Production Of Palm Oil And Effect Of Heat On It
Table Of Contents
Chapter ONE
INTRODUCTION
- 1.1Introduction
- 1.2Background of Study
- 1.3Problem Statement
- 1.4Objective of Study
- 1.5Limitation of Study
- 1.6Scope of Study
- 1.7Significance of Study
- 1.8Structure of the Research
- 1.9Definition of Terms
Chapter TWO
LITERATURE REVIEW
- 2.1Overview of Palm Oil Production
- 2.2Historical Perspectives on Palm Oil
- 2.3Palm Oil Processing Methods
- 2.4Palm Oil Composition and Properties
- 2.5Economic Importance of Palm Oil
- 2.6Environmental Impact of Palm Oil Production
- 2.7Global Palm Oil Market Trends
- 2.8Health Benefits and Concerns of Palm Oil Consumption
- 2.9Palm Oil Certification and Sustainable Practices
- 2.10Future Prospects of Palm Oil Industry
Chapter THREE
RESEARCH METHODOLOGY
- 3.1Research Design and Strategy
- 3.2Data Collection Methods
- 3.3Sampling Techniques
- 3.4Data Analysis Tools
- 3.5Research Ethics and Considerations
- 3.6Case Study Selection
- 3.7Questionnaire Design
- 3.8Data Validation Techniques
Chapter FOUR
DATA PRESENTATION AND ANALYSIS
- 4.1Overview of Research Findings
- 4.2Analysis of Data Collected
- 4.3Comparison with Existing Literature
- 4.4Interpretation of Results
- 4.5Discussion on Key Findings
- 4.6Implications of Findings
- 4.7Recommendations for Future Research
- 4.8Practical Applications of Study Results
Chapter FIVE
SUMMARY, CONCLUSION AND RECOMMENDATIONS
- 5.1Summary of Research
- 5.2Conclusions Drawn
- 5.3Contributions to Knowledge
- 5.4Research Limitations and Future Directions
- 5.5Practical Implications
- 5.6Recommendations for Stakeholders
- 5.7Reflection on Research Process
- 5.8Conclusion Remarks
Project Abstract
The abstract is as follows Palm oil is one of the most widely used vegetable oils globally, finding applications in various industries such as food, cosmetics, and biofuels. The production of palm oil involves several stages, including fruit harvesting, sterilization, threshing, digestion, oil extraction, and clarification. Heat is a critical element in the processing of palm oil, as it is used in multiple stages to facilitate the extraction of oil from the fruit bunches. The effect of heat on palm oil can significantly impact its quality, nutritional composition, and shelf life. During the sterilization process, steam is applied to the fruit bunches to deactivate enzymes and loosen the fruits from the bunches, allowing for easier oil extraction. The heat applied during sterilization can affect the chemical composition of the oil by altering the fatty acid profile and reducing the moisture content. Excessive heat or prolonged heating can lead to the degradation of important nutrients and antioxidants in the oil, diminishing its nutritional value. Threshing and digestion are subsequent stages in palm oil production that also utilize heat to separate the oil-bearing mesocarp from the fruits and break down the oil-containing cells to release the oil. The temperatures used in these processes must be carefully controlled to ensure optimal oil extraction efficiency while preserving the quality of the oil. High temperatures can accelerate oxidation reactions in the oil, leading to rancidity and off-flavors. The clarification stage involves heating the extracted crude oil to remove impurities and moisture, further refining the oil for various applications. Heat treatment during clarification can improve the oil's clarity and stability by separating out solids and water, but excessive heat can also cause thermal degradation of the oil, leading to color changes and flavor alterations. In conclusion, heat plays a crucial role in the production of palm oil, affecting its quality attributes and nutritional value. Proper control of temperatures throughout the processing stages is essential to ensure high-quality oil with desirable characteristics. Understanding the effects of heat on palm oil can help optimize processing conditions to maintain the nutritional integrity and functionality of the oil for different applications.
Project Overview
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<b>1.1 INTRODUCTION</b></p><p><b>1.0 BACKGROUND STUDY </b></p><p>Palm oil is an edible oil derived from the fruits of the oil palm Elaeis guineensis (Siew,
2002). Palm olein is one of the major palm oil products that domestically and industrially
used as cooking/frying oil. The functions of frying oils are to transfer heat to cook foods
and to produce characteristics of fried-food flavor.
The major advantage of palm olein is its high stability during frying that produced
minimum amount of breakdown products in an acceptable level. Study conducted by Azmil
and Siew (2008) shows that palm oil, single-fractionated palm olein and doublefractionated palm olein were more stable than high oleic sunflower oil after 80 hours of
heating at 180 °C. These palm products also produced lower amount of free fatty acids,
polar and polymer compounds, as well as preserved higher smoke points and tocols content.
However, palm olein tends to crystallize at low temperature that limits its usage in
temperate countries.
