3.4_Deodorization.ppt

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    Processing of Edible Oil

    (Palm Oil)

    CHAPTER 3

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    3.4 : Deodorization

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    Introduction

    CPB 30303 (JAN 2014)3

    Deodorization is usually the last refining processcarried out to improve the taste, odor, color, and

    stability of the edible oils.

    In commercial deodorization steam strip-ping is

    used to remove undesirable volatile compoundssuch as FFA, aldehydes, ke-tones, and alcohols.

    However, a simultaneous loss of nutritionally

    beneficial bioactive oil components occurs.

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    Introduction

    CPB 30303 (JAN 2014)4

    Complex chemical and physical changes occur inoil composition during deodorization.

    Thermal decomposition of oxidation products and

    pigments, and hydrolysis of conjugated polyenoic

    compounds and TG are some of the chemicalreactions that take place during steam stripping

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    Objectives

    CPB 30303 (JAN 2014)5

    Although the process is commonly nameddeodorization, it is actually a combination of threedifferent effects on the oil:

    (1) stripping: Stripping of volatile components(free fatty acids, odorous compounds,tocopherols, sterols, and contaminants such aspesticides and light polycyclic aromatichydrocarbons, etc.),

    (2) deodorization: Removal of different off-

    flavors, and (3) temperature effect.: Thermal destruction of

    pigments and unwanted side reactions such ascis-trans-isomerization polymerization,

    conjugation, and so on.

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    Deodorization

    CPB 30303 (JAN 2014)6

    Odoriferous compounds are from: Aldehydes

    Ketones

    Others partially eliminated:

    Volatile components such as FFA, alcohol,

    sterols and tocopherol

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    Deodorization

    CPB 30303 (JAN 2014)7

    During deodorization flavor compounds can beformed by hydrolysis and thermal decomposition

    Peroxides are decomposed by heat

    These reactions plays a major role in the flavor

    stability improvement achieved by deodorization ofvegetable oils & fats

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    Deodorization

    CPB 30303 (JAN 2014)8

    High deodorization temperature , air inside thevessel can initiate oxidation with severe

    impairment of taste and flavor stability.

    Residence time and steam volumes significantly

    required compare to normal distillation.

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    Deodorization

    CPB 30303 (JAN 2014)9

    Thermal decomposition with protiens,carbohydrates, phospatides and soap also can

    cause flavor and taste stability

    Deodorization is performed in vacuum because the

    lower partial vapor pressure of the compounds tobe removed.

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    Deodorization

    CPB 30303 (JAN 2014)10

    Consumption of stripping steam increases withdecreasing vapor pressure of the volatile

    components and with the increasing pressure in

    the deodorizer

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    Deodorization

    CPB 30303 (JAN 2014)11

    Optimal stripping parameters (temperature, time,operating pressure, and amount of stripping gas)

    are governed by the properties of the ingoing

    product, the specifications of the outgoing product,

    equipment limitations, and the need to minimizecosts.

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    Deodorization

    CPB 30303 (JAN 2014)12

    Method of operation: Batch

    Continuous

    Semi continuous

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    Deodorization

    CPB 30303 (JAN 2014)13

    Most edible oils and fats can be deodorized attemperatures ranging from 230260 C with

    pressure of

    approx. 23 mbar.

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    Deodorization

    CPB 30303 (JAN 2014)14

    High quality of the deodorized oil due to: excellent efficiency in stripping of high free fatty

    acid contents by utilizing a stripping columnduring continuous processing

    extremely low contamination between differentfeedstock materials during product change insemi-continuous processing mode

    dosing of citric acid to form complexes with theheavy metals in the oil in order to lower theoxidation rate of the deodorized oil

    moderate increase of trans-isomers whendeodorizing at lower temperatures

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    Stripping

    CPB 30303 (JAN 2014)15

    Vapor pressure The volatility of a given component is expressed

    by its vapor pressure, which increases with

    increasing temperature (Figure 2).

    The lower the vapor pressure, the lower thevolatility and, thus, the more difficult to remove

    the component from the oil. For each specific

    component, the vapor pressure-temperature

    relationship can be expressed by the Equation ofAntoine:

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    Stripping

    CPB 30303 (JAN 2014)16

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    Stripping

    CPB 30303 (JAN 2014)17

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    Stripping

    CPB 30303 (JAN 2014)18

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    CPB 30303 (JAN 2014)19

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    CPB 30303 (JAN 2014)20

    Crude Bleached oil Bleached &Deodorized oil

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    Deodorization.

    CPB 30303 (JAN 2014)21

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    Deodorization.

    CPB 30303 (JAN 2014)22

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    CPB 30303 (JAN 2014)23

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    CPB 30303 (JAN 2014)25

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    CPB 30303 (JAN 2014)26

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    For example: Vapor pressure calculation of

    compositions

    CPB 30303 (JAN 2014)27

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    For example:

    CPB 30303 (JAN 2014)28

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    CPB 30303 (JAN 2014)29

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    CPB 30303 (JAN 2014)30

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    CPB 30303 (JAN 2014)31

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    CPB 30303 (JAN 2014)32

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