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Raw Mix Design Software
Descripción: RAW MIX DESIGN SOFTWARE : Cement Plant...
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REQUIRED DATA FOR RAWMIX DESIGN SiO2
Al2O3
Fe2O3
CaO
MgO
Na2O
K2O
Cl
LOI
Other Traces
Lime Stone - 1
11.92
2.32
1.12
43.42
2.32
0.09
0.2
0.004
37.95
0.66
Lime Stone - 2
11
2.1
1.3
45
2.5
0.09
0.02
0.005
37.12
0.86
Lime Stone - 3
25
7.57
4.56
30.5
2.4
0.26
0.24
0.005
28.53
0.94
Laterite
11.54
33.64
41.05
0.11
0.09
0.02
0.22
0.004
10.33
3.00
Iron Ore
10.1
7.82
78.65
0.11
0.07
0.01
0.07
0.004
0.17
3.00
Bauxite
9.5
60
10.5
2.5
0.8
0.5
0.75
0.004
12.5
2.95
SiO2
Al2O3
Fe2O3
CaO
MgO
Na2O
K2O
Cl
Distribution ( In % )
ASH
IM
55.14
25.12
6.05
1.41
0.5
0.11
0.11
1.6
100
30
1.5
0
9
0.6
Fuel Used : -
i. Coal ii. Pet - Coke
LOI OF KILN FEED
35.6
%
FREE LIME IN CLINKER
2.0
%
Sp. Heat Consumption of Plant
692
Kcal. / kg-Clk.
`
RAW MIX DESIGN Target Value of LSF in RawMeal Contr. in %
SiO2
Lime Stone - 1
0.92
11.920
2.320
Lime Stone - 2
0.02
11.000
Lime Stone - 3
0.04
Laterite
Other Traces
TOTAL
LSF
SM
AM
61.39
37.95
0.66
100.00
117.71
3.47
2.07
0.005
62.02
37.12
0.86
100.00
131.71
3.24
1.62
0.240
0.005
70.54
28.53
0.94
100.00
37.17
2.06
1.66
0.020
0.220
0.004
86.67
10.33
3.00
100.00
0.11
0.15
0.82
0.070
0.010
0.070
0.004
96.83
8.00
1.60
106.43
0.12
0.12
0.10
2.500
0.800
0.500
0.750
0.004
84.55
12.50
2.95
100.00
2.37
0.13
5.71
42.36
2.30
0.10
0.20
0.00
62.12
37.18
0.70
100.00
107.00
2.66
1.66
MgO
1.120
43.420
2.320
0.090
0.200
0.004
2.100
1.300
45.000
2.500
0.090
0.020
25.000
7.570
4.560
30.500
2.400
0.260
0.01
11.540
33.640
41.050
0.110
0.090
Iron Ore
0.00
10.100
7.820
78.650
0.110
Bauxite
0.00
9.500
60.000
10.500
1.00
12.47
2.93
1.76
RAW MIX
SUB LOI
CaO
Na2O
Variables
Al2O3 Fe2O3
107
K2O
Cl
TOTAL
Kiln Feed Composition Details :
Fuel Ash Absorption :
SiO2
=
12.47
Al2O3
=
2.93
Fe2O3
= = = =
1.76 42.36 2.30 0.10
= =
0.20 0.00
CaO MgO Na2O K2O Cl LOI
Fuel Analysis : % %
i.Ash ii.I.M. iii.Net Calorific Value
Kcal./Kg-Coal
%
iv. Distrubution of Fuel v.Sp. Heat Cons.of Plant
Kcal./Kg-Clk.
% %
vi.Fuel Consumption vii.Ash Absorption
35.6 35.79 0.70 1.66 2.66 107.00
ii. C
= =
Others AM SM LSF
= = = =
=
20.92
FCaO
=
= = = =
5.43 2.88 63.11 3.45
LSF SM AM C3S
= = = =
0.91 2.52 1.89 49.13 OK
= =
0.15 0.30
C2S C3A
= =
=
0.07
C4AF SO3
=
i. Mea
Coal
Pet-Coke
= = = =
30.0 1.50 4864 100
9.0 0.60 7361 0
= = =
692 14.2 4.3
692 9.4 0.8
Na2O
K2O
0.11
0.11
Cl 1.6
Units
Chemical Analysis Report ( FUEL ASH ) :SiO2
Al2O3
Fe2O3
55.14
25.12
6.05
CaO 1.41
MgO 0.5
i.1338°C ii.1338°C iii.1450°C M SO3
= = = =
22.94 OK 9.52 OK
Liquid % Liquid %
= =
25.46 26.48
8.76
Burning Zone Temp.
=
1375.28
CLINKERIZATION : SiO2 Al2O3 Fe2O3 CaO MgO Na2O K2O Cl
Requirments :
=
2.0
Liquid Phase :
OK
21.0212 A.M. > 1.38 A.M. < 1.38 0 26.6728 A.M. > 0.64 -
Avg. Fuel
30.0 1.50 4864 100 692 14.2 4.3
RAWMIX - DESIGN REPORT 1.0 LIME SATURATION FACTOR in RAWMEAL
=
107.00
2.0 ALLUMINA RATIO in RAWMEAL
=
1.66
3.0 SILICA RATIO in RAWMEAL
=
2.66
i. Lime Stone - 1
=
0.92
ii. Lime Stone - 2
=
0.02
iii. Lime Stone - 3
=
0.00
iv. Laterite
=
0.01
v. Iron Ore
=
0.00
vi. Bauxite
=
0.00
=
4.27
a. CaO
=
63.11
b. LSF
=
0.91
c. SM
=
2.52
d. AM
=
1.89
e. C3S
=
49.13
f. C2S
=
22.94
g. C3A
=
9.52
h. C4AF
=
8.76
h. Liquid Phase (1338 C )
=
25.46
4.0 Fraction of Raw Materials :-
5.0 Coal ASH Absorption 6.0 COMPOSITION OF CLINKER : -
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