hydrogenation .ppt; basestock and process control
TRANSCRIPT
Copyright M HUSNI RIZAL WTDP 2008 1
Hydrogenation ; Base stock and Process Control
Solidification, Consistency, and Composition Analysis
Copyright M HUSNI RIZAL WTDP 2008 2
• Palmitic basedThe major content of oil is palmitic acid which derived from Crude Palm Oil eg. RBDPO, RBDST, RBDOL, Soft ST, COL, CPS, PMF, PFAD, etc
• Lauric basedThe major content of oil is lauric acid which derived from Crude Coconut Oil and Crude Palm Kernel Oil eg. CKS, CKL, RKS, RKL, RCNO, PKFAD, etc
Oil Type
Copyright M HUSNI RIZAL WTDP 2008 3
• Crude eg. CPO, CPKO, CCNO, CKS, CKL, etc.
• Refinedeg. RPO, RST, RBDOL, RKS, RKO, RKL, RCNO, etc.
• Hydrogenatedeg. HPO, HKL, HKS, HKO, HCNO, etc.
• Refined Hydrogenatedeg. RHPO, RHPKO, RHCNO, RHKS, RHKL, etc.
• Fatty Acid Distillateeg. PFAD, PKFAD.
Oil Classification
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• Free Fatty Acid (%)• Lovibon Color (R/Y)• Iodine Value (Wijs)• Moisture & Impurities (%)• Solid Fat Content (%)• Fatty Acid Composition (as FAMEs) • Cold Test (hrs)• Melting Point & Cloud Point (deg C)• Peroxide Value (meq/kg)• Odor (Organoleptic Test)
Oil Quality Analysis
Copyright M HUSNI RIZAL WTDP 2008 5
Hydrogenation
R – CH = CH – CH3 R – H2 – CH2 – CH2 - COOH
H2
Pt / Ni
1. decreasing degree of unsaturated, where poly unsaturated turns to mono unsaturated whilst mono unsaturated becomes saturated
2. tends to solid forming
Breaking double bond replaced by hydrogen, in consequences ;
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Types of Hydrogenation ;• fully hydrogenation ( IV ≤ 1 )• partial hydrogenation ( IV ≥ 1)
Hydrogenation cont.
Hydrogenation role in process of ;• Cocoa Butter Substitute• Cocoa Butter Replacer
Copyright M HUSNI RIZAL WTDP 2008 7
SFC (%) = number of protons in solid state x 100
number of protons in solid & liquid state
Solid Fat Content
using NMR Spectrometer represent amount of fat on variable temperatures
PurposeDetermining on what temperatures oil solidify or liquidify
Copyright M HUSNI RIZAL WTDP 2008 8
Solid Fat Content cont.
Methods
• TemperingApplied for cocoa butter equivalent, or exotic oil blend such as illipe butter and salstearin
• Non TemperingApplied for palm oil, palm kernel oil, fraction derived oil and oil blended product
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Solid Fat Content cont.
Tempering procedures
1.apply sample in SFC vial at about 3-4 cm,2.heated to 70 deg C for 30 minutes,3.cooled to 0 deg C for 90 minutes,4.temper at 26 deg C for 40 hours,5.cooled to 0 deg C for 90 minutes,6.distribute to variable temperatures
10 ; 20 ; 25 ; 30 ; 35 ; 40 deg C, for 30 minutes,7.read the SFC using NMR.
Copyright M HUSNI RIZAL WTDP 2008 10
Solid Fat Content cont.
Non Tempering procedures
1.apply sample in SFC vial at about 3-4 cm,2.heated to 70 deg C for 30 minutes,3.cooled to 0 deg C for 90 minutes,4.distribute to variable temperatures
10 ; 20 ; 25 ; 30 ; 35 ; 40 deg C for 30 minutes,5.read the SFC using NMR.
Copyright M HUSNI RIZAL WTDP 2008 11
Fatty Acid Composition
using Gas Chromatography analysis, FAC of oil analyzed as Fatty Acid Methyl Ester (FAME) resulting peak perform with specific number, order, and intensity. These data is specific for each palmitic or lauric based oil which differentiate on the amount of each specific dominant fatty acids C16 and C12 respectively.
PurposeDetermining the composition of each fatty acids content on specific oil.
Copyright M HUSNI RIZAL WTDP 2008 12
Procedures1. weigh sample 0.05 gram onto GC vial2. add 1 ml NaOH-methanolic 0.5 N3. add 1 ml BF3-methanolic (for crude only)4. heated on 70 deg C water bath for 10 minutes5. cooled in room temperature6. add saturated NaCl 0.5 ml7. add 2 ml n-hexane8. apply to GC with syringe
Fatty Acid Composition cont.
