hydrogenation .ppt; basestock and process control

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Copyright M HUSNI RIZAL WTDP 2008 1 Hydrogenation ; Base stock and Process Control Solidification, Consistency, and Composition Analysis

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Page 1: Hydrogenation .Ppt; Basestock and Process Control

Copyright M HUSNI RIZAL WTDP 2008 1

Hydrogenation ; Base stock and Process Control

Solidification, Consistency, and Composition Analysis

Page 2: Hydrogenation .Ppt; Basestock and Process Control

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

Page 3: Hydrogenation .Ppt; Basestock and Process Control

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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Copyright M HUSNI RIZAL WTDP 2008 4

• 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

Page 5: Hydrogenation .Ppt; Basestock and Process Control

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