Showing posts with label DIPOM. Show all posts
Showing posts with label DIPOM. Show all posts

Sunday, 31 August 2025

🌴 Hana and DIPOM: From Participant to Educator

Hana sat quietly in front of the lecture hall, holding the teaching schedule for the Diploma in Palm Oil Milling Technology & Management (DIPOM). Once again, she had been invited by MPOB to teach two topics this year.

“Why me?” she asked herself. The answer, however, was not just about teaching—it was about giving back to a platform that once shaped her career.

📖 Memories of 2007 – A Turning Point

Hana recalled the year 2007, when she was still a participant in DIPOM.

Before that, her world was small, confined to the daily routines of palm oil mill operations. For over three years, she had been battling the challenges of mill management—pressure, fatigue, and steep learning curves. Her career path felt narrow, almost like a frog trapped in a well.

But through DIPOM, everything changed. She met fellow millers from other companies, attended lectures by seasoned industry practitioners, and visited mills run by her classmates on weekends.

That was the moment she realized the world of palm oil milling was far larger than she imagined. Networking, industrial exposure, and mentorship became the turning points in her professional journey .

🌟 From Participant to Educator

Fast forward nearly two decades later, Hana returned to the same platform—but now in a different role.

From a participant hungry for knowledge, she now stood at the front as an educator. For Hana, teaching at DIPOM was not just an assignment; it was a mission—to share her experience, inspire others, and pave the way for the next generation of millers and managers .

🤝 Supporting MPOB & the Industry

Hana firmly believed that the strength of the palm oil industry does not only lie in machines, technology, or policies, but in people—the millers and managers nurtured through programs like DIPOM.

That is why, whenever invited, she made every effort to be present. She also encouraged her peers in the industry to support MPOB in producing future leaders.

For Hana, knowledge shared today is an investment for tomorrow’s industry .

✨ Hana smiled. Once, she sat on the benches as a participant. Today, she stood at the podium as a lecturer. The journey felt complete—not because she had reached the end, but because she was finally giving back what she had once received.

📚 Footnotes

[1] MPOB (2007). History and Objectives of the Diploma in Palm Oil Milling Technology & Management (DIPOM). Malaysian Palm Oil Board.
[2] Razak, A. & Ismail, S. (2018). The Role of Training in Developing Palm Oil Mill Managers. Journal of Oil Palm Research.
[3] MPOB (2023). Capacity Building for the Palm Oil Milling Sector: Challenges and Opportunities. MPOB Technical Bulletin.

#blog #blogger #mpob #dipom

🌴 Hana dan DIPOM: Dari Peserta ke Tenaga Pengajar

Hana duduk termenung seketika di hadapan dewan kuliah. Di tangannya, ada jadual pengajaran Diploma in Palm Oil Milling Technology & Management (DIPOM). Tahun ini, sekali lagi dia dijemput oleh MPOB untuk mengajar dua topik.

“Kenapa aku?” bisik Hana dalam hati. Soalan itu membuatkan dia tersenyum kecil kerana dia tahu jawapannya bukan sekadar tentang mengajar, tetapi tentang membayar semula budi kepada sebuah platform yang pernah membentuk dirinya.

📖 Kenangan 2007 – Titik Perubahan

Hana teringat kembali tahun 2007, ketika dia sendiri masih seorang peserta DIPOM.

Sebelum itu, hidupnya ibarat katak di bawah tempurung. Tiga tahun bergelumang dengan rutin harian di kilang sawit — mengurus operasi, menanggung tekanan, belajar dari kegagalan — semuanya dirasakan seperti dunia yang sempit.

Namun, melalui DIPOM, Hana mula mengenali wajah-wajah baharu. Rakan-rakan miller dari pelbagai syarikat, tenaga pengajar berpengalaman, malah peluang melawat kilang sawit lain sewaktu hujung minggu bersama rakan sekelas.

Itulah saat Hana sedar bahawa dunia ini jauh lebih luas daripada apa yang dia bayangkan di sebuah kilang kecil. Networking, pengalaman lapangan, mentor industri — semuanya menjadi bekalan berharga dalam perjalanan kariernya.

