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MALAYSIAN OIL SCIENCE AND TECHNOLOGY Vol. 27 No. 2 (2018) Hybrid OxG Palms: GM Soy: High-Yield, GM-Canola for LC High Oleic Oils High Oleic Oils ω3 Oils Coconut Revival: New Products New Technologies in PO Milling Innovations: Food Quality & Safety Disruptive IR 4.0 Transforming the PO Industry USD 12.00/RM 30.00 • FREE FOR MEMBERS THE PUBLICATION OF THE MALAYSIAN OILand Malaysian Oil Science SCIENTISTS’ Technology 2018AND Vol. 27TECHNOLOGISTS’ No. 2 ASSOCIATION a
MALAYSIAN OIL SCIENTISTS’ AND TECHNOLOGISTS’ ASSOCIATION (PERSATUAN AHLI SAINS AND TECHNOLOGI MINYAK MALAYSIA) 29th ANNUAL GENERAL MEETING 27th April 2019 at 9am Hall 2, Level 4 Crystal Crown Hotel Petaling Jaya, Selangor The Future of Palm Oil Industry Through IR 4.0 1-Day Best Practices Workshop by MOSTA & FUSIONEX Thursday, 25 April 2019 Fusionex office, Level 12, Tower A, Plaza 33, No. 1 Jalan Kemajuan, Section 13, 46200 Petaling Jaya Limited Places 200 max (contact MOSTA)
Malaysian Oil Science and Technology (MOST) INTERNATIONAL ADVISORY COMMITTEE: COVER STORY James Fry (LMC,UK) While there are much geopolitical turmoil and Dennis J. Murphy (Murphy Biotechnology demographic problems in many parts of the world, Consultancy, United Kingdom) great strides have been made in agricultural oil and Paul Hovelmann (Cognis, Holland/Germany) Thomas Mielke (ISTA Mielke, Germany) food crops. Record yields of soybean are coming from Yusof Basiron (Malaysia) highly mechanised US farms (Barton) and higher- Marc Kellens (Desmet Ballestra Group, Belgium) yielding, high-oleic GM soybeans are benefiting the farmers. Hybrid OxG oil palms (Teo & Wong) have been EDITORIAL BOARD developed for higher oleic oils, higher tocotrienols and Chairman many other useful traits. Except for the coconut (Dayrit S.H. Goh +6012-363 1948 & Salum) there has generally been an oversupply of +603-7958 1391 edible oils and this has led to much trade frictions +614-3194 0825 giving rise to intense negative campaigns against chmgsh@yahoo.com tropical oils with perceived sustainability issues (Park). chmgsh@gmail.com Additionally low uptake from the biodiesel sector Members: coupled with volatile petroleum crude have led to Tang Thin Sue depressed prices (Park; Benny Lee) of most edible oils. S.F. Cheng Chuah Cheng Hock High quality palm oils are available from present M.R. Chandran plantations with the adoption of best practices (Lee) S. Krishnan and recommendations for new quality guidelines of Teh Soek Sin CPO (3.5% FFA & DOBI > 2.5) for food uses have been Mah Siau Hui made (Kellens et al). For new food safety demands on levels of process contaminants from the EU, refining MOSTA Council Members 2017/2018 options and affordable modifications to present Academician Emeritus Prof Tan Sri Datuk Dr Augustine S H Ong physical refining operations have been detailed Mr S. Krishnan (Kellens et al; Lee). Prof Dr Chuah Cheng Hock Ms Christine Ong May Ee Meanwhile, GM canola has been able to produce Dr Goh Swee Hock long chain omega-3 oils (Abeywardena) which will Datuk Dr Choo Yuen May provide the much needed nutrient as natural marine Mr MR Chandran fish resources are being exhausted. Soy and oil palms Mr Lee Keong Hoe can soon provide high oleic oils much demanded by Ms Khor Yu Leng consumers while MCT oils from the coconut and palm Tunku Alina Alias kernels are beginning to be appreciated as replantings Printing: of coconut will hopefully fulfill new demands (Dayrit & Percetakan Soon Lee Heng Sdn Bhd Salum). The oil palm (Teo & Wong) has specialty Elaeis 15, Jalan Besar, Selayang Baru cultivars to provide high tocotrienols and omega-7 68100 Batu Caves, Selangor oils, as well as other traits. Layout: Public Media Agency Sdn Bhd 717, Menara Mutiara Majestic, Jalan Othman Acknowledgements: Pictures & Chart from CK Wong, USDA, 46000 Petaling Jaya, Selangor Dayrit & Salum, SH Goh and Benny Lee www.publicmediaagency.org publicmedia.agency@gmail.com Malaysian Oil Science and Technology 2018 Vol. 27 No. 2 i
Malaysian Oil Science and Technology (MOST) EDITORIAL POLICY INFORMATION MOST is a regular bulletin devoted to furthering ARTICLES: Contributions are invited for feature the objectives of Malaysian Oil Scientists’ and articles, news items, newsletters, letter to the Technologists’ Association. This is to promote interest editor, general articles, research papers, review to in all aspects of oils and fats in Malaysia, regionally the community involved in oils and fats including and worldwide. Articles of interest could be directed business managers, chemists, engineers, scientists, to the layman, technologist, scientist, researcher or technologists and other personnel involved in various the entrepreneur. News of the association’s activities commercial aspects of oils and fats. All articles will and developments in oils and fats will be routinely be refereed and suitably edited before publication. published. Letters to the editor are also acceptable after editing. The views expressed by the contributors are not FORMAT: Instructions to authors may be obtained necessarily endorsed by MOSTA. The editorial board from the Editor or recent issues of MOST may be used and the referees would do their best to ascertain as examples. General instructions are similar to the authenticity and accuracy of information on all articles format required by major international journals and and MOSTA reserves the right to alter or to omit any include the following: TITLE, Abstract, Text with major article or advertisement submitted. No responsibility headings (Introduction, Materials and Methods, is accepted by the association, the editor or the printer Results and Discussion, Acknowledgements and for the accuracy of the information contained in the References). Abbreviations, symbols and units used text and advertisement. MOSTA requires indemnity are as by the best of international journals. In addition from advertisers and contributors against damages to a hard-copy, authors are encouraged to send with which may arise from materials published. their papers as attachments in e-mail for easy editing using Word or other common IBM-PC software. All materials in MOST are copyright and should not be reproduced wholly or in part without the written ADVERTISEMENTS: Advertisers are welcomed to consent of the editor. place their Ads, which will be printed at reasonable cost, in this publication. Materials for publication should be submitted directly to the editor and would normally require two SUBSCRIPTIONS: Individuals and libraries may month’s editorial/refereeing work prior to publication. subscribe to this publication. Guidelines of formatting of technical material may be obtained from the Editor. Web editions are promptly published after editing. MOSTA SECRETARIAT: C-3A-10, 4th Floor, Block C (Lift No. 5) Damansara Intan No. 1 Jalan SS20/27 47400 Petaling Jaya DEADLINES Selangor Darul Ehsan, Malaysia Deadlines for publishing edited versions and Tel : 603-7118 2062 / 64 Fax: 603-7118 2063 advertisements are 20 days before the publication E-mail: mosta.secretariat@gmail.com dates of each volume. Website: http://www.mosta.org.my ii Malaysian Oil Science and Technology 2018 Vol. 27 No. 2
