

NE41102-Topic 5
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•
Science
•
12th Grade
•
Practice Problem
•
Hard
Norazlina Ridhwan
Used 1+ times
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87 Slides • 0 Questions
1
NE41102- Fats and Oil Technology
Semester 1 Session 2023/24
Fats Modification:
Hydrogenation
2
To know the principles and the application of
major technologies and processes in edible
fats and oils production.
3
4
5
6
Hydrogenation process..
•
During hydrogenation, vegetable oils are reacted
with hydrogen gas at about 60ºC.
•
A nickel catalyst is used to speed up the reaction.
•
The double bonds are converted to single bonds in
the reaction. In this way unsaturated fats can be
made into saturated fats – they are hardened.
7
Why Hydrogenation?
• Convert vegetable oils into plastic fat forms
• Two reasons:
1. Change into physical forms with consistency and
handling characteristics required
2. Increase oxidative stability
•
Depends on conditions used, the starting
oils, degree of saturation or isomerization!
8
Hydrogenation Process
• Hydrogenated products = very complex
mixture of simultaneous reactions occur:
– Saturation of double bonds
– cis-/trans-isomerization of double bonds
➢Changes from low-melting cis form to higher melting
trans form
– Shifts of double bond locations
➢Affects melting point
9
10
1. Iodine value – Wij Iodine reach with double bond
where there was direct relation with iodine value and
degree of saturation
2. Bromine water test. Unsaturated vegetable oils
contain double carbon-carbon bonds. These can be
detected using bromine water (just as alkenes can be
detected). Bromine water becomes colourless when
shaken with an unsaturated vegetable oil, but it stays
orange-brown when shaken with a saturated vegetable
fat
Testing of double bond
11
12
• 2 types of unsaturated fatty acid
– cis configuration — "on the same side" in Latin
– trans configuration — "across" in Latin
Substrate for Hydrogenation
13
14
Hydrogenation Process
Hydrogen Gas
+
Nickel Catalyst
160 - 200 0C
Unsaturated and cis-unsaturated
fatty acid
IV of RBD Soya Bean Oil = 125
Double bond
partial
Double bond
trans-unsaturated fatty acid
Single bond
full
Saturated
IV of Hydrogenated Soya Bean Oil = 70
15
Hydrogenation Process
• How?
Unsaturated fatty acids
contain one or more double bonds
[liquid, lower melting point]
Chemically react hydrogen gas with double bond
More saturated fatty acid
Shifting to new position / twisting to trans configuration
[increase melting point]
16
Hydrogenation Process
• How? Three Reactants:
1. Unsaturated oil
2. Catalyst
3. Hydrogen gas
–
Dissolved in liquid oil
17
Hydrogenation Process
• How?
18
Hydrogenation Process
• Operating variables
– Oil, hydrogen, catalyst
– sufficient supplied of
hydrogen will increase
reaction rate > trans-
isomer decrease, flatter
SFI curve
19
Hydrogenation Process
• Operating variables
– any condition affects the catalyst surface or
controls the supply of gas to catalyst surface ~
1. Temperature
•
Rate
•
Solubility of hydrogen gas
•
Selectivity
•
Fatty acid configuration
20
Hydrogenation Process
• Operating variables
2. Hydrogen Pressure
•
Availability of hydrogen gas
•
Selectivity
•
Fatty acid configuration
21
Hydrogenation Process
• Operating variables
3. Agitation
•
Solubility of hydrogen gas
•
Selectivity
•
Fatty acid configuration
22
Hydrogenation Process
• Operating variables
4. Catalyst
o
Level / concentration
➢
Rate
o
Type
➢
Nickel, sulfur-poisoned/treated catalyst, copper
chromite catalysts, precious metals (palladium)
o
Poisons (from refined oils and hydrogen gas)
➢
Sulfur, phosphorus, water, FFA
o
Reuse
23
How the catalyst work…
24
Hydrogenation Process
• Operating variables
5. Source oils
•
Type of unsaturated fatty acids
•
Number of unsaturated fatty acid per triacylglyceride
Fatty Acid
Relative Reactivity
C-18:3 Linolenic
40
C-18:2 Linoleic
20
C-18:1 Oleic
1
25
Hydrogenation Process
• Systems
– Batch (simplicity, flexibility)
• Two different designs
1.