🌟 Dari Peserta ke Penceramah

Kini, selepas hampir dua dekad, Hana kembali ke platform yang sama — tetapi dengan peranan berbeza.

Daripada seorang peserta yang dahagakan ilmu, kini dia berdiri sebagai tenaga pengajar. Baginya, mengajar di DIPOM bukan sekadar tugasan, tetapi sebuah misi untuk berkongsi semula pengalaman, memberi inspirasi, dan membuka ruang bagi generasi baharu miller untuk melangkah lebih jauh.

🤝 Menyokong MPOB & Industri

Hana percaya, kejayaan industri sawit tidak hanya bergantung kepada mesin, teknologi atau polisi, tetapi juga kepada manusia — miller dan pengurus kilang yang lahir daripada program seperti DIPOM.

Sebab itu, setiap kali dipanggil, Hana seboleh mungkin hadir. Malah, dia turut mengajak rakan-rakan industri untuk sama-sama menyumbang.

Kerana bagi Hana, ilmu yang dikongsi hari ini adalah pelaburan untuk industri esok.

✨ Hana tersenyum. Dahulu dia duduk di bangku peserta, kini dia berdiri di podium tenaga pengajar. Perjalanan ini seakan lengkap — bukan kerana dia sudah sampai, tetapi kerana dia telah memulangkan semula apa yang pernah dapat.

#blog #blogger #dipom #mpob #miller

Saturday, 13 June 2009

DIPOM ; The Palm Oil Factory




THE PALM OIL FACTORY

by Ir. Amin Buhari Hj. Md. Zain

summary of the notes

1. Planning for operation

1.1 Investment
1.2 Justification
1.3 Project Management
1.4 Project Appraisal

2. FEASIBILITY STUDY

A feasibility study cover :-

2.1 The FFB available for the manufacture
2.2 The cost of getting the FFB to the mill gate
2.3 The cost of manufacture
2.4 Investment cost of the Plant
2.5 Evacuation of the products and the markets
2.6 Approval from the relevant authorities for issuing of licences for the construction, operation and other environmental impact factor.
2.7 The proper phasing of the processing capacity of the palm oil mill which affects the cash flow requirements (especially when substaniate loan and interest are a major factor)

3. EFFICIENT PLAN & IMPLEMENTATION

3.1 Crop projection
3.2 Initial planning of required capacity
3.3 Site selections
3.4 Capacity expenditure projections
3.5 Details engineering design of machinery, choice of equipment, preparation of drawing, specifications, contract documents, etc.
3.6 Supervision of the construction
3.7 Training / commissioning
3.8 Project appraisal

4. CROP PROJECTION

Each project or mill will have different consideration but generally the method to be adapted for any proposed mil construction is to list the planted acreage along with the year of planting in the field and the allocation theoretical yields/acre in the following manner.
Table 1 : Year, Acreage, Yield, Crop projection
To complete the factor throughput requirement capable of handling peak month crops at 12.5 % of the annual crop and on 25 operational days / month at 20 hours/day
Table 2 : Crop projection, monthly crop, peak month crop, peak day crop
to justify throughput (mt/hr)
Throughput
8 hours operation
16 hours operation
20 hours operation
From the Table 1 & 2, we can make the choice on the timing of the operation and the mill capacity requirements.

a. Generally, the availability of the fuel is only sufficient nowadays when a mill operates at 20 tonnes FFB/hr. This is not to say we cannot operate a 10 mt/hr mill but will entail alternative power supply for the operation. Any throughput below 20 mt/hr will be considered low in the fuel availability and not able to support the kW demand.
On the other hand, it may be possible to get mains electricity which could make a 10 mt/hr mill a profitable venture.

b. Outlet available for the fruit? any nearby mill? or considered cheaper to manufacture outside rather than building your own mill. The break-even point is usually mill overheads or fixed charges against transport cost, assuming that the extraction rate given are always fixed.