Copyright M HUSNI RIZAL WTDP 2008 13
Variables contribute in resulting chromatogram;• instrument• column• gas flows• injection technique• recorderThings to concern about the chromatogram;• right number of the peaks• right order of the peaks• right relative sizes
Fatty Acid Composition cont.
Copyright M HUSNI RIZAL WTDP 2008 14
Based on hypothesis that every oil & fat properties connected each other while palm kernel oil derivate is an essential part in edible oil industry, so the research undergo with kernel oil (which is lauric based) and it’s hydrogenated derivatives as objects;
Research
Refined RKO RKL RKS
# 1105 # 1104 # 1205
IV 17.61 IV 23.15 IV 6.24
Hydrogenated HRKO HRKL HRKS
# 1302 # 1306 # 1401
IV 0.44 IV 8.69 IV 0.05
Refined Hydrogenated RHKO RHKL RHKS
# 1604 # 1609 # 1601
IV 0.41 IV 8.39 IV 0.09
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Chromatogram of RKO IV 17.61
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Chromatogram of RKL IV 23.15
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Chromatogram of RKS IV 6.24
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Chromatogram of HRKO IV 0.44
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Chromatogram of HRKL IV 8.69
Copyright M HUSNI RIZAL WTDP 2008 20
Chromatogram of HRKS IV 0.05
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Chromatogram of RHKO IV 0.41
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Chromatogram of RHKL IV 8.39
Copyright M HUSNI RIZAL WTDP 2008 23
Chromatogram of RHKS IV 0.09
Copyright M HUSNI RIZAL WTDP 2008 24
Solid Fat Content (%) SFC RKO SFC RKL SFC RKS SFC HRKO SFC HRKL SFC HRKS SFC RHKO SFC RHKL SFC RHKS
Source 1105 1104 1205 1302 1306 1401 1604 1609 1601
IV 17,61 23,15 6,24 0,44 8,69 0,05 0,41 8,39 0,09
N 10 72,72 58,43 94,66 96,23 91,53 96,96 96,04 93,14 97,07
N 20 40,74 16,94 86,64 89,64 67,47 95,54 88,34 66,41 95,55
N 25 17,63 0,41 71,26 65,52 37,36 89,11 65,16 38,02 88,39
N 30 0,03 - 33,92 34,29 14,78 47,3 33,22 14,71 48,03
N 35 - - 0,21 12,45 5,68 2,4 12,23 5,44 2,19
N 40 - - - 5,71 0,4 - 5,54 0,96 0,23
Fatty Acid Comp (%) FAME RKO FAME RKL FAME RKS FAME HRKO FAME HRKL FAME HRKS FAME RHKO FAME RHKL FAME RHKS
C6:0 0,30 0,31 0,08 0,22 0,24 0,08 0,21 0,24 0,06
C8:0 3,50 4,29 1,85 3,42 3,85 1,86 3,25 3,93 1,80
C10:0 3,33 3,62 2,82 3,32 3,42 2,79 3,18 3,45 2,77
C12:0 46,59 43,08 55,62 46,77 41,82 55,18 46,39 41,95 55,26
C14:0 15,73 12,75 22,06 15,78 12,66 21,89 15,97 12,67 22,03
C16:0 8,81 8,33 8,68 8,59 8,75 8,80 8,67 8,78 8,75
C16:1 0,00 0,00 0,00 0,00 0,00 0,00 0,00 0,00 0,00
C17:0 0,00 0,00 0,00 0,00 0,00 0,00 0,00 0,00 0,00
C18:0 2,46 2,52 2,07 21,58 18,73 9,26 21,89 18,54 9,15
C18:1 tr 0,11 0,00 0,00 0,05 6,20 0,00 0,10 6,14 0,00
C18:1 cis 16,41 21,42 5,89 0,00 4,06 0,01 0,07 4,04 0,04
C18:2 tr 0,00 0,00 0,00 0,00 0,00 0,00 0,00 0,00 0,00
C18:2 cis 2,52 3,37 0,81 0,00 0,00 0,00 0,00 0,00 0,00
C18:3 0,11 0,14 0,05 0,00 0,00 0,00 0,00 0,00 0,00
C20:0 0,12 0,13 0,07 0,23 0,23 0,13 0,24 0,22 0,13
