
% COAL ASH ABSORBED IN CLINKER
IX DESIGN - - - - - - - - -
HSLS RAWMEAL ESP DUST KILN FEED
ANALYSIS 100.00 AS IT IS BASIS ANALYSIS DESIGNED

1.24 100.00 8.00 100.00


30.99 13.30 10.96 14.18
2.91 3.61 3.99 3.92
2.00 1.85 3.24 2.11
27.28 41.18 42.70 44.60
0.82 1.37 1.68 1.50
0.90 0.39 0.49 0.43
0.08 0.06 0.20 0.07
0.02 0.06 0.21 0.07
34.00 37.00 37.00 35.50
99.00 98.81 100.46 102.39
2.44 1.52 2.35
1.95 1.23 1.86
96.46 97.60

er 65.8
CaO
65.54 21.3 2.982
65.4 14
3.02
supposetotal coal ton
consumption=
% of Moisture in fine 0.14
coal is=
Total Ash in coal= ton
Total ash absorbed in tons
clinker=
-15.1782656
COAL ASH CLINKER
ANALYSIS DESIGNED

2.98 100.00
**
52.00 SiO2 22.87 C3S 2.25
28.93 Al2O3 6.77 C2S 1.64
4.96 `
Fe2O3 3.32 `
C3A 46.48
3.02 CaO 67.17 C4AF 1.36
0.72 MgO 2.28 H.M 0.40
0.32 K2O 0.66 C.Index 0.04
0.69 Na2O 0.13 LQ.phase 0.06
3.43 SO3 0.21 B.Z Temp. 38.14
- S.R. 2.27 B.Factor 16.08
94.07 A.R. 2.04 B.Index 17.09
1.53 L.S.F. 90.54 MSO3 18.10
5.83 Cl Q.H 19.10
MSO3 20.11

1.27519379844961
1.38697674418605
BYPASS DUST CLINKER
ANALYSIS With Losses

2.00
16.59 23.21
5.42 6.87
3.81 3.40
63.38 68.44
3.04 2.34
0.10 0.66
1.57 0.16
2.43 0.26
3.00 0.50
99.34 105.85
1.80 2.26
1.42 2.02
114.56 90.90

5160
- - - - - - - - - RAWMIX DESIGN - - - - - - -
LIMESTONE CLAY LATARITE BAUXITE
ANALYSIS ANALYSIS ANALYSIS ANALYSIS

% 88.00 9.13 0.23 1.40


SiO2 9.08 45.34 28.82 28.82
Al2O3 2.25 12.10 5.09 27.65
`
Fe2O3 1.64 1.22 40.09 13.02
CaO 46.48 2.96 6.96 2.43
MgO 1.36 1.62 0.67 0.78
K2O 0.40 0.30 0.98 0.07
Na2O 0.04 0.20 0.05 0.06
SO3 0.06 0.04 0.05 0.05
L.O.I. 38.14 36.00 17.23 27.03
TOTAL 99.45 99.78 99.94 99.91
S.R.
A.R.
L.S.F.

% Coal ash absorbed in Clinker


SiO2 Al2O3 Fe2O3
clinker 23.76 8.85 3.47
raw mix 19.87 5.72 3.23
Ash 52 28.93 4.96

X1 X2 X3 X4
-21.51562914 3.5078846154 2.9322813688 -0.411209677
% COAL ASH ABSORBED IN CLINKER
IX DESIGN - - - - - - - - -
HSLS RAWMEAL ESP DUST KILN FEED
ANALYSIS 100.00 AS IT IS BASIS ANALYSIS DESIGNED

1.24 100.00 8.00 100.00


30.99 12.98 10.96 13.86
2.91 3.52 3.99 3.84
2.00 1.85 3.24 2.11
27.28 41.56 42.70 44.98
0.82 1.37 1.68 1.50
0.90 0.39 0.49 0.43
0.08 0.06 0.20 0.07
0.02 0.06 0.21 0.07
34.00 37.00 37.00 36.00
99.00 98.79 100.46 102.87
2.42 1.52 2.33
1.90 1.23 1.82
99.63 100.59

er 65.8
CaO
65.54 21.3 2.982
65.4 14
3.02
supposetotal coal ton
consumption=
% of Moisture in fine 0.14
coal is=
Total Ash in coal= ton
Total ash absorbed in tons
clinker=
-15.1782656
COAL ASH CLINKER
ANALYSIS DESIGNED

2.98 100.00
**
52.00 SiO2 22.56 C3S 2.25
28.93 Al2O3 6.68 C2S 1.64
4.96 `
Fe2O3 3.35 `
C3A 46.48
3.02 CaO 68.27 C4AF 1.36
0.72 MgO 2.30 H.M 0.40
0.32 K2O 0.67 C.Index 0.04
0.69 Na2O 0.13 LQ.phase 0.06
3.43 SO3 0.21 B.Z Temp. 38.14
- S.R. 2.25 B.Factor 16.08
94.07 A.R. 1.99 B.Index 17.09
1.53 L.S.F. 93.22 MSO3 18.10
5.83 Cl Q.H 19.10
MSO3 20.11

1.27519379844961
1.38697674418605
BYPASS DUST CLINKER
ANALYSIS With Losses

2.00
16.59 22.89
5.42 6.79
3.81 3.43
63.38 69.54
3.04 2.36
0.10 0.67
1.57 0.16
2.43 0.26
3.00 0.50
99.34 106.60
1.80 2.24
1.42 1.98
114.56 93.54

5160

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