Assessment of Production Kernel (PK) Stone

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    Assessment of Production

    Kernel Stone Contamination

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    Introduction

    High stone contamination resulted in PK deduction of 30MT &25MT on Sept

    & Oct 2011 respectively.

    Possible faulty of machineries were checked (damper, cyclone & airlock).

    Silo Kernel quality was given hourly attention

    Dampers were adjusted correspond to lab sample quality.

    However, after silo kernel stone % still fluctuated between 0.18% - 5.04%. Due to the inconsistency of PK stone %, this survey is carried out.

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    November 17th

    The source of Small Stone was investigated.

    Press Cake

    Nut

    Before Silo

    Before Silo

    6.35 gram

    0.62% to

    P.Cake

    Press #4

    17/11/2011

    Press Cake

    61.05 gram

    5.41% to P.CakePress #4

    17/11/2011

    6.69 gram

    0.60% to P.D. Nut

    P. Drum

    17/11/2011

    Polishing Drum Nut

    Polishing Drum Nut

    28.18 gram

    2.43% to P.D.

    Nut

    P. Drum

    17/11/2011

    12.64 gram

    1.16%

    Before Silo

    17/11/2011

    8.72 gram

    0.73%Before Silo

    17/11/2011

    Press cake stone Avg. 2.73%, before silo stone high 1.16% &

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    November 18thPress Cake

    Press Cake

    Press Cake

    Polishing Drum Nut

    Polishing Drum Nut

    Polishing Drum Nut

    Before Silo

    Before Silo

    Before Silo

    2.85 gram

    0.25% to P.Cake

    Press #4

    18/11/2011

    4.03 gram

    0.37% to P.Cake

    Press #6

    18/11/2011

    19.47 gram

    1.62% to P.Cake

    Press #5

    18/11/2011

    69.66 gram

    6.40% to P.D. Nut

    P. Drum

    18/11/2011

    6.64 gram

    0.60% to P.D. Nut

    P. Drum

    18/11/2011

    5.74 gram

    0.51% to P.D. Nut

    P. Drum

    18/11/2011

    5.01 gram

    0.45%

    Before Silo

    18/11/2011

    17.53 gram

    1.61%

    Before Silo

    18/11/2011

    11.02 gram

    1.00%

    Before Silo

    18/11/2011

    Press cake stone Avg. 0.75%, before silo stone high 1.61% &

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    smaller stones were carry forward from press cake to nut bin and finally to

    kernel silo.

    Press PolishingDrum

    Destoner LTDS #1 Before Silo

    Filtered stonesfrom press cake

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    November 17thNovember 18th Cont.

    Stones in PK were similar in size and weight if not larger comparing to

    kernel. (Refer to Figure 1) This resulted in difficulty of air separation.

    LTDS Kernel (Dry) & Hydro cyclone Kernel (Wet) were studied for stone %

    and found that 100% stone contamination was contributed by LTDS kernel

    (Dry).

    Wet shell was sampled and found that the stone size in wet shell was

    relatively small. (Refer to Figure 2) Reconfirmed hydro cyclone separation efficiency.

    Kernel Stone

    1.12 gram 1.72 gram

    Figure 1

    Wet Shell Mini Stones

    Figure 2

    0.03 0.14 gram

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    November 20thNovember 25th

    Production kernel with low stone % is stored in bunker #2 and blended with

    bunker #1 for despatch.

    Since air separation is not reliable to tackle our present problem, mill did a

    trial to feed in more chipped mixtures to hydro cyclone for water separation

    by adjusting LTDS #2 damper.

    Ripple mill throughput was fixed for control convenience.

    LTDS #1 damper reduced, LTDS #2 damper was opened more.

    LTDS losses was monitored during the trial.

    Average LTDS losses significantly higher than target, during the trial mill had

    to sacrifice broken kernels to improve stone contamination.

    Date

    Kernel Losses Stone %

    LTDS1 LTDS2 LTDS Avg.

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    November 20thNovember 25th Cont.

    Due to the nature of air separation, feed in to hydro cyclone via LTDS #2 is

    not effective.

    Before silo stone < 0.5% was not constantly achievable (refer to Table 1).

    Therefore, workshop started fabricating new trunking to by-pass LTDS #2

    (Line 1) chipped mixtures to hydro cyclone.

    Airlock Airlock Airlock HydrocycloneChipped Conveyer

    Wet Kernel

    Boiler Dry Shell

    Conveyer

    1st Stage LTDS 2nd Stage LTDS

    Previous Setup

    R. Mill

    Airlock Airlock Airlock HydrocycloneChipped Conveyer

    Wet Kernel

    Boiler Dry Shell

    Conveyer

    1st Stage LTDS 2nd Stage LTDS

    Current Setup

    R. Mill

    Current setup using water separation entirely.

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    November 24thNovember 25th

    The new trunking was ready and put into testing. (Right Picture)

    Necessary mechanical modifications were made. (Left Picture)

    During the testing, LTDS damper and hydro cyclone were adjusted

    according to PK quality by supervisors.

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    Hydro Cyclone Fine Tuning Wet shell losses & dirt before silo were utilized as tuning parameters.

    Mill running two hydro cyclone for tuning by trial & error. (Left Picture)

    Shell was minimized on Stage 1 & 2, while kernel minimized on Stage 3

    during tuning.

    Stage 3

    Stage 2

    Stage 1

    Stones

    Wet Shell KernelLosses

    Wet Shell Kernel Losses

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    November 26th onward New trunking was put to use officially, data comparison as table below,

    Date

    Kernel Losses Stone %

    LTDS1 LTDS2LTDS Avg.

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    Future Problem Due to New Setup

    # Pros & Cons Effect

    1Carryover of hydro cyclone

    water into kernel silos

    Molding and odor of production kernels.

    Longer kernel cooking time, risk of uncooked kernel.

    2 Carryover of LTDS fiber toproduction kernel Molding and odor of production kernels due to watercarryover by LTDS fiber.

    3

    Wear and tear of

    hydrocyclone mechanical

    components (cone, impeller

    etc.)

    Increase maintenance cost & reduce hydrocyclone

    efficiency

    4 More wet shell excess

    Wet shell Increased to average 1.25% from 0.65% per

    tonne FFB. (converts to 10MT excess wet shell

    processing 800 MT FFB)