C22:0 0,03 0,04 0,00 0,03 0,04 0,00 0,03 0,04 0,00
10 degC 96,21 95,39 98,07 96,36 95,91 98,06 96,54 95,84 98,14
% deviation 24,41439806 38,74839132 3,479293483 0,132776061 4,57003741 1,122486364 0,521266427 2,812767846 1,089297601
Copyright M HUSNI RIZAL WTDP 2008 25
Lauric Palmitic
FAC RKO RKL RKS RPO ROL RPS
C 6:0 0.1 - 0.5 0.2 - 0.4 0 - 0.1
C 8:0 3.4 - 5.9 3.6 - 5.0 1.5 - 2.3
C 10:0 3.3 - 4.4 3.2 - 4.5 2.5 - 2.9
C 12:0 46.3 - 51.1 42.1 - 46.3 54.8 - 58.2 0.1 - 0.3 0.2 - 0.4 0.1 - 0.3
C 14:0 14.3 - 16.8 12.3 - 15.5 21.1 - 24.1 1.0 - 1.4 0.9 - 1.2 1.1 - 1.7
C 16:0 6.5 - 8.9 7.4 - 10.6 7.2 - 8.6 40.9 - 47.5 36.6 - 43.2 49.8 - 68.1
C 18:0 1.6 - 2.6 1.8 - 2.7 1.3 - 2.2 3.8 - 4.8 3.7 - 4.8 3.9 - 5.6
C 18:1 13.2 - 16.4 14.6 - 21.3 4.6 - 6.8 36.4 - 41.2 39.8 - 44.6 20.4 - 34.4
C 18:2 2.2 - 3.4 2.6 - 3.8 0.6 - 1.1 9.2 - 11.6 10.4 - 12.9 5.0 - 8.9
C 18:3 ND ND ND 0.1 - 0.6 0.1 - 0.5 0 - 0.5
C 20:0 ND 0 - 0.2 ND 0.2 - 0.7 0.3 - 0.5 0 - 0.5
FAC Ring Specification
SFC Control Limit for CKS Derivatives
Product Target N30 SFC
CKS 30 min
RKS 30 min
HKS 45 min
RHKS 46 min
Copyright M HUSNI RIZAL WTDP 2008 26
SFC and FAC of Kernel Oil and Its Hydrogenated Derivatives
0
10
20
30
40
50
60
70
80
90
100
N 10 N 20 N 25 N 30 N 35 N 40
%
0.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
80.00
90.00
100.00
C6
:0
C8
:0
C1
0:0
C1
2:0
C1
4:0
C1
6:0
C1
6:1
C1
7:0
C1
8:0
C1
8:1tr
C1
8:1cis
C1
8:2tr
C1
8:2cis
C1
8:3
C2
0:0
C2
2:0
%
SFC RKO
SFC HRKO
SFC RHKO
FAME RKO
FAME HRKO
FAME RHKO
Copyright M HUSNI RIZAL WTDP 2008 27
SFC and FAC of Kernel Olein and Its Hydrogenated Derivatives
0
10
20
30
40
50
60
70
80
90
100
N 10 N 20 N 25 N 30 N 35 N 40
%
0.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
80.00
90.00
100.00
C6
:0
C8
:0
C1
0:0
C1
2:0
C1
4:0
C1
6:0
C1
6:1
C1
7:0
C1
8:0
C1
8:1tr
C1
8:1cis
C1
8:2tr
C1
8:2cis
C1
8:3
C2
0:0
C2
2:0
%
SFC RKL
SFC HRKL
SFC RHKL
FAME RKL
FAME HRKL
FAME RHKL
Copyright M HUSNI RIZAL WTDP 2008 28
SFC and FAC of Kernel Stearin and Its Hydrogenated Derivatives
Copyright M HUSNI RIZAL WTDP 2008 29
Conclusion
In determining correlation between SFC and FAC data of oil and fat using lauric based oil as experiment object end up with unsatisfactorily unfinished complete conclusion. Yet still there’s a patron model that for oil with low IV value perform slight deviation compared both N10 value with sum of fatty acid content with melting point above 10 deg C.
Copyright M HUSNI RIZAL WTDP 2008 30
Further Tasks
1. completing oil and fat properties data as a useful catalogue for production or product development purposes,
2. dig more insight to each oil and fat properties that contributes to or influence other, since that every analysis is numerous and routine so whether for efficiency and practical reason, it is beneficial.
In order to get a complete information of oil and fat properties which is very important when dealing with customer specification and the capabilities of production, so we need to do;