Recirculation
»
Filled with hydrogen under pressure in
recirculation system
2.
Dead-end
»
Hydrogen is added and vented when endpoint
reached
»
Safer, more versatile, lesser oxidation and
hydrolysis
26
Recirculation System
The reaction mixture (oil, H2
and catalyst) is continuously
re-circulated by an external
pump through an external
heat exchanger and a venturi
jet that is located inside the
autoclave, where fresh H2 is
added (see figure 2). These
reactors are generally
referred to as ‘loop-reactors’
27
Dead-end System
28
Hydrogenation Process
• Systems
– Continuous
•
Limited, due to variety of products to be
hydrogenated
29
Hydrogenation Process
• Control / endpoint?
– SFI
– IV
– Refractive Index
– Melting point
– Quick titer (refractometer)
30
Hydrogenation
• Product modification
– Softness, plasticity, organoleptic
– More selective hydrogenation process with higher
temperature, lower hydrogen pressure, lower
hydrogen gas solubility, higher catalyst selectivity
➢Product with steeper SFI (more trans- formed)
31
Hydrogenation
• Product modification
– Less selective hydrogenation process with lower
temperature, higher pressure, lower catalyst
selectivity level
➢Product with flatter SFI (less trans- formed)
32
Source: http://blog.fooducate.com/tag/hydrogenation/
33
34
35
36
37
38
Hydrogenated Fats Consumption
Source: http://www.purplemedicalblog.com/2005/12/what-trans-fat-labels-meanread-them.html
Major Food Sources of Trans Fat for American Adults
(Average Daily Trans Fat Intake is 5.8 Grams or 2.6 Percent of Calories)
39
Hydrogenated Fats in Food Product
40
41
42
43
44
Thank You
45
To know the principles and the application of
major technologies and processes in edible
fats and oils production.
46
47
48
49
Hydrogenation process..
•
During hydrogenation, vegetable oils are reacted
with hydrogen gas at about 60ºC.
•
A nickel catalyst is used to speed up the reaction.
•
The double bonds are converted to single bonds in
the reaction. In this way unsaturated fats can be
made into saturated fats – they are hardened.
50
Why Hydrogenation?
• Convert vegetable oils into plastic fat forms
• Two reasons:
1. Change into physical forms with consistency and
handling characteristics required
2. Increase oxidative stability
•
Depends on conditions used, the starting
oils, degree of saturation or isomerization!
51
Hydrogenation Process
• Hydrogenated products = very complex
mixture of simultaneous reactions occur:
– Saturation of double bonds
– cis-/trans-isomerization of double bonds
➢Changes from low-melting cis form to higher melting
trans form
– Shifts of double bond locations
➢Affects melting point
52
53
1. Iodine value – Wij Iodine reach with double bond
where there was direct relation with iodine value and
degree of saturation
2. Bromine water test. Unsaturated vegetable oils
contain double carbon-carbon bonds. These can be
detected using bromine water (just as alkenes can be
detected). Bromine water becomes colourless when
shaken with an unsaturated vegetable oil, but it stays
orange-brown when shaken with a saturated vegetable
fat
Testing of double bond
54
55
• 2 types of unsaturated fatty acid
– cis configuration — "on the same side" in Latin
– trans configuration — "across" in Latin
Substrate for Hydrogenation
56
57
Hydrogenation Process
Hydrogen Gas
+
Nickel Catalyst
160 - 200 0C
Unsaturated and cis-unsaturated
fatty acid
IV of RBD Soya Bean Oil = 125
Double bond
partial
Double bond
trans-unsaturated fatty acid
Single bond
full
Saturated
IV of Hydrogenated Soya Bean Oil = 70
58
Hydrogenation Process
• How?