c. Usually, it is better to delay heavy Capital Expenditure as long as possible. However, each case has to be considered separately. We must bear in mind that bank loans have to be serviced once the facility is built. There is an immediate commencement of depreciation.
extension program licensing MPOB throughput x 25 days x 16 hours/day = maximum crop

5. INITIAL PLANNING
Clearing land after the palms come into maturity or start bearing fruit. Actual requirement :-
5.1 Areas of mill's building and compound
5.2 Quarters for labors/staff/executive
5.3 Roads and accessibility

6. SITE SELECTION
Fixed variable : Transport of FFB, mill produces and mill operating cost such as the water supply, disposal of effluent etc. A compromise has to be made between these factors from which a determination can only be arrived at after a full cost study.
Site with poor ground loading conditions requires extra cost for piling and costly excavation/filing for undulating area respectively.
Cost in general infrastructure, water treatment costs, cost of road access to site etc
Regulations in force which could affect the selection of the site as regards to environmental conditions and has to be borne in mind.

7. CAPITAL EXPENDITURE PROJECTIONS
Important of available of money to prevent the project fall behind time and incurring extra loss.
example : 60 mt/hr Cost of a palm oil mill at roughly RM28,000,000., depends on where it is built and what goes into it.
Also depends on what equipment we chooses to install.

8. MILL DESIGN
Commence at least two years prior to the commissioning of the mill.
A long lead time on the delivery of the certain items of equipment and the choice of these items needs to be very established in order to allow the required period for fabrication, delivery and installation. (a period which could stretch to about 1 to 1.5 years).
Equipment selection, correct balance for throughput, steam consumption etc. The actual requirements. (Refer to Fuel/Steam Balance).
Standardization of equipment such as valves, gearboxes, electric motors, starters etc.
Main items of equipment, layout of the mill, design of the buildings and initial work on the layout of the machinery. Final work on the machinery layout and working drawings etc.
Thought must be given to the number of workers that will be required to operate the mill. In step of the development, the adjustment to the design can be made so that the best use of the workers.
Safety factors should be put at first place during the construction stage and even more during commissioning stage in regards safe working practices.

9. SUPERVISION OF THE CONSTRUCTION
Sufficient time should be allocated to carry out the actual construction work for the mill.
The civil works sholud be completed before work commences on the erection of machinery.
The erection of machinery and equipment should follow the logical sequence of commencing from in to out i.e pressing station erected first in the main bay, threshing and kernel/clarification station to follow.
To make sure all installation are user friendly for operation and maintenance.
10. TRAINING
The training of personnel who will be operating the mill when it is commissioned is something which invariable does not receive sufficient attention and yet is very important aspect as it could bring about savings regarding loss of product and expenditure on maintenance due to mal - operation of machinery.
Mill Manager to operators in the mill. A carefully planned program should be drawn up to suit the training of each individual or group of individuals.
Systematically implemented and correct.

11. COMMISSIONING
A period of one month.
First stage, all items of equipment should be run-up separately under no-load conditions.
A through inspection should be carried out on the equipment during operation and after the no-load test run. This should show up any faults such as misalignment, poor fitting, etc which can be corrected before running under loaded conditions.
Next stage, run at short period (4 to 8 hours) with the passing through the mill at low throughput.
Not all equipment should be brought out into operation, as in the initial stages of operation with product. The kernel station only can be run after nut silos are fully loaded.
If any faults arise with the equipment during the commissioning stage, it is the best to cease operation and correct the fault rather than improvise.
After a period of 2 weeks of gradually increase in running hours and throughput, it should be possible to operate the mill at its designed throughput.
The availability of fuel is always a problem during the commissioning period and an adequate quantity of fiber/shell should be stockpiled at the mill prior to the commissioning date.

12. PROJECT APPRAISAL
Well planned from the beginning to the end. It is not only important to get the project finished on time but also important it is finished within budget and performs up to specifications i.e quantity and quality.
Use of a CPA or network analysis to enable the various major event to be planned in such a manner that there was continuity of works and that important items are nor forgotten.
In order to improve the project management, the review of process, engineering design, cost factors. If a well organized Project Management Plan has been initiated form the start, then the final appraisal becomes a check against what was initially planned.
This is the most important part of any project and one that is usually not done effectively. That why our industry mistakes are often repeated over and over again.

