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7/27/2019 Assessment of Production Kernel (PK) Stone
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Assessment of Production
Kernel Stone Contamination
7/27/2019 Assessment of Production Kernel (PK) Stone
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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)