Unsaturated fatty acids
contain one or more double bonds
[liquid, lower melting point]
Chemically react hydrogen gas with double bond
More saturated fatty acid
Shifting to new position / twisting to trans configuration
[increase melting point]
59
Hydrogenation Process
• How? Three Reactants:
1. Unsaturated oil
2. Catalyst
3. Hydrogen gas
–
Dissolved in liquid oil
60
Hydrogenation Process
• How?
61
Hydrogenation Process
• Operating variables
– Oil, hydrogen, catalyst
– sufficient supplied of
hydrogen will increase
reaction rate > trans-
isomer decrease, flatter
SFI curve
62
Hydrogenation Process
• Operating variables
– any condition affects the catalyst surface or
controls the supply of gas to catalyst surface ~
1. Temperature
•
Rate
•
Solubility of hydrogen gas
•
Selectivity
•
Fatty acid configuration
63
Hydrogenation Process
• Operating variables
2. Hydrogen Pressure
•
Availability of hydrogen gas
•
Selectivity
•
Fatty acid configuration
64
Hydrogenation Process
• Operating variables
3. Agitation
•
Solubility of hydrogen gas
•
Selectivity
•
Fatty acid configuration
65
Hydrogenation Process
• Operating variables
4. Catalyst
o
Level / concentration
➢
Rate
o
Type
➢
Nickel, sulfur-poisoned/treated catalyst, copper
chromite catalysts, precious metals (palladium)
o
Poisons (from refined oils and hydrogen gas)
➢
Sulfur, phosphorus, water, FFA
o
Reuse
66
How the catalyst work…
67
Hydrogenation Process
• Operating variables
5. Source oils
•
Type of unsaturated fatty acids
•
Number of unsaturated fatty acid per triacylglyceride
Fatty Acid
Relative Reactivity
C-18:3 Linolenic
40
C-18:2 Linoleic
20
C-18:1 Oleic
1
68
Hydrogenation Process
• Systems
– Batch (simplicity, flexibility)
• Two different designs
1.
Recirculation
»
Filled with hydrogen under pressure in
recirculation system
2.
Dead-end
»
Hydrogen is added and vented when endpoint
reached
»
Safer, more versatile, lesser oxidation and
hydrolysis
69
Recirculation System
The reaction mixture (oil, H2
and catalyst) is continuously
re-circulated by an external
pump through an external
heat exchanger and a venturi
jet that is located inside the
autoclave, where fresh H2 is
added (see figure 2). These
reactors are generally
referred to as ‘loop-reactors’
70
Dead-end System
71
Hydrogenation Process
• Systems
– Continuous
•
Limited, due to variety of products to be
hydrogenated
72
Hydrogenation Process
• Control / endpoint?
– SFI
– IV
– Refractive Index
– Melting point
– Quick titer (refractometer)
73
Hydrogenation
• Product modification
– Softness, plasticity, organoleptic
– More selective hydrogenation process with higher
temperature, lower hydrogen pressure, lower
hydrogen gas solubility, higher catalyst selectivity
➢Product with steeper SFI (more trans- formed)
74
Hydrogenation
• Product modification
– Less selective hydrogenation process with lower
temperature, higher pressure, lower catalyst
selectivity level
➢Product with flatter SFI (less trans- formed)
75
Source: http://blog.fooducate.com/tag/hydrogenation/
76
77
78
79
80
81
Hydrogenated Fats Consumption
Source: http://www.purplemedicalblog.com/2005/12/what-trans-fat-labels-meanread-them.html
Major Food Sources of Trans Fat for American Adults
(Average Daily Trans Fat Intake is 5.8 Grams or 2.6 Percent of Calories)
82
Hydrogenated Fats in Food Product
83
84
85
86
87
Thank you
NE41102- Fats and Oil Technology
Semester 1 Session 2023/24
Fats Modification:
Hydrogenation
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