More posts on the topic
1. Palm Oil Mill
http://zul1979.blogspot.com/search/label/Palm%20Oil%20Mill
2. Steam Engineer
http://zul1979.blogspot.com/search/label/Steam%20Engineer
3. Boiler
http://zul1979.blogspot.com/search/label/Boiler
4. Palm Oil Mill Operation
http://zul1979.blogspot.com/2017/06/operasi-kilang-sawit.html

Sunday, 7 June 2009

Majlis Penyampaian Sijil Diploma DIPOM 2007

Majlis Penyampaian Sijil Kursus DIPOM 2007, Penyelia dan Gradder yang berlangsung pada 29hb. Mei 2008 di Sabah Hotel, Sandakan, Sabah. Tahniah MPOB. Teruskan usaha untuk meningkatkan taraf industri !
Tn. Hj. Awaluddin dan Dr. Lee (MPOB)
Isteri yang banyak membantu dan memberi sokongan semasa mengikuti DIPOM
Ucapan Pengerusi MPOA Sabah yang penuh semangat
Group Picture : future mill managers
Ucapan mewakili perserta DIPOM 2007
Peserta DIPOM 07 yang hadir
Penyampaian

Friday, 5 June 2009

DIPOM : Fuel Steam Balance

1. Basic Requirement

Crop must be processed at a certain hourly throughput rate to give sufficient quantity of fuel in the form of palm fibres and palm shells for burning in the steam generating boilers to produce sufficient quantity of high pressure steam which will, in turn, provide the necessary motive power as well as the necessary process steam needed to run the Mill economically.
2. Crop Projection
  • Giving information about the area from which the FFB must be processed.
  • The type of planting material and age of planting.
  • Expected yield per acre from maturity to peak production at 9-10 years from planting.

3. Throughput Table
Having established a crop projection and assuming 12% of the annual crop in any peak month, it is possible to plan a factory throughput based upon one or two shifts operation up to 20 hours/day as indicated in the following table.

4. Conversion Of Crop To Fuel

Fuel produced per hour is related to :


(i) hourly FFB throughput rate
(ii) type of planting material - ratio of fuel to FFB
(iii) losses in palm fibres/shells/EFB


Ratio of total fuel available as a % of FFB is as follows :


Fuel Ratio to FFB by Weight Net calorific value
Fibres : 12% at Moisture   38%   11,350 kJ/kg
Shells : 7% at Moisture     10%   18,840 kJ/kg
EFB    : 22% at Moisture   50%     8,160 kJ/kg


A completely mixed fibre/shells fuel can give a net energy value of about 14,100 kJ/kg.

5. Conversion Of Fuel To Steam

Kg of water evaporated from and at 100 DegC per kg of fuel of various calorific values at the following efficiencies.

  • Latent Heat of Vaporization:
    Water requires 2,256 kJ/kg to convert from liquid to steam at its boiling point. 
  • Fuel Calculation:
    If a fuel, like wood, has a calorific value of, say, 10,000 kJ/kg, and the boiler is 70% efficient, then it would require roughly 2,256 / (10,000 * 0.70) = 0.32 kg of wood to produce 1 kg of steam. 

The thermal efficiency of a boiler naturally depends on the type of boiler installed, cleanliness of the fire or water tubes and general efficiency of operation. It is however, safe to assume a thermal efficiency of about 70% which at a fuel of 14,000 kJ/kg will give about 4.0 kg of steam/kg of fuel. Total steam which can be generated from the fuel available is shown hereunder.

1kg of coal : 8kg of steam

1kg of gas : 17kg of steam

Fuel Available (kg/hr) Steam Evaporation (kg/hr)

10 tons FFB can produce 1.9 mt solid fuel with 7.6 mt steam as below:-

10 tons FFB/h 1,900 7,600
20 tons FFB/h 3,800 15,200
30 tons FFB/h 5,700 22,800
40 tons FFB/h 7,600 30,400
50 tons FFB/h 9,500 38,000
60 tons FFB/h 11,400 45,600


From above table it appears that the fuel available at a throughput of 30 tons of FFB/h should be sufficient to evaporate about 22,800 kg of steam. It should therefore be possible to establish the fuel/steam balance by installing a 22 T/hr boiler.