CONTENTS i Cover Story ii Editorial Policy iii Contents iv Editorial 69 REFINING CRUDE PALM OIL: CURRENT STATUS AND LATEST DEVELOPMENT TO ENSURE HIGH FOOD OIL QUALITY AND SAFETY Mark Kellens, Wim De Greyt and Antonios Papastergiadis 83 DEVELOPING INNOVATIVE TECHNOLOGIES FOR PALM OIL MILLING: CHALLENGING - ENRICHING - PROFITABLE JOURNEYS K.H. Lee 94 ADVANCES ON BREEDING FOR HYBRID OxG OILS C.J. Teo and C.K. Wong 104 PRICE OUTLOOK: PALM OIL USE IN FOOD, OLEO AND BIOFUELS (EU, US, CHINA, JAPAN AND INDONESIA) Meezy Park 109 IT/AI SOLUTIONS FOR THE PALM OIL INDUSTRY Ivan Teh 113 RISING GLOBAL DEMAND FOR LONG-CHAIN OMEGA3 PUFAS: EMERGING SOLUTIONS FOR A SUSTAINABLE SUPPLY Mahinda Abeywardena 118 WORLD SCENARIO OF SOYBEAN OIL & PROTEIN: CURRENT STATUS (PRODUCTION, APPLICATIONS, MARKET TRENDS), ISSUES, CHALLENGES AND FUTURE PROSPECTS Rich Barton 127 GLOBAL SCENARIO OF COCONUT OIL Fabian M. Dayrit and Uron N. Salum 146 ANTICIPATING 2019 MARKET DIRECTION AMIDST CHALLENGES Benny Lee vii News ix Talking Points xi On A Lighter Note xiii Index Malaysian Oil Science and Technology 2018 Vol. 27 No. 2 iii
Editorial Volatile and Sinking Markets The background noise may be the tit-for-tat tariff trade war, but it is for the all-important domination of the Crude oil staged a brave comeback hitting $76 in the advanced digital technology and global cyberspace. climb towards the $100 mark (in anticipation of a total Iranian oil ban) but only to fall back dramatically to $50 (when waivers to China and other countries were given More Than A Palmful of Problems for importing Iranian oil), an obvious consequence The anti-palm oil campaign from EU is one case where of too much political interventions. A low oil price is the glut of palm oil has been considered a threat to welcome for energy consumers (cheaper transport competing oil crops, especially in EU. The rapid growth and manufacturing) as GDPs can be raised 0.5-0.7% of production of palm oil, which cannot be halted once per $10 drop in price for importing countries. Over the the trees are planted, has come about with producers longer term, oil is predicted to keep rising as supplies not taking this (marketing) into consideration. And on can be bolstered by hydraulic fracking technology hindsight the total takeovers of British and French oil when prices are above $50, and probably peak oil palm companies may not have been wise by reducing could occur around 2050. Low petroleum crude prices such European stakeholders. depress CPO prices in view of the Fry’s price band relationship due to biodiesel (Park). Previously the US which hardly imports any palm oil (< 1%) for consumption, had launched a preemptive Geopolitics and the US-China trade war affect other health campaign against palm to slow its growth but commodities such as soybeans apart from edible oils this has now been agreed by all parties to be baseless, (Barton; Park) while unnecessary waste of resources unfair and unjustified. Palm oil, kernel oil and the and increase in carbon footprint are seen as China coconut (Dayrit & Salum) are now much appreciated buys soybeans from S America which had been by consumers and manufacturers for nutritional diverted from US. The slide in prices for soybeans and goodness and functional versatility. Furthermore, for soyoil will cap and depress palm oil prices. Even after many competing polyunsaturated oils, a ban has now the temporary tariff truce, economic uncertainties been made on trans fats from partial hydrogenation remain and negative effects on global trade will of such oils, on top of the warning against excessive cause persistent volatility. Inability to be competitive intake of omega-6 oils. in free trade on many areas has been distorted in the guise of sustainability, labour exploitation, or even It is clear that wealthy first world nations are not national security issues whether they be edible oils enthusiastic of palm oil as nature’s gift to the world: and soybeans (Barton; Park; Dayrit & Salum) or high where sight is given to those potentially going blind technology products/services. It is clear that most rich for lack of vitamin A (abundant in CPO); potential nations including the present superpower will do their prevention of strokes and Alzheimer’s disease from utmost to maintain their present leadership advantage. palm tocotrienols and MCTs from kernel oil; nutritional iv Malaysian Oil Science and Technology 2018 Vol. 27 No. 2
EDITORIAL heart-healthy palm olein is provided with high sn-2 of global debt, with the two biggest economies also unsaturation and for use as one of the best frying competing in the race to the bottom. The toppish oils; palm kernel oil is provided with medium chain global markets combined with trade conflicts could be triglycerides having special nutritional values; and the early signs that a correction of global financial excesses availability of new potential health-giving omega-7 is about to begin or has begun. oils. On sustainability there is no other more productive oil crop than the oil palm: averaging 4-8 times more yield than other major competing oil crops; ability to Biofuels supply about 30% of oils to the world while using only Weak crude oil prices mean weak edible oil prices due 6.6% of the land used for other oil crops; sparing use of to the relationship with biodiesel, which the present only 1/7 of fertilizers as compared to other oil crops; a excess production has been targeted for use in the palm tree which is a net sequester of CO2 and provider mitigation of climate change. However nations may of green tree cover; sustainable (RSPO & MPSO) palm have found that it is economically more profitable to oils will be produced more than market uptake as all be in the climate denial camp in an era of cheap fossil oil palms will be MSPO-certified in Malaysia by 2019. fuels, apart from the fading enthusiasm in the use of biofuels against climate change. Further, an adaptive Meanwhile refined palm oils, having relatively more strategy to negative effects seems to be gaining diacylglycerols, face a new problem of trace process optimistic acceptance. Excess palm oil from increasing contaminants (GE and 3-MCPDE), but these are also supplies from Indonesia due to maturing palms has found in other oils that are physically refined. Mitigation been unable to find the anticipated biodiesel market procedures have been recommended (Kellens et al; in developed countries which had to support their Lee). In view of the stringent requirements demanded domestic crops rather than the cheaper palm oil. by EU, added costs are inevitable for physical refining Thus, it has been disastrous for palm oil prices even while recommendations have been made to produce as biodiesel finds aggressive use in the home markets better quality CPOs with less FFA (Kellens et