Rotary Kiln Operation .Kiln Feed vs Kiln speed calculation
data
Description : Kiln
FEEDFull description
Descripción: AXERA
clinker
A course includes clinker cooler function and types from elder to the most recent technology.
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Difference between FEED and Detail Engineering
Description : calculations for kiln operation
Kiln MiscellaneousFull description
Difference between FEED and Detail Engineering
Kiln Drying
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mechanics
Kiln Training
Cement Kiln Shell
Descripción completa
KILN FEED TO CLINKER
P H Dust loss L O I Of Kiln feed Coal Ash Content SHC Kiln Coal Kiln Coal NCV PC Coal PC Coal NCV weighted Average N CV of Coal Kiln feed Basis Clinker produced from above kiln feed KILN FEED TO CLINKER CONVERSION FACTOR Raw meal TO Clinker Conversion Factor
% % % Kcal / Kg Clinker MT Kcal / Kg Coal MT Kcal / Kg Coal Kcal / Kg Coal MT MT
Normal Density to Actual density : mmWg Po 10336 mmWg Do 1.293 Kg/Nm3 To 273 Deg.K Actual Density to Normal density : mmWg Po 10336 mmWg Do,Kg/NM3 1.34873297 To 273 K
Actual Vol. to Normal Volume : mmWg Pb 10311.51 Po 10336 mmWg Stat.Press -28 Vo,NMtr3/Hr. 26087.9781 V1, Mtr3/Hr.29294.69 To 273 K T1, Deg.C 32 Clinker prodn. NMtr3/Kg.Cl.
7600 TPD 0.08238309
Day Avg. Clinker Day 1 % LOI ---% SiO2 22.4 % Al2O3 5.58 % TiO2 Not reported 0 % Fe2O3 3.1 % Mn2O3 Not reported 0 % CaO 66.94 % MgO 1.32 % SO3 (total sulfur) 0.5 % P2O5 Not reported 0 % Na2O 0.114 % K2O 0.37 % Cl 0.0063 % Cr2O3 Not reported 0 Total 100 % Na2O equivalent 0.36 Silica ratio 2.58 Alumina ratio 1.80 Lime standard (KUEHL) 94.24 SiO2 / (Al2O3 + TiO2) 4.01 Clinker phases (Bogue) % C3S 60.4 % C2S 18.69 % C3A 9.54 % C4AF 9.43 % Liquid phase 25.09 (acc. to LEA. 1400° C ) HEAT OF REACTION 427 Average Kcal / kg Cl.
