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RAW MIX DESIGN OF TWO COMPONENTS o m p o ne n t s
Clinker
Raw Mix
M1
M2
Fuel Ash
SiO2
%
0. 00
0. 00
1 .65
54.87
5 8.00
Al2O3
%
0. 00
3. 20
0 .80
25.35
2 5.54
Fe2O3
%
0. 00
2. 50
0 .80
8.00
8.1 3
CaO
%
0. 00
46.0 0
53 .20
1.14
2.0 0
M gO
%
0. 00
0. 00
1 .10
2.40
1.0 0
Mn2O3
%
0. 00
0. 00
0 .00
0.00
0.0 0
TiO2
%
0. 00
0. 00
0 .00
0.00
0.0 0
P2O5
%
0. 00
0. 00
0 .00
0.00
0.0 0
K2O
%
0. 00
0. 00
0 .00
0.00
0.0 0
Na2O
%
0. 00
0. 00
0 .00
0.00
0.0 0
SrO
%
0. 00
0. 00
0 .00
0.00
0.0 0
SO3
%
0. 00
0. 00
0 .00
0.00
0.0 0
LOI
%
0. 00
0. 00
36 .50
3.00
0.0 0
Balance
%
100. 00
#VALU E!
5 .95
5.24
5.3 2
Total
%
100. 00
100.0 0
100 .00
100.00
10 0.00
0 .00
0.00
2.0 0
Raw Mi Mix ( % Raw Mi Mix ( % Cl
%
H2O
%
0.0 00
#VALU E!
#DI V/0!
# DIV/0 !
0. 003
0.003
0 .00
0.00
0 .014
LSF
#DIV /0!
1 111.0 0
855 .31
0.57
0.9 6
SM
#DIV /0!
0. 00
1 .03
1.65
1.7 2
AM
#DIV /0!
1. 28
1 .00
3.17
3.1 4
HM
#DIV /0!
8. 07
16 .37
0.01
0.0 2
SAM
#DIV /0!
0. 00
2 .06
2.16
2.2 7
K2O eq.
0. 00
0. 00
0 .00
0.00
0.0 0
Na2O eq.
0. 00
0. 00
0 .00
0.00
0.0 0
C3S
-6. 11
162.1 9
C2S
4. 61
- 122.3 6
C3A
0. 00
4.25
M1
:
Limes tone
C4AF
0. 00
7.61
M2
:
Phyli te
Free Free CaO CaO-- %
1.50
Fuel : Coal
Bur. Index
#DIV /0!
13.6 8
Bur. Factor
#DIV /0!
1 111.0 0
Bur. Bur. Temp Temp C
#######
Liq.Ph. 14 % SO3/AlK E.S.
Raw Materials
0.00
Coal Ash
:
16 .00
%
Coal Feed Rate
:
12 .50
%
Ash Absorption
:
10 0.00
%
#DIV/0! Sieve Analysis & Residue 0. 00
FCaO-S/C %
#DIV/0!
SiO2( +45m )
:
0.00
A4 5 (A .I.R. ) :
0.00
FCaO-A/T %
#DIV/0!
CaCO3(+125m) :
0.00
T125 (T.R.)
0.00
o ns t i t u e n t
M o de
SO3 Balan
Input
0. 00
0 .00
(Kg-SO3/Kg-Cl)
Output
0. 00
Alkali Balance
Input
0. 00
Raw Mix
Fuel
Dust
:
Clinker
Exit Gas
Total
0.00
0. 00
0 .00
0.0 0
0 .00
0.00
0. 00
0 .00
0.0 0
0 .00
0.00
0. 00
0 .00
0.0 0
(Kg-Alkali/Kg-Cl)
Output
0.00
0.00
0.00
Assumptions & Comments a) Kiln Feed Rate
1.57
Kg/Kg-Cl
b) Dust Returned to Kiln
8.00
%
c) Limestone sample (HG/LG) d) Coal sample taken from Korba Mines, Bilaspur (M.P.) e) Laterite sample taken from Gadchandur Mines (M.S.)