al; Lee). (B20 in Indonesia; B10 in Malaysia by Dec 2018). The problems of the world trade and economy are Indonesia’s tax structure for B20 biodiesel mandate complex, even if it is free and fair trade being targeted is commendable but implementation over the vast to find solutions. Population pressures (Barton) and the number of the nation’s islands may be challenging. quest for dominance of technology are difficult issues, Meanwhile the continuing increase in production from whereby competition in agricultural produce now Indonesia for 2019 will affect prices negatively (Park), pales in significance. It is political agenda but nothing even as price discovery and forecast is becoming associated with sustainability of supply of food more of a Nostradamus art in the present politically calories, the abundance of which have come about uncertain and volatile era (technical chart by Benny from advances in science in general and genomics Lee in cover page). in particular. This fact should be enforced unto the With so many economic problems on the plate, climate mindsets of environmentalists, conservationists and deniers seem to have gained the upper hand and a climate specialists who are pushing all the blame on new political trend seems to be for an adaptation to poor palm farmers; in Malaysia there has always been global temperature rise. EU’s enthusiasm for biofuels much available agricultural jobs for people of poorer to mitigate climate change has waned with uncertain neighbouring countries. Negative campaigns should mandates and they are pushing hard for the phasing target for less consumption (by the wealthy) of pasture out of palm biodiesel by 2030. Perhaps, the previous animal meats which have caused the highest carbon drive for aviation biofuels could be rekindled as no footprints (Barton). other energy source can reduce this source of GHG There are bigger world economic issues than concerns emissions. The technology is ripe to collaboratively of food, excess or lack of it, and it could be population produce aviation jet fuel at reduced costs on growth (Barton) within a planet of finite resources. But economies of scale. lurking in the background is the unsolvable problem Malaysian Oil Science and Technology 2018 Vol. 27 No. 2 v
Refining Crude Palm Oil: Current Status and Latest Development to ensure High Food Oil Quality and Safety Mark Kellens, Wim De Greyt and Antonios Papastergiadis Desmet Ballestra Group, Belgium [Lecture presented at OFIC2018 Conference, 17th Oct 2018, Kuala Lumpur] Introduction Why is palm oil under fire? The growth of production of palm oil has been Some perceived reasons may be the following: immense and it has become the dominant edible in the • Deforestation & destruction of wildlife habitat world (Fig. 1). In the years 1999 to 2018 Malaysian CPO • Disregard of local community rights production has been increasing (except in few years) • Impact on global warming at about 0.5 MMT/yr while higher growth was from • Ethical issue of food oil used for fuel Indonesia at ~ 1.75 MMT/yr. Most of the oil has been used in food with minor uses in surfactants, biodiesel, oleochemicals, etc (Fig. 1). Palm oil is the number 1 What may be the other reason for anti-palm oil campaign? food oil (>30%) and will continue to strengthen its • Too efficient, too versatile & too cheap? position in the coming decades. • Has it become a political matter, as other oils are being threatened? Figure 1. Production of palm oil and its widespread uses Malaysian Oil Science and Technology 2018 Vol. 27 No. 2 69
REFINING CRUDE PALM OIL: CURRENT STATUS AND LATEST DEVELOPMENT TO ENSURE HIGH FOOD OIL QUALITY AND SAFETY OIL QUALITY REFINING PROCESS PLANT EFFICIENCY PROCESS SUSTAINABILITY Figure 2. Efficient and sustainable refining processes for quality oils • Is it healthy (more saturated fats) and safe (can have Cost-Efficient Sustainable Production of High more 3-MCPDE/GE) to use? Quality Palm Oil • Is the consumer made aware of the real facts? Oil processors and technology providers are continuously looking for solutions to solve current What is the alternative? problems and prepare for new challenges to come. Oil can be refined to the desired quality and safety There is no alternative as no other crop is as efficient standards of consumer needs while balanced by cost as the oil palm and no other oil is as versatile as palm and sustainability (Fig. 2) and palm kernel oils. “Half of the world’s population uses palm oil in food, and if we ban or boycott it, other, more land-hungry oils will likely take place”.- Oil Refining Inger Anderson, IUCN Director General. There will be Oil refining means the removal of unwanted environmental disasters and total climate change as minor components while avoiding production of it will need as much as five to ten times more land contaminants as illustrated in Fig. 3. Refining removes need to be found to cultivate other oil crops to replace unwanted foreign as well as oil-related impurities and palm oil. at the same time limit or eliminate process-related The answer is to make all production follow the contaminants. With improved analytical detection sustainable production methods as well as oil methods, more trace process contaminants (3-MCPDE processing techniques to be food-safe. The palm oil and GE) have been detected in oils and technologies industry is taking measures to ensure sustainable have to be modified to reduce or eliminate them. production of high quality crude palm oil for food GE and 3-MCPDE are new trace contaminants found uses but these need time for implementation of in all edible oils and are compared to other trace new policies. contaminants as well as the much larger levels of trans fat components (Fig. 4). Crude Oil REFINING Refined Oil FOREIGN OIL-RELATED PROCESS-RELATED Pesticides Gums TFA PAHs FFA Polymers PCB Color bodies Acrolein Dioxins Oxidation products Dialkylketones Aflatoxins Metals 3-MCPDE/GE ... ... ... Figure 3. Refining to remove unwanted components and limit process -related contaminants 70 Malaysian Oil Science and Technology 2018 Vol. 27 No. 2
REFINING CRUDE PALM OIL: CURRENT STATUS AND LATEST DEVELOPMENT TO ENSURE HIGH FOOD OIL QUALITY AND SAFETY 1Polycyclic aromatic hydrocarbons; 2Mostly Aflatoxins in peanut oil; 3Mainly in Marine oils; Risk Figure 4. Comparison of some contaminants of concern Highest levels of 3-MCPDE and GE are found in physically refined Palm oil 3-MCPD esters ≠ Glycidyl Esters Main precursors Main precursors 3-MCPDE Chloride GE “DAG” (“organic”/ acid) (FFA/alkaline) Figure 5. Nature and formation of 3-MCPDE and GE in oils and fats Process Contaminants in Food Oils: the Ongoing the presence of chloride impurity. They are formed Challenge for Palm Oil differently and have different properties and require different and specific mitigation solutions. Glycidyl esters (GE) and mono-chloropropandiol esters (MCPDE) are newly detected trace processed components found in edible oils and fats and the Targets Limits for GE highest levels are found in physically refined palm Maximum levels for GE are described in the annex oils. The chemical structures and their formation are to regulation (EC) No 1881/2006, section 1 in the summarized in Fig. 5. The common precursors are the COMMISSION REGULATION (EU) 2018/290 of 26 high levels of diacyglycerol (DAG) in crude palm oil and February 2018 as given below: 208 Glycidyl fatty acid esters expressed as glycidol Maximum level (μg/kg) ppm 4.2.1. Vegetable oils and fats placed on the market for the (1000) final consumer or for use as an ingredient in food with 1 the exception of the foods referred to in 4.2.2 4.2.2. Vegetable oils and fats destined for the production of baby food (500) and processed cereal-based food for infants and young children 0.5 Malaysian Oil Science and Technology 2018 Vol. 27 No. 2 71
