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    BEFORE OPTIMIZATION (AFTER MAY2009 BRICK LINING WORK)

    Cooler heat balance Date- 12-7-2008

    Ref.Temp.(deg.C) Flow Flow Cp Temp. H35 kg/kg-cl, kg/kg-cl kcal/kg OC OC kcal

    Nm3/kg-cl

    Heat in

    Clinker 1 1 0.26 1350 34

    Cooling air 2.37 3.06 0.24 35 0

    Total 3

    Heat out

    Cooler vent 1.50 1.93 0.24 336 14

    Discharged clinker 1 1 0.19 106 1

    Radiation loss 2

    Total 1

    NOTE:

    Cooler efficiency on

    heat loss basis=

    = 54 %

    SAVING OF THERMAL ENERGY BY COOLE

    = 27.3

    Energy cost Rs/m kcal 6

    Clinker production Tonne p.a. 90

    Heat saving k cal/kg.clk 2

    saving p.a.cooler heat Rs.p.a. 160

    Cr.p.a. 1.

    =

    UNDER GRATE PRESSURE IS BETWEEN 450 TO 470 MM WG.

    ((heat in by clinker + cooling air) -(heat loss by vent air+ clinker + radi

    SAVING OF HEAT BY PREHEATER EXHAU

    THERMAL ENERGY COST SAVING BY INC

    EFFICIENCY

    THERMAL ENERGY COST SAVING BY RE

    TEMP.

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    Clinker production Tonne p.a. 90

    Heat saving k cal/kg.clk 1

    saving p.a.PH exhaust heat Rs.p.a. 585

    Cr.p.a. 0.

    ELECTRICAL ENERGY SAVING=

    ELECTRICAL ENERGY COST=

    CLINKER PRODUCTION = 9

    POWER COST SAVING =

    TOTAL SAVING BY THERMAL AND ELECT

    =

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    AFTER OPTIMIZATION (AFTER NOVEEMBER 2009 BRICK LINING

    Cooler heat balance Date- 19-12-2008

    eat % Ref.Temp.(deg.C) Flow Flow Cp Temp.l/kg-cl 35 kg/kg-cl, kg/kg-cl kcal/kg OC OC k

    Nm3/kg-cl

    Heat in

    3.08 100 Clinker 1 1 0.26 1350

    .00 0 Cooling air 2.1 2.72 0.24 35

    43 100 Total

    Heat out

    2.49 90 Cooler vent 1.28 1.65 0.24 325 1

    .61 9 Discharged clinker 1 1 0.19 96

    .44 2 Radiation loss

    59 100 Total

    NOTE:

    Cooler efficiency on

    heat loss basis=

    = 62 %

    R OPTIMIZATION

    8 K Cal/kg clinker

    50

    0000

    .38

    14510

    601

    10 K Cal/kg clinker

    tion))/( total heat in)

    UNDER GRATE PRESSURE IS BETWEEN 570 TO 5

    ((heat in by clinker + cooling air) -(heat loss by v

    radiation))/( total heat in)

    ST GAS TEMP. REDUCTION

    EASING COOLER

    UCING PH. EXHAUST GAS

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    0000

    .00

    0000

    585

    1.3 Unit/tonne clk

    3.2 Rs/unit

    00000 Tonne p.a.

    .3744 Cr.p.a.

    ICAL ENERGY

    .6 Cr.p.a.

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    ORK)

    Heat %al/kg-cl

    43.08 100

    0.00 0

    343 100

    117.06 89

    11.66 9

    2.44 2

    131 100

    90 MM WG.

    ent air+ clinker +

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