In spite of various nutritional studies, palm olein is not well considered as a recommended
choice due to its higher saturation content. Against this factor, there is a need to reduce its
saturation content, so as to enhance its versatility in applications for market penetration in
cold countries as well as cater to market trends. Generally, the saturation content of palm
olein can be reduced by multistage fractionation of palm olein. However removal of
saturation in palm olein is difficult due to the difficulty in controlling the crystallization of
palm olein (Gijs et al., 2007a). Other than that, blending palm olein with other soft
vegetable oils such as canola oil, cottonseed oil, rice bran oil, sunflower oil, soybean oil etc
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is implemented to reduce the saturation level of palm olein and for frying purposes in
temperate countries (Razali and NorΓ’β¬ΕΈaini, 1994). In fact, blending of palm olein may also
enhance the stability and frying performance of the oil.
In this study, palm olein is modified by enzymatic interesterification and dry fractionation
to reduce the saturation content of the oil. Enzymatic interesterification enables interchange
of acyl groups between and within triacylglycerols (TAGs) at specific positions to form
new TAG species that have high melting TAGs, PPP and PPS. These saturated TAGs that
causes the crystallization of palm olein, can be removed as stearin during fractionation.
Two sn-1,3 specific immobilized lipases; Lipozyme® TL IM (Thermomyces Lanuginosa)
and Lipozyme® RM IM (Rhizomucor Miehei) are selected as biocatalysts for
interesterification in solvent-free system (Appendix A and B). Palm olein has been chosen
as the feedstock due to its higher unsaturation content compared to palm oil. Two types of
new palm oil products can be derived from this study; the low saturation palm liquid oils
and the respective stearin fractions.
1.2 The Objectives of the Studies
The main objective of the studies was to prepare pure palm-based products with low
saturation, via enzymatic interesterification of palm olein with iodine value (IV) of 62
follow by dry fractionation, as well as to characterize the physicochemical properties of the
products. Besides, the efficiency of the lipases; Rhizomucor Miehei (Lipozyme® RM IM)
and Thermomyces Lanuginosa (Lipozyme® TL IM) in the interesterification reaction will
also be looked into. Optimization of the interesterification reactions and dry fractionation
will also be carried out.
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1.3 Chemical Properties of Palm Oil
Palm oil consists of mostly glyceridic materials with some non-glyceridic materials in trace
amount (Chong, 1994). TAG is the most abundant glyceridic component in palm oil which
comprises of triesters of high aliphatic acids or fatty acids, while monoacylglycerol (MAG)
and diacylglycerol (DAG) are the minor glyceridic components in palm oil. The chemical
structures of partial acylglycerols (MAG and DAG) and TAG were shown in Figure 1.1.
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TAGs are esters formed from glycerol acylation of three fatty chains, while acylation with
one or two fatty chains formed partial acylglycerols (MAG and DAG). The hydrocarbon
chains in the ester group, R could be varied in terms of carbon number and the chemical
structure (bend structures for unsaturated fatty acids) (Chong, 1994). The physicochemical
properties of the oil could be due to the types of fatty acid presence, and the manner in
which fatty acids combine to form various TAG molecules (Naudet, 1996). In general, the
hydrophobic nature of oil is due to the long fatty acid chains in the glyceridic materials.
2-monoacylglycerol (β) 1-monoacylglycerol (α) 3-monoacylglycerol (α’)
1,3-diacylglycerol 1,2-diacylglycerol 2,3-diacylglycerol Triacylglycerol
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The Fatty Acids Composition of Palm Oil
For palm oil, the fatty acids composition falls within a very narrow range from twelve to
twenty carbon number, with a balanced fatty acids composition between saturation and
unsaturation (Berger, 2001).
Table 1.1 shows the common name, systematic name, shorthand name of fatty acids
presence in palm oil and its fatty acid composition. In most vegetable oils, the sn-2
position fatty acids of TAGs are preferentially occupied by unsaturated fatty acids such as
oleic acid and linoleic acid. Saturated fatty acid (SFA) (e.g. palmitic acid) is found in the
sn-2 position of animal fats TAGs for instance lard, tallow etc (Naudet, 1996). Although
palm oil contains high quantity of SFA, the sn-2 position fatty acids in the TAGs is
preferably occupied by unsaturated fatty acids (mainly oleic acids) (Naudet, 1996; Nor Aini
and Noor Lida, 2005).
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Table 1.1
Common name, Systematic name, Shorthand name of fatty acids in palm oil and its fatty acid
compositions (Sean, 2002; Siew, 2002) </p><p>Common name Systematic name Shorthand FAC</p><p> Lauric Dodecanoic </p><p>12:0 0.1-0.4
Myristic Tetradecanoic 14:0 1.0-1.4
Palmitic Hexadecanoic 16:0 40.9-47.5
Palmitoleic Cis-9-Hexadecenoic 16:1ω7 0-0.4
Stearic Octadecanoic 18:0 3.8-4.8
Arachidic Eicosanoic 20:0 36.4-41.2
Oleic cis-9-Octadecenoic 18:1ω9 9.2-11.6
Linoleic cis-9, cis-12, Octadecadienoic 18:2ω6 0-0.6
Linolenic cis-9, cis-12, cis-15-Octadecatrienoic 18:3ω3 0-0.4
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