REFINING CRUDE PALM OIL: CURRENT STATUS AND LATEST DEVELOPMENT TO ENSURE HIGH FOOD OIL QUALITY AND SAFETY As GE get enriched in Palm olein, industry may need to Target Levels for 3-MCPDE set lower limits for RBDPO (?), such as New suggested maximum 3-MCPDE levels according < 0.7 ppm GE for category 4.2.1 (?) to regulation (EC) No 1881/2006, section 1 (Draft < 0.3 ppm GE for category 4.2.2 (?) released on 4 October 2018): As 3-MCPDE get enriched in palm olein, industry may Conventional Route of Physical Refining of Palm Oil need to set lower limits for RBDPO (?) < 1.5 ppm 3-MCPDE for category 4.3.1 (?) Physical refining may be summarized below to provide < 0.5 ppm 3-MCPDE for category 4.3.2 (?) the desired refined oil of the desired specifications: CPO Dry acid pretreatment Bleaching with ABE Stripping-deodorization Hydrating gums, reaction Absorbing impurities, breaking Removing FFA, heat bleaching, with metals… down pigments… eliminating taste and odour, improving stability… RBDPO: PORAM spec Industry FFA (%palmitic acid): 0.1% max 0.03-0.05% max M&I: 0.1% max 0.01-0.05% max Colour (5.25” Lovibond cell): 3 red max 1.5-2.5 red max M.Pt (AOCS Cc 3-25): 33-39°C (ns) IV (Wijs): 50-55 (50.5-52.5) PV: (ns) nil Taste: (ns) bland P: (ns) 1-3 ppm max 72 Malaysian Oil Science and Technology 2018 Vol. 27 No. 2
REFINING CRUDE PALM OIL: CURRENT STATUS AND LATEST DEVELOPMENT TO ENSURE HIGH FOOD OIL QUALITY AND SAFETY Conventional Physical Refining of CPO is then followed by a single temperature and pressure stripping-deodorization (Fig. 7). Conventional CPO refinery uses dry acid pretreatment plus bleaching but not wet pretreatment (Fig. 6). This Figure 6. Conventional physical refining: dry acid pretreatment and bleaching Figure 7. Conventional physical refining: single temperature & pressure stripping deodorization Malaysian Oil Science and Technology 2018 Vol. 27 No. 2 73
REFINING CRUDE PALM OIL: CURRENT STATUS AND LATEST DEVELOPMENT TO ENSURE HIGH FOOD OIL QUALITY AND SAFETY Mitigation of the formation of GE and 3-MCPDE has Processors may not like it as there are higher utility been examined from various technological aspects costs in NaOH and H2SO4, higher oil losses (acid oils (Fig. 8). CPO quality remains an important parameter vs deodorizer distillate), and troublesome soapstock to be able to achieve low levels of 3-MCPDE. Fig. 9 splitting forming more waste water. With 70 MMT/ provides data from reasonably good quality CPO from yr of CPO produced chemical refining may not be physical refining but better values come from chemical the solution. refining. Chemical refining is effective process solution for CPO as for other edible oils for low 3-MCPDE. fresh oil with high DOBI Crude Palm Oil QUALITY -Low FFA / low DAG (GE) CPO washing -low Chloride (3-MCPDE) Mitigation options Solutions low Chloride (3-MCPDE) Crude Palm Oil QUALITY fresh oil with high DOBI CPO washing Low FFA / low DAG (GE) DRY DEGUMMING Wet degumming (enzyme?) Acid washing 0.05-0.15% H3PO4(85%) Other degumming acid 70-90°C, 1-15 min - No acid at all > caustic neutralising 3-MCPDE BLEACHING 0.6-1.2% Natural bleaching earth Activated Bleaching Silicas/silicates /zeolites Modified bleaching Earth, 90-110°C, 20-40 Combination of adsorbents, (NBE) min, 30-100 mbar acid & alkaline conditions DEODORIZATION 250- Lower temp / longer time Dual temp stripping / 265°C, 45-90 min Dual temp stripping/deodo deodorising 2-4 mbar, 0.6-1.2% Low P (1-2 mbar) stripping steam GE Post-bleaching/deodorising Mild refining Refined Palm Oil Post-stripping Low P Figure 8. Useful conditions in physical refining to mitigate 3-MCPDE 1. Chemical Refining is the Best Solution for Low 3-MCPDE (& GE)? Data from experiments on chemical refining are given in Fig. 9, where low guideline levels can be achieved. Industrial + lab refined samples 3-MCPDE (ppm) 1 3-MCPD Esters in Chemical Refined Palm Oil 0.5 CPO quality remains the key factor Figure 9. Chemical refining can achieve the lowest levels of 3-MCPDE 74 Malaysian Oil Science and Technology 2018 Vol. 27 No. 2
REFINING CRUDE PALM OIL: CURRENT STATUS AND LATEST DEVELOPMENT TO ENSURE HIGH FOOD OIL QUALITY AND SAFETY 3-MCPDE in refined palm oil (ppm) Optimized Physical Refining 3.01 25% 2.64 2.54 40% 2.29 C/R 1.86 Washing with ¢ No ¢ Caustic ¢ Water ¢ Acid Figure 10. Effect of CPO washing on 3-MCPDE formation 2. CPO Washing: Effect on 3-MCPDE Formation Effect of CPO Washing on 3-MCPDE Formation in Good & Premium Quality CPO Physical refining results for different washings are given in Fig. 10 where water washings are given in Processing conditions. Washing with 5% water without more detail. Chemical refining still provides the lowest acid or caustic; bleaching with 10 kg natural bleaching level of MCPDE. Effectiveness of CPO washing depends earth/tonne oil; dual T stripping/deodorization at on crude oil quality & when it is applied. Most effect 240°C/220°C (120 min), 8 and 12 kg/T steam, 3 mbar. is from ‘caustic washing’, but this is less than chemical The results are given in Table 1. refining. Oil losses of 0.05 – 0.1% occur if 5% wash water • Washing has a determining impact on 3-MCPDE is used and 1-2% oil/FM in wash water. Combined mitigation acid degumming/washing further reduce P and other elements. • Dual temperature deodorization gives low GE at 0.24- 0.42 ppm Table 1. 3-MCPDE formation mitigation in washing good and premium quality CPO Feedstock Good quality CPO Good quality CPO Premium quality not washed CPO washed Not washed FFA% (16:0) 3.7 3.5 1.3 DOBI 2.6 / 3.4 Refining Physical refining Physical refining Physical refining Chemical refining FFA% (16:0) 0.04 0.04 0.03 0.02 Colour Lovibond (51/4) 2.0R/51Y 2.2R/57Y 1.2R/28Y 0.7R/16Y 3-MCPDE (ppm) 1.21 0.37 0.46 0.08 2-MCPDE (ppm) 0.66 0.21 0.25 0.05 GE (ppm) 0.40 0.42 0.27 0.24 Malaysian Oil Science and Technology 2018 Vol. 27 No. 2 75