6. Power Requirements In The Mill

Some of the actual values obtained :

Mill Size Power Consumption
10 T FFB/hr 28 kWh/T
20 T FFB/hr 20 kWh/T
30 T FFB/hr 16-17 kWh/T
40 T FFB/hr 18-19 kWh/T
50 T FFB/hr 18-19 kWh/T
60 T FFB/hr 19-20 kWh/T


These mills supply steam power for processing as well as domestic load. This does not include additional equipment such as extended effluent treatment plant, decanters and EFB presses.

7. Process Steam Requirement In The Mill

(As a guide only - obviously the steam consumption depends on the way we run the Mill and how well the steam system & steam traps are maintained)

L.P. Steam

1. Sterilisation single peak 100 kg/T FFB
double peak 200 kg/T FFB
triple peak 270 kg/T FFB
2. Other Process Units : 250 kg/T FFB


H.P. Steam
Deaerators & Steam Feed Pumps : 125 kg/T FFB
depending on whether reciprocating or turbine driven steam feed pumps are used.
TOTAL single peak 475 kg/T FFB
==== double peak 575 kg/T FFB
triple peak 645 kg/T FFB


Rule of thumb figures for process steam requirements :
0.4 - 0.5 T steam/T FFB on average

How to improve steam generation in palm oil mills?

To improve steam generation in a palm oil mill, focus on optimizing the steam cycle, enhancing combustion control, maintaining equipment, implementing energy recovery systems, and closely monitoring data. Specifically, this includes optimizing feedwater quality, recovering condensate, and potentially using steam accumulators. 
Detailed strategies:
  1. 1. Optimize the Steam Cycle:
    • Feedwater Economizer: Installing a feedwater economizer can preheat the water before it enters the boiler, reducing the energy required to produce steam and improving overall efficiency. 
    • Blowdown Control: Reducing the blowdown rate of the boiler, potentially through an automatic blowdown control system, can minimize heat loss and improve steam quality. 
    • Condensate Recovery: Implementing systems to recover and reuse condensate (water from condensed steam) can significantly reduce water and energy consumption. 
    • Steam Accumulators: Using steam accumulators can help optimize steam supply and reduce the need for fresh water, particularly when production capacity is increased. 
  2. 2. Enhance Combustion Control:
    • Fuel Optimization: Ensure proper fuel mixing and combustion conditions to maximize heat transfer efficiency and minimize fuel waste. 
    • Air/Fuel Ratio: Maintaining the correct air-to-fuel ratio is crucial for efficient combustion. Too much air can cool the flame, while too little can lead to incomplete combustion. 
  3. 3. Maintain Equipment:
    • Clean Heat Exchangers: Regularly cleaning boiler heat exchange surfaces ensures maximum heat transfer from the burning fuel to the boiler water. 
    • Insulation: Proper insulation of steam pipes and equipment minimizes heat loss, improving steam pressure and reducing energy consumption. 
    • Regular Maintenance: Implement a regular maintenance schedule for all steam-related equipment to prevent leaks, corrosion, and other issues that can impact efficiency. 
  4. 4. Implement Energy Recovery Systems:
    • Waste Heat Recovery: Explore opportunities to recover waste heat from sources like flue gas or exhaust steam from the sterilizer. 
    • Cogeneration: Consider cogeneration systems that can utilize waste heat to generate electricity, further improving energy efficiency. 
  5. 5. Monitor and Analyze Data:
    • Real-time Monitoring: Install sensors and monitoring systems to track key parameters like steam pressure, temperature, and flow rate. 
    • Data Analysis: Analyze the collected data to identify areas for improvement and track the effectiveness of implemented changes. 
By focusing on these areas, palm oil mills can significantly improve steam generation efficiency, leading to reduced energy costs and increased overall plant efficiency.