Modification of Edible Fats and Oils

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1 Modification of Edible Fats and Oils Namal Senanayake Martek Biosciences Corporation Winchester, Kentucky 40391, USA Fereidoon Shahidi Department of Biochemistry Memorial University of Newfoundland St. John s, NL, A1B 3X9, Canada November 12, 2007

2 Why Modified Lipids? Improves Oxidative Stability Alter the Melting Properties Alter the Crystallization Properties Economic Advantages: Less Expensive Oil More Expensive Oil

3 Modification Methods 1) Hydrogenation 2) Fractionation 3) Interesterification 4) Physical Blending

4 Hydrogenation Treatment of Fats and Oils with Hydrogen A Catalyst and Heat must be present Exothermic Reaction Converts Liquid Oils into Solid or Semi- Solid Products Improves Oxidative Stability Imparts desired Physical Properties (melting point, SFC)

5 Hydrogenation: Principle Catalyst CH = CH + H 2 CH 2 CH 2

6 Possible Reactions during Hydrogenation Complete Saturation: 18:3 18:2 18:1 18:0 Partial Hydrogenation Geometric Isomerization: cis trans Positional Isomerization: cis trans

7 Hydrogenation Hydrogen Oil Deaeration Heating Reaction Catalyst Bleaching Filtration Cooling Termination

8 Hydrogenation: Monitoring the Reaction H 2 Consumption Refractive Index Iodine Value Melting Properties: - Melting Point - SFC

9 Hydrogenation Variables Reaction Temperature Pressure Agitation Catalyst Type Catalyst Concentration Reaction Time

10 Impact of Hydrogenation Variables Increase of: Catalyst Dosage Agitation Speed Temperature Pressure Saturate Formation Decrease Increase Decrease Increase Trans Isomer Formation Increase Decrease Increase Decrease

11 Hydrogenation Conditions Affecting Selectivity Selective Hydrogenation High temperature (170 o C) Low hydrogen pressure ( 1 Atm) High catalyst (0.05% Ni) Selective catalyst Low agitation High trans fatty acids Steep SFC Curve Nonselective Hydrogenation Low temperature (120 o C) High hydrogen pressure ( >3 Atm) Low catalyst (0.02% Ni) Nonselective catalyst High agitation Low trans fatty acids Shallow SFC Curve

12 Hydrogenation: Feedstock Oil Quality Parameter Peroxide value p-anisidine value Free fatty acids Moisture Soaps Phosphorus Specification < 0.5 meq/kg < 10 < 0.05% < 0.05% < 25 ppm < 2 ppm

13 Effect of Hydrogenation on Soybean Oil Composition Fatty Acid (%) 16:0 18:0 18:1 18:2 18:3 RBD oil Partially Hydrogenated and Winterized oil

14 Hydrogenated Oil End Products: Examples Liquid Oils Brush Hydrogenation Margarine Bases Partial Hydrogenation Shortening Bases Partial Hydrogenation Stearin - Total Hydrogenation Coating Fats Partial Hydrogenation

15 Fractionation Separates Fats and Oils into Fractions with different Melting Points Three Major Processes: (a) Dry Fractionation - Gradual cooling of oil w/o solvent - includes winterization and dewaxing (b) Solvent Fractionation - Crystallization performed in diluted solutions - Solvents: Acetone, Hexane & IPA (c) Detergent Fractionation - Addition of detergent solution into crystallized oil - An electrolyte is also added

16 Fractionation Principle Liquid Olein Oil Crystallization Filtration Solid Stearin Crystallization [ SSS-SSU-SUU-UUU ] [ SSS-SSU ] + [ SUU-UUU ] Filtration

17 Fractionated Fats & Oils OIL TYPE REFINING STATE Palm oil Palm kernel oil Soybean oil Cottonseed oil crude / bleached / deodorized crude / bleached / deodorized bleached / deodorized bleached / deodorized Fish oil- Native crude / bleached - Hydrogenated bleached / deodorized Tallow crude Milk fat crude / deodorized

18 Fractionation: Analytical Methods Analytical Technique Solid fat content (SFC) Melting point Cloud point Dropping point Cold test Peroxide value Iodine value (Wijs method) Fatty acid composition (GC) Lovibond color AOCS Method Number Cd 16b-93 Cc 1-25 Cc 6-25 Cc Cc Cd 8-53 Cd 1-25 Ce Cc 13e-92

19 Effect of Fractionation on Palm Oil Composition Chemical Properties Palm Oil Palm Olein Palm Stearin 14:0 (%) :0 (%) :0 (%) :1 (%) :2(%) Iodine Value Melting Point ( o C) SFC (%) at 10 o C

20 Interesterification Rearrange and Randomize the FAs on the Glycerol Molecules Why Interesterify? - Achieve Melting Properties that cannot be achieved by Other Methods - Replace Hydrogenated Fats - Change the Melting Properties

21 Chemical Interesterification: : Principle R 1 R 1 R 1 R 1 R 1 R 1 + R 2 R 2 R 2 Catalyst R 1 R 2 R 1 R 2 R 1 R 1 R 1 R 2 R 2 R 2 R 1 R 2 R 2 R 2 R R2 60 SFC (%) R1 SFC (%) R1, R Temperature (C) Temperature (C)

22 Chemical Interesterification: : Feedstock Oil Quality Parameter Peroxide value Free fatty acids Moisture Phosphorus Specification < 1.0 meq/kg < 0.05% < 0.01% < 5 ppm

23 Chemical Interesterification: : Process Steps 1) Pretreatment of Oil: 120 o C, < 50 mbar H 2 O < 0.01% 2) Catalyst Addition: % 3) Reaction: o C; min; < 50 mbar 4) Catalyst Deactivation: water; organic acid; silicate 5) Centrifugation

24 Interesterification CHEMICAL: - Random - Preferred Catalysts: CH 3 ONa; CH 3 CH 2 ONa ENZYMATIC: - Selective - Lipase-Catalyzed

25 Interesterification: : Process Comparison Chemical Interesterification: Pretreatment of Oil Catalyst: CH 3 ONa Catalyst Deactivation Bleaching Deodorization Enzymatic Interesterification: Pretreatment of Oil Catalyst: Lipase Deodorization

26 Interesterification: : Monitoring the Reaction SFC Melting Point Dropping Point Cloud Point TAG Profile (FT-NIR)

27 Interesterification: : Current Trends Increasing trends to reduce/ eliminate TFA in foods -Legislation USA: FDA labeling ontrans fats January 2006 Europe: max 2% in food fats (Denmark) Major food processors are replacing TFA by low/zero TFA alternatives Increased demand for: Low trans products: < 5% in food fats Zero trans products: < 0.5% in food fats Alternative technology for partial hydrogenation

28 Interesterification: : Product Examples Low/No Trans Margarines and Spreads Low/No Trans Shortenings Cocoa Butter Alternative Fats Reduced Calorie/ No Calorie Fats Milk Fats

29 Physical Blending Easiest and Most Economical Way to Modify Fat Purpose: - Increase Stability - Alter the Color and Flavor - Alter the Melting Properties Blend Two Oils with different Melting Curves to achieve Oil with a Specific Melting Properties Blends can be Calculated using the SFI Value and Linear Algebra

30 Summary Reasons for Modifying Fats & Oils: 1) Alter Physical Properties 2) Improvement of Stability 3) Economical Benefits Modification Methods: 1) Hydrogenation 2) Fractionation 3) Interesterification 4) Blending 5) Combinations of each of the above

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