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Sivakumar Kumaresan

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Title: Sivakumar Kumaresan


1
  • Phytochemical Process
  • Debottlenecking Economic Studies

Sivakumar Kumaresan CEPP, UTM
2
Outline
  • Herbal industry and Tongkat Ali
  • CEPP Tongkat Ali production
  • Base case simulation
  • Debottlenecking alternatives
  • Scheme 1
  • Scheme 2
  • Scheme 3
  • Scheme 4
  • Economic comparisons
  • Conclusion
  • Question and Answer

3
Malaysias Rich Herbal Heritage
  • Malaysias rainforest - worlds oldest rainforest
  • 4th most bio-diverse nation in Asia after India,
    China and Indonesia
  • The one of the only 12 countries in the world
    with mega diversity of plants, medicinal and
    aromatic plants
  • Home to about 12 of all the plant species on
    earth, which has not been fully exploited and
    cultivated
  • One of the primary centres of biodiversity
  • 15,000 known plant species,
  • 3,700 are known to be useful,
  • 2,000 species with medicinal value
  • the balance remain largely unexploited.

M
GHT
i
M
GHT
i
4
Herbal Industry and Tongkat Ali
  • Herbal Industry
  • Local Market worth at least RM 2 Billion
  • Over 90 of products imported
  • Global Market USD300-500 Billion
  • Tongkat Ali
  • Traditionally used as aphrodisiac, postpartum
    tonic, energy tonic, anti fever and anti malarial
  • Scientically proven for its aphrodisiac, energy
    boosting, and anti malarial properties
  • Also has anti tumor potential
  • Currently sold at RM2500/kg extract and between
    10 -15,000 /kg in capsule form
  • Needs better engineering work to increase yield
    and quality

5
CEPP Tongkat Ali production
Tongkat Ali
Water extract
EXTRACTOR
Deionised Water
HOLDING TANK
Hot air
SPRAY DRYER
Extract fibre
Dehydrated water extract (final product)
FILTER
Slurry
6
Base case simulation
7
Base case simulation
  • Production process has long cycle time
  • Minimum cycle time is 24 hours
  • Bottleneck is Spray drier, 22 hours
  • Annual number of batches limited to 323
  • Process is economically infeasible
  • Production is insufficient to cover operating
    costs
  • Revenue is USD257883 based on 391 kg Extract
    produced
  • Need to debottleneck process
  • Tackle spray drier first

8
Throughput analysis
9
Operation Gantt chart
Time bottleneck spray drying (22.44 hrs)
10
Scheme 1
11
Scheme 1
  • Added second spray drier with same capacity
  • Improvements in
  • Minimum cycle time reduced from 24 hours to 13.4
    hours
  • Number of Batches increased to 591
  • Total extract yield increased to 714 kg
  • Process Economics still infeasible
  • Revenues insufficient to cover operating costs
  • Debottlenecking
  • Spray drier remains the bottleneck
  • Try an alternative process to reduce
    time/throughput bottleneck

12
Scheme 2
13
Scheme 2
  • Added evaporator to reduce extract liquid
  • Improvements in
  • Minimum cycle time reduced from 24 hours to 13.6
    hours
  • Number of Batches increased to 583
  • Total extract yield increased to 698 kg
  • Process Economics still infeasible
  • Extractor cost was lower, thus lower capital cost
  • Revenues still insufficient to cover operating
    costs
  • Debottlenecking
  • Evaporator becomes new bottleneck
  • Continue to try an alternative process to reduce
    time/throughput bottleneck

14
Scheme 3
15
Scheme 3
  • Added evaporator AND spray drier
  • Improvements in
  • Minimum cycle time reduced from 24 hours to 8.0
    hours
  • Number of Batches increased to 984
  • Total extract yield increased to 1178 kg
  • Bottleneck has shifted to V-102, thus drying
    section no longer bottleneck
  • Process Economics still infeasible
  • Revenues still insufficient to cover operating
    costs
  • Product selling price is too low!
  • Need value added scheme

16
Scheme 4
17
Scheme 4
  • Added capsuling, bottling, and packaging line
  • Improvements in
  • Batch cycle time reduced from 24 hours to 8.3
    hours
  • Number of Batches increased to 950
  • Total extract yield increased to 1137 kg
  • Slight cycle time reduction compared to Scheme 3
    due to increase in cycle time
  • Bottleneck shifted to capsuling process
  • Process Economics FINALLY feasible
  • Capsules sold at USD8700/kg vs Extract at
    USD655/kg
  • Return on Investment of 33
  • Annual revenue of USD6.3 Million

18
Throughput economic analysis results
19
Equipment specifications purchase cost for
Scheme 4
20
Equipment specifications purchase cost for
Scheme 4 (cont)
21
Conclusion recommendation
  • QA session
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