REFINING CRUDE PALM OIL: CURRENT STATUS AND LATEST DEVELOPMENT TO ENSURE HIGH FOOD OIL QUALITY AND SAFETY Nano-Washing Nano-washing technology is shown in Fig. 11; this is efficient, flexible and provides low effluent. Figure 11. Nano washing technology 3. Bleaching: Effect of Amount and Type of BE Experiments conducted on the use of bleaching earths have provided results as shown in Fig. 12. Bleaching conditions: 105°C, 50 mbar, 30 min. Büchner filtration over Whatman No1 Deodorization conditions: Dual T stripping/ deodorization, 240°C /220°C (120 min). Total sparge steam : 1.6 % - pressure: 2 mbar Lowest levels of 3-MCPDE formation can be achieved by (a) use of natural BE iso acid activated BE is No HCl – treated BE used recommended, (b) higher BE dosing (more pronounced effect with natural BE). Natural BE Acid BE pH 7.8 3.7 Cl- (mg/L) 7.1 28.4 Formation of 3-MCPDE and GE During Bleaching Figure 12. Effect of bleaching earths Experiments carried out on high dosage of activated on MCPDE formation bleaching earth showed MCPDE and GE can be formed with higher dosages of bleaching earth and further formation of MCPDE in deodorization (Table 2). There is no formation of GE. During deodorization there is further formation of 3-MCPDE. Isomerisation of 3-MCPDE to 2-MCPDE occurred. 76 Malaysian Oil Science and Technology 2018 Vol. 27 No. 2
REFINING CRUDE PALM OIL: CURRENT STATUS AND LATEST DEVELOPMENT TO ENSURE HIGH FOOD OIL QUALITY AND SAFETY Table 2. Formation of MCPDE and GE during bleaching and deodorization BE type Natural BE Acid activated BE BE dosage (kg/T) 10 15 20 10 15 20 Bleaching T (°C) 105 105 85 105 105 105 105 FFA % (16:0) 0.05 0.06 0.05 0.05 0.05 0.05 0.05 Color Lovibond 51/4 6.1R/70Y 5.0R/70Y 6.4R/70Y 5.2R/70Y 5.5R/70Y 4.4R/70Y 4.0R/70Y Bleached palm oil 3-MCPDE (ppm) 0.34 1.20 2-MCPDE (ppm)
REFINING CRUDE PALM OIL: CURRENT STATUS AND LATEST DEVELOPMENT TO ENSURE HIGH FOOD OIL QUALITY AND SAFETY 260°C 3 mbar 60 min, 1% SS Glycidyl esters (ppm) 1% SS 3 The lower the P, the higher 2 mbar the NO losses 240°C (MAG, 230°C DAG, 220°C 1 Toco) 0 1 2 3 4 5 Time (hr) Figure 14. Effect of temperature on GE formation Figure 15. Balance of stripping and formation of GE Can GE be Stripped During Deodorisation? Effect of Packed Column on Stripping GE GE can be stripped from the oil, but…. The designed column (Fig. 16) provides short resident times at high(er) temperatures and gives (a) almost no • Under normal deodorizing conditions - formation formation of GE, even at T > 240°C and (b) very efficient of GE > stripping (Fig. 15) FFA stipping but only limited heat bleaching. • Stripping can only be significant at higher Essentially, dual temperature high-temp fast stripping/ temperature and lower pressure low-temp mild deodorization achieved. • Best strategy therefore to limit formation (temp. < 240°C) • Best compromise: FFA strip at high temperature, Final Treatment of RBPO deodorise at low temperature A dual temperature – dual pressure system allows optional low pressure prestripping and post-stripping (Fig. 17). 10 min, 0.5% SS ≠ GE ≠ FFA 0.1 ppm 0.08% Figure 16. Effect of packed column: fast GE stripping and mild deodorization 78 Malaysian Oil Science and Technology 2018 Vol. 27 No. 2
REFINING CRUDE PALM OIL: CURRENT STATUS AND LATEST DEVELOPMENT TO ENSURE HIGH FOOD OIL QUALITY AND SAFETY Intermediate cooling + Qualistock dual temp deodorising Figure 17. Dual temperature-dual pressure GE stripping and deodorisation 5. Optimised Physical Refining: CPO Washing, Bleaching Optimized physical refining: 15 min/245°C followed by with NBE and Dual Temp Deodorisation 45 min/230°C Experiments conducted according to the given 3-MCPDE: standard PR with ABE > standard PR with conditions provide data presented in Table 3. NBE = optimized PR > chemical refining Standard physical refining : 60 min/260°C/3mbar. GE: standard PR with ABE = standard PR with NBE > Chemical refining: 120 min/225°C/3 mbar optimized PR = Chemical refining Table 3. Comparison of refining methods and optimisations Crude Standard PHYSICAL Standard PHYSICAL CHEMICAL Optimized Parameter Palm refining refining refining PHYSICAL refining Oil Activated BE Natural BE Natural BE Natural BE 1% 1% 1% 1% FFA (% C16:0) 5.83 0.02 0.017 0.013 0.02 Color (Lovibond 5 ¼ “) N.A. 1.8R/23Y 2.0R/24Y 2.3R/19Y 2.5R/32Y Total chlorine (ppm) 5.0 N.A. N.A. N.A. N.A. 3-MCPDE (ppm) - 4.21 → 1.25 → 0.48 → 1.18 Glycidyl esters (ppm) 3.12 → 2.94 → 0.48 → 0.55 Malaysian Oil Science and Technology 2018 Vol. 27 No. 2 79
REFINING CRUDE PALM OIL: CURRENT STATUS AND LATEST DEVELOPMENT TO ENSURE HIGH FOOD OIL QUALITY AND SAFETY 6. Post Bleaching: A Solution to GE Reduction and reliable at low pressures. Final treatment of RBPO is becoming a key standard feature for new refineries. Post-bleaching : Non HCl Activated BE, 105°C, 50 mbar. No post-deodorisation. Results are given in Fig. 18. 0.5% ABE gives very fast and almost complete GE Post-Stripping of GE from RB palm oil degradation: GE < 0.1 ppm within 10 min Top pressure packed column at 1.5 mbar using Dry 0.2% ABE gives slower but still good GE degradation: condensing Sublimax 2G GE < 0.2 ppm within 30 min The results of GE stripping at different temperatures are charted in Fig. 20 7. Mild Post Refining of RBPO GE Post-stripping will not only reduce GE, but may also create additional losses as other components will Post-bleaching conditions: 0.5% Activated BE, 110°C, also be stripped (Tocotrienols, MAG, …) 30 min. Post-deodorization: 0.5% stripping steam, 3 mbar, 60 min. RBD PO GE can be eliminated by post-refining, but mild 4.3 conditions are to be used as GE can be formed (Fig. 18). 2.8 3-MCPDE + GE (ppm) Redeodorized at 260°C GE may again be formed during post-deodorization so that low deodorization temperature is required. 0.3 Redeodorized MCPDE are more difficult to remove during 0.1 at 230°C Post-bleached post-refining. Equipment for the final processing of RBPO is illustrated Sample number in Fig. 19 operating a 1 mbar. This is considered safe Figure 18. Removal of GE by post-refining Figure 19. Equipment for RBPO final treatment 80 Malaysian Oil Science and Technology 2018 Vol. 27 No. 2
REFINING CRUDE PALM OIL: CURRENT STATUS AND LATEST DEVELOPMENT TO ENSURE HIGH FOOD OIL QUALITY AND SAFETY Chemical refining and good quality CPO can provide low levels of 3-MCPDE and GE (< 0.5 ppm). There is Glycidol (ppm) 200°C a need to account for the enrichment of these trace 230°C 210°C contaminants in the oleins on fractionation. 260°C Sparge steam (kg/ton) CPO Quality: Key Determining Factor in Mitigation of 3-MCPDE & GE Figure 20. Removal of GE optimized Industry has to adopt new best practices to ensure highest CPO quality for food safety. There is a clear Palm Oil Physical Refining: Steps to Mitigate 3-MCPDE need for segregation of good & excellent quality for & GE food versus the rest for non-food uses (Fig. 21). The A summary is given diagrammatically and tabulated palm oil industry can provide excellent quality food oil below. (70%) with FFA < 3.5% and DOBI > 2.5 which is sufficient for the PO used in foods, so where is the problem? Dual bleaching with Dual temp Stripping- CPO wet pretreatment NBE/ABE deodorization Q Mitigate 3-MCPDE Mitigate 3-MCPDE Mitigate GE RBDPO: PORAM spec Industry FFA (%palmitic acid): 0.1% max 0.03-0.05% max M&I: 0.1% max 0.01-0.05% max Colour (5.25” Lovibond cell): 3 red max 1.5-2.5 red max M.Pt (AOCS Cc 3-25): 33-39°C (ns) IV (Wijs): 50-55 (50.5-52.5) PV: (ns) nil Taste: (ns) bland P: (ns) 1-3 ppm max 3-MCPDE 2.5 ppm max* GE 1 ppm max* personal care oleochemicals food Objective parameters DOBI > 2.5? FFA < 3.5? biodiesel Chloride < 2 ppm ? infant food Palm Oil Figure 21. Palm oil quality for food and non-food uses Feedstock Good quality CPO Good quality Poor quality CPO Premium quality not washed CPO washed Not washed CPO, Not washed FFA % (16:0) 3.4 6.7 1.3 DOBI 2.6 1.7 3.4 Refining Physical Physical Physical Physical Physical Physical refining refining refining refining refining refining FFA % 0.04 0.04 0.06 0.02 0.03 0.02 Colour lovibond (51/4) 2.0R/51Y 2.2R/57Y 6.0R/70Y 2.4R/16Y 1.2R/28Y 0.7R/16Y 3-MCPDE ppm 1.21 0.34 2.78 1.76 0.46 0.08 2-MCPDE ppm 0.66 0.21 1.31 0.05 0.25 0.05 GE ppm 0.40 0.42 0.59 0.24 0.27 0.24 Figure 22. CPO quality: refining for food quality and safety Malaysian Oil Science and Technology 2018 Vol. 27 No. 2 81
