by pass mass-balance

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  • 8/17/2019 By Pass Mass-Balance

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    Material balance for bypass

    Kcal/Kg cli 980

     

    Material L.O.I % element

    Kiln feed 34.74 SO3

    Kiln Dust 3.97 K!O

    "#$ass dust 7.4 &a!O'l!

    1-Input by Raw material

    (a) meal Kiln dust

    element )et l*ss free element )et

    SO3 0. 0.84 SO3 0.3

    K!O 0.3 0.4 K!O 0.!

    &a!O 0.34 0.! &a!O 0.34

    'l! 0.!0 0.3+ 'l! 0.7

    2-Input by Fuel oil

    t*tal sul$,ur - !.+8 SO3 - .4

    SO3 in feed fr* 0.!73

    1-Output by clinker 

    element %

    SO3 +.!

    K!O 0.3!

    &a!O 0.!8

    'l! 0.00

    2-Output by Bypass dust

    element % l*ss free

    SO3 3.37 3.4K!O !.3+ !.0

    &a!O 0.99 +.07

    'l! 3.94 4.!

    balance sheet

    input

    SO3 K!O &a!O 'l

    (a) Meal 0.84 0.4 0.! 0.3+

    uel *il 0.!73

    total input 112 !"# !"2 !$1

    output

    SO3 K!O &a!O 'l!

    'liner +.! 0.3! 0.!8 0.00

    Kiln Dust 0.+3 0.0 0.07 0.+!

    "#$ass dust 0.! 0.+7 0.07 0.!9

    total output 1%# !"# !#2 !#1

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    &O$ 'l2

    (olatility 0.49 +.00

    )nrichment !.!0 !.4+

    alali /sul$,ate 0.70!087

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    Hot meal

    %

    !.4

    0.74

    l*ss free

    +.00

    0.40

    0.4

    0.90

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    &ulphur *o +lkali

    Inputs

    S$. eat '*nsum$ti*n 800 Kcal/Kg cli

    '*al 1s, !3.3 %

    Net CV of coal as red +30 'al/Kg

    O2ide Raw meal)et LOI % loss free

    K!O 0.3 34. 0.0

    &a!O 0.039 34. 0.00

    SO3 0.+! 34. 0.+9+

    1s, c*ntriuti*n t* cliner 0.0304 g 1s,/g 'liner

    L*ss ree (a) Mi2 c*ntriuti*n t* 'liner 0.99 g 1s,/g 'liner

    Total K2O 0.007 g K!O/g 'liner

    Total Na2O 0.000 g &a!O/g 'liner

    Total SO3 0.00! g SO3/g Sul$,ur

    Total SO3 0.003 g SO3/g 'liner

     5*tal 1lali 1S &a!O 0.44 , in 'linker 

    Sul$,ur 5* 1lali rati* 0.3

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    Material L.O.I %

    Kiln feed 34.74

    Kiln Dust 3.97

    "#$ass dust 7.4

    1-Input by Raw material(a) meal

    element )et l*ss free

    SO3 0. 0.84

    K!O 0.3 0.4

    &a!O 0.34 0.!

    'l! 0.!0 0.3+

    2-Input by Fuel oil

    t*tal sul$,ur - !.+8

    SO3 in feed fr* 0.!73

    1-Output by clinker 

    element %

    SO3 +.!

    K!O 0.3!

    &a!O 0.!8

    'l! 0.00

    2-Output by Bypass dust

    element % l*ss free

    SO3 3.37 3.4

    K!O !.3+ !.0

    &a!O 0.99 +.07'l! 3.94 4.!

    balance sheet

    input

    SO3 K!O

    (a) Meal 0.84 0.4

    uel *il 0.!73

    total input 112 !"#

    output

    SO3 K!O

    'liner +.! 0.3!

    Kiln Dust 0.+3 0.0

    "#$ass dust 0.! 0.+7

    total output 1%# !"#

    &O$ 'l2

    (olatility 0.49 +.00

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    )nrichment !.!0 !.4+

    alali /sul$,ate 0.70!087

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    atio

    'oal%

    +.3! In +sh

    0.08 In +sh

    0.! +s elemental &

    3.04 , in 'linker 

    9.9 , in 'linker 

    0.!" , in 'linker 

    0.0 , in 'linker 

    0.3! , in 'linker 

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    Hot meal

    element %

    SO3 !.4

    K!O

    &a!O

    'l! 0.74

    Kiln dust

    element )et l*ss free

    SO3 0.3 +.00

    K!O 0.! 0.40

    &a!O 0.34 0.4

    'l! 0.7 0.90

    SO3 - .4

    &a!O 'l

    0.! 0.3+

    !"2 !$1

    &a!O 'l!

    0.!8 0.00

    0.07 0.+!

    0.07 0.!9

    !#2 !#1

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