REFINING CRUDE PALM OIL: CURRENT STATUS AND LATEST DEVELOPMENT TO ENSURE HIGH FOOD OIL QUALITY AND SAFETY Quality and Origin of CPO (3) Technology development, finding the right balance between efficiency, quality & sustainability For a long time it is known that quality does matter as regards to the CPO and the levels of trace process Various mitigation solutions (preventive and contaminants. The tabulated results below confirms curative) have been developed, some already this point again. Good quality CPO is the key for low applied, others still under investigation, taking 3-MCPDE formation. GE can be managed during into account COST factor (CAPEX & OPEX), as the refining by prevention or correction. final refined food oil must remain affordable. Abbreviations. ABE = activated BE; BE = bleaching earth; CSR = CPO Quality: New Commercial Standard For Food Oil corporate social responsibility; CSPO = Certified Sustainable Palm Oil; CSV = creating shared value; DAG = DG or diacylglycerol; DHA = docosohexaenoic acid; EFSA = European Food Safety Authority; In view of the new demands for edible oils quality ENGO = environmental NGO; EPA = eicosopentaenoic acid; EU with respect to trace process contaminants, standards = European Union; FA = fatty acid; FEDIOL = Federation of the for palm oil quality may need to be reviewed. Figs. European Vegetable Oil and Proteinmeal Industry; FELDA = Federal Land Development Authority of Malaysia; FFA = free fatty acid; 22 & 23 illustrate the main parameters that may be FFB = fresh fruit bunches; Fob = free on board (responsibility for useful to set guidelines for CPO quality for food. goods until leaving a specified point); GE = glycidyl ester; GM = genetically modified; GMO = genetically modified organism; Ha = High quality CPO for food can be selected from the hectare; IARC = International Agency for Research on Cancer; LOD palm oil mill. As good practices, low quality oils (e.g. = limit of detection; MAG = monoacylglycerol or monoglyceride; MCPD = monochloropropandiol; MCPDE = MCPD esters; Mln, mln = sludge, condensate and FFB oils) in milling must not be million; MPOA = Malaysian Palm Oil Association; MPOB =Malaysian recycled to the food quality CPO. Reserve low quality Palm Oil Board; MPOC = Malaysian Palm Oil Council; MUFA = monounsaturated fatty acid; NBE = natural bleaching earth; NGO = CPO for oleochemicals and other non-food uses or non-government organization; NO = non- odoriferous; OFIC = Oils process bad quality CPO into biodiesel (Fig. 21). and Fats International Congress organized regularly every two years by MOSTA; P = phosphorus or pressure; PAHs = polycyclic aromatic hydrocarbons; PCBs = polychlorinated biphenyls; PFAD = palm fatty distillate; PO = palm oil; POPs = persistent organic pollutants; ppb = Conclusion parts per billion; ppm = parts per million; ppt = parts per trillion; PR = physical refining; PUFA = polyunsaturated fatty acid; R = red; RBDPO There is no “one size fit all” in 3-MCPDE & GE mitigation = refined, bleached and deodorized PO; RSO = rapeseed oil; RSPO = Round Table on Sustainable Palm Oil; SAFA = saturated fatty acid; SBO solutions. Best solution depends on: = soybean oil; T = tonne, also temperature; TFA = trans fatty acid; Y = (1) Plant configuration: chemical or physical, new or yellow; Yr = year existing plant (2) Required specs: special vs commodity; individual or formulated fat Max 5% FFA Max 3.5% M&I DOBI (moisture & CPO Quality (Deterioration of Impurities) Bleachability Index) Max 0.25% Min 2.3% Max 5% Chloride (after washing) Min 2.5% Max 2 ppm Figure 23. Guidelines for food-quality palm oil 82 Malaysian Oil Science and Technology 2018 Vol. 27 No. 2
Developing Innovative Technologies for Palm Oil Milling: Challenging - Enriching - Profitable Journeys KH Lee IHMS & MOSTA [Presented at the Palm Oil Milling Workshop, 14th Aug 2018, Johor Bahru, Malaysia] Introduction Oil palm plantations have been around for 101 years and extraction of fruit oil has been following closely the increasing fruit harvest for the last century. The oil palm fruit is unique in having heavy bunches which need to be sterilized to stop enzymatic action, cooked to release the fruits from the bunches, have the fruits separated and screw-pressed for the mesocarp oil and kernels and the pressed oil separated, pumped dried and stored. While conceptually simple, the engineering and technologies have to be designed and adapted for this unique oil and the successful development Figure 1. Tan Sri Ong of MOSTA and Calvin Ho of Ladang TaiTak agreed to collaborate to hold a milling workshop to commercial plants spanned over half a century. for the Malaysian palm oil industry While many would have thought that milling has not made much of advances for decades, it is surprising from indigenous technologies to be adapted uniquely that many incremental improvements have been for the oil palm crop. Further downstream processing happening among the mills of the major corporate technologies provide a versatile range of fats and oil plantation companies. The present revelation oils ranging from nutritious liquid oils, semi-solid fats comes from the MOSTA workshop on milling held and solid fats demanded by the needs of the variety in August 2018 in collaboration with Ladang TaiTak of foods and cuisines around the world. Processing (Fig. 1), which is a follow-up from the MOSTA workshop for specialty fats, infant formulas, functional foods, on Agronomics held a year earlier in Ipoh. fat-soluble vitamins and medicinal supplements have The farm-to-fork quality of vegoils from the oil palm been made available. that are supplied to world consumers is remarkable in that the technologies in the multiple steps of the The Start of the Innovation Journey for the Palm Oil Mill supply chain has been developed in the third world The earlier developments by MARDI and PORIM have countries of SE Asia. Best practices begin with the provided the basic framework for commercial palm oil plantations producing 4 to 6 tonnes of palm fruit oil per mills with engineering technologies for sterilization of hectare sustainably with MSPO and RSPO standards; fruit bunches, separation of fruits from empty bunches, such yields far exceed all the other oil crops. The pressing out of mesocarp oil, recovery of kernels and extractions of palm oil and kernel oils have evolved separation of oil from effluent water. For decades the Malaysian Oil Science and Technology 2018 Vol. 27 No. 2 83
DEVELOPING INNOVATIVE TECHNOLOGIES FOR PALM OIL MILLING: CHALLENGING - ENRICHING - PROFITABLE JOURNEYS Figure 2. Pioneering engineers and supporting staff at Riverside Palm Oil Mill (1971) basic milling technology remained without advances or she probably just stands aside and comments although there were attempts to introduce more from afar. automation. In 1971 young engineers shown in Fig. 2 and elsewhere embarked on a journey of innovation Mill Engineers Stand to create more efficient milling using technologies as they become available. • Mills must not piggy back claim on any pride in any achieved higher palm product extractions on The vision to develop innovative technologies is FFB arising from better planting material or field important and led by many and this paper has practices. highlighted the wide expertise of the Executive Director of IHMS Sdn Bhd. • They can only be proud in their use of GOOD Milling Practices & Technology in achieving lowest possible milling loss, irrespective of any outcome values in Innovative Developing Technologies extractions on FFB. After all, milling does not add in It is recognized that many of these are already any extra quantity of palm products and can only around and available in the market place; but what is optimize recoveries (lower Milling Loss). still lacking: • In any instances, whenever perceptions of poor • Successful uses in milling are few possibly due to milling arise, do bring in competent, independent lack of the following: and professional Milling Auditors who can provide not only the Whys and the Whats but also the Hows. i. Inability to synergize with the current milling Avoid any ‘YES Sirs’ auditors boosting their own egos operation and know-how and/or with business wise focus supporting pre-biased ii. No clarity to define performance expectations to top management perceptions. mill owners except financial gain promises and guarantee of $$$ returns Successful Technology Selection and Use iii. In-Correct and In-Efficient ideas may unexpectedly lead to incorrect and inefficient • Technology has to be verifiable based on science & uses engineering iv. Most mill managers and engineers have • Developing New Technology – In Stages • proof of their hands full from ever administrative and concept g pilot trials g comparative runs g use environmental regulations, demands and • Use of Proven Developing Technology: • Non-sense compliances added on to their high workload to conduct further re-evaluation tests WITHOUT for optimize milling cost, higher food quality sizeable comparative tests and proper certified demands and lower milling palm product loss, & qualified team participation; • Need to identify They are understandingly unable to participate shortfalls for corrections as no two Mills are built to and contribute productively; at best or worse he the same design flow system and capacity. 84 Malaysian Oil Science and Technology 2018 Vol. 27 No. 2
DEVELOPING INNOVATIVE TECHNOLOGIES FOR PALM OIL MILLING: CHALLENGING - ENRICHING - PROFITABLE JOURNEYS Resource Support Brief on Tai Tak Palm Oil Mill • Hands-on Participation inputs WILL assure any • It is a very OLD Mill, 50 Loving Milling Years; built in Technology Input success Y1968 • Patience & Confidence needed from Mill Owners - • Free flow of finger food and drinks at reception clear understanding of any needed extended times to • Productive & smart blending of YOUNGIES & OLDIES SUCCEED • Mill IMAP Advisors (5 persons) totaling 240 MILLING • Team players (Providers – Participators – Users) YEARS milling experience having win-win-win interests (monetary, right of use, recognition, satisfaction), WILL bring out effective • WILLING to share Milling Practices & Technology values to enhance and make good any shortcoming in • Proud but not prideful or boastful the use of technology. Tai Tak Palm Oil Mill Open Day on 14th August 2018 further Technology Development Project Management reinforced both Tai Tak and IHMS’s intention and commitment Manage and Motivate to place their developed and developing Innovative Technology in the PUBLIC DOMAIN as Open Source. • Manage the team and activities in communicating, supporting, and helping with decisions. The Visit focused on the following: • Inexperienced members of the team prefer clear 1. Mechanized Sterilization Indexer System – Y2003 instructions, but these on the contrary can de- 2. Oil Room Discharge / Mill Waste Separation – Y2018 motivate experienced and creative people 3. Auto Sterilization / Safe Use – Y2003 • Manage these people by the results they get 4. Saturated Steam for Sterilizing – Y2018 5. Megasonic (Ultrasound) – Oil Capture – Y2010 • Share plaudits with your team, but never, never accept plaudits yourself 6. Non-Oil Screen Waste Removal (Puree) – Y2015 7. Sterilized Detached Fruits Storage (SDF) – Y2010 • Never ‘dump’ blames on anyone in your team. As project manager any problem is always ultimately 8. Pre- Recovery of Pressed Oil (PRS) – Y2013 down to you anyway. 9. Quality & Loss Control Lab (NIR) – Y2011 10. Boiler Flue Gas Pre-Scrubber (BGSS) – Y2017 / ESP Check, Measure, Monitor, Review Project Progress Scrubber Use by Y2019 11. Condensing Turbine for Low Use of Power Steam – • Check the progress of activities against the plan. Y2014 • Review performance regularly and at the stipulated 12. H.P. to L.P. Steam – Process Steam – Y2014 - Y2018 review points, and confirm the validity and relevance 13. 13 Boiler (Biomass) Fuel Feed System – Y2016 of the remainder of the plan. 14. Separate Oil Traps – Oil Station/Milling Waste – • Adjust the plan if necessary, in light of performance, Y2018 changing circumstances, and new information, 15. Biogas Extraction (CUBRA). For Heat Energy Plant – but remain on track and within the original terms Y2017 of reference. 16. Low Collectable Oil ETP/Enzyme Assisted – Y2013 • Identify, agree and delegate appropriate new 17. Launching IMAP Center (240 Milling Years’ actions. Experience) – (Advisors in place Since Y2003) 18. INTER-ACT Center (Milling Participators) Malaysian Oil Science and Technology 2018 Vol. 27 No. 2 85
DEVELOPING INNOVATIVE TECHNOLOGIES FOR PALM OIL MILLING: CHALLENGING - ENRICHING - PROFITABLE JOURNEYS Figure 3. Workshop sharing interactions: challenges in the use of innovative developing technologies Sterilization and Cooking of Fruits stage provide an efficient way to remove chloride impurity which will be the cause of trace processed Palm fruit bunches harvested from plantations arrive contaminants (MCPDE). While high temperatures at the oil extraction mill and they need to be sterilized are useful, saturated steam temperature of
DEVELOPING INNOVATIVE TECHNOLOGIES FOR PALM OIL MILLING: CHALLENGING - ENRICHING - PROFITABLE JOURNEYS • A DEFINITE VALUABLE SYSTEM TOOL minimizing Sterilizer Condensate Oil Loss The installation of the Sterilizer Indexer System was fully participated by the owner (Fig. 4). As this system is the first of its kind in the world, the technology team (needed be “fearless and righteous”) was blessed. The steadfast step by step approach to successful use re-established confidence from “God help you” doubters. Figure 6. Manual loading of fruits into old B4 sterilizer cages The old B4 sterilizer cages involved a lot of manual labour in charging and moving the cages with much leakages and fruit losses causing greasiness and litter (Figs. 5 and 6). Tai Tak Palm Oil Mill: Megasonic Journey Ultrasonics have been used in science and industry Figure 4. Installation of the semi-automatic Sterilizer for heating, cleaning, cellular disruption, cavitation Indexer System catalysis and recently investigated by CSIRO for milk fat emulsification or agglomerating milk fat particles. It was a challenge to the palm oil industry which faces separation problems of oil micro-emulsions during milling and this technology was made known to MPOB in 2010 (Fig. 7). Tai Tak Palm Oil Mill took up the development of this Technology Intense discussions were carried out at Tai Tak Mill (Fig. 8) in Sept 2010 and by Oct decision based on the proof of concept was A GO (Fig. 9), followed by planning and intense work (Figs. 10 & 11). Figure 5. Milling in the old system of sterilizer cages with fruits shunting continue without Mill Shutdown Figure 7. PAC meeting of MPOB in April 2010 (Dr YM Choo of MPOB, front row, 8th from right; Tan Sri SH Ong, front row, 7th from right; CSIRO’s Mary Ann Augustin, 3rd row, 3rd from left; Ir KH Lee of IHMS, last row, 2nd from left; Dr PT Gee, 3rd row, 3rd from right) Malaysian Oil Science and Technology 2018 Vol. 27 No. 2 87
DEVELOPING INNOVATIVE TECHNOLOGIES FOR PALM OIL MILLING: CHALLENGING - ENRICHING - PROFITABLE JOURNEYS Figure 8. Intense discussions on engineering aspects of the project Figure 9. Decision to go ahead at the mill for proof of concept in Oct 2010 Figure 10. Planning and aspects of work in progress Figure 11. By 18th Sept 2012 it was demo day and celebration 88 Malaysian Oil Science and Technology 2018 Vol. 27 No. 2
DEVELOPING INNOVATIVE TECHNOLOGIES FOR PALM OIL MILLING: CHALLENGING - ENRICHING - PROFITABLE JOURNEYS Figure 12. AOCS Corporate Achievement Award in 2013 Achievements with Megasonic samples, analyses and measurements since Nov 2013 to confidently claim: Megasonic reduces oil loss consistently to 2.5 kg/T FFB and there is zero run-away oil loss. Rapid oil separation i. The low oil loss in sludge centrifuge discharges provides better oil quality. POME discharge is lower. achieved at 2.3-2.99 kg/T FFB The most rewarding moment comes from the AOCS ii. The extra collectable oil from sludge centrifuge Corporate Achievement Award in April 2013 (Fig. 12). returns another 2.00-3.00 kg/T FFB Tai Tak mill is never ‘rich’ on OERs and over the years, Use of Megasonic in Palm Oil Mills process yearly some 100,000 T FFB - own FFB of old- It is not one size that fits all. It is advisable to audit your age palms and substantial 100,000 T FFB from Traders own mills and establish the need for this Megasonic to maintain processing continuity and acceptable tool. milling costs for her 45 TPH FFB plant. In comparison to previous data with no Megasonic Key Issues Best Answered by the Mill: intervention in months of Nov 2012 – Oct 2013 to • Are there frequent oil clarifier upsets requiring current months of Nov 2013 – Oct 2014 with Megasonic discharges or complete empty-outs? intervention, the mill had an increase of 0.56% oil extraction rate of FFB and on 211,449 T FFB processed, • Are there frequent high collectable oils in the mill’s translating to some higher earnings gain of RM2.9 sludge pits or de-oiling tank? million. And to cream the top, Kai Tak mill had the • Is there high oil in the ETP acidification ponds? highest OER achievement in Y2014 in comparison to previous 30 years since Y1984. • Is there poor ripeness of FFB? Megasonic intervention assists in: Achievements of Tai Tak Mill i. Dislodging oil droplets trapped in the suspended and dissolved non-oil solids. At Tai Tak mill we had complete mass balance and analytical data for 277 run days covering 15,000 ii. Agglomerating emulsified and tiny oil droplets from sludge centrifuge returns. Malaysian Oil Science and Technology 2018 Vol. 27 No. 2 89
DEVELOPING INNOVATIVE TECHNOLOGIES FOR PALM OIL MILLING: CHALLENGING - ENRICHING - PROFITABLE JOURNEYS iii. Agglomerating emulsified oil from the pressed crude oil; all these coalesced into bigger droplets which are then collectable in the oil clarifier tank. Food for Thought • Low oil at the centrifuge discharge is not good enough • Recoverable centrifuge oil still has to be totally converted into collectable oil. Quality & Loss Laboratory: Introduction of Near Infrared (NIR) Spectrometer Classical laboratory although with standard procedures takes too long for plant operations correction. The NIR spectrometer can also now analyse for many other critical chemical parameters. This was installed and tested during the period of July – Nov 2011 (Fig. 13). Figure 14. Replacing the old turbines (1968-1998) with new ones (1999-2012) More Power - Less Steam Consumption with Lower Biomass Boiler Fuel Use The multistage condensing steam turbine generates power at 90KWe/T FFB. Boiler provides process steam consumption of 350kg/T FFB and lower. • Operational skills were acquired in early 2013 to run independent steam for power and process. Figure 13. NIR spectrometer monitors quality and oil loss • Installed process steam supply systems were for 350 kg/T FFB Condensing Turbine • Improved sterilizing steam supply and use without The next continuing project is a smart partnership sacrificing cooking efficiency & throughput to power with renewable energy from conversion of • Improved boiler super heater design and biomass waste to reduce GHG emissions and power installation, had continuous monitoring of superheat other down-stream activities. This looks at updating temperature and improve proper start-up and shut- the steam turbine which was developed in the early down procedures years (1880s) whereby steam was expanded in piston engines (Fig. 14). The vertical motion was then • Condensing (3 stage) turbine installed in Sept 2013 converted to rotary motion to generate power. In 1884 • The steam boiler and steam turbine stations run well Charles Parsons developed the first practical, modern since Mar 2014 high-speed steam turbine. The single stage back- pressure turbines for integrated supply of steam for power and process in Tai Tak mill (1999-2012). 90 Malaysian Oil Science and Technology 2018 Vol. 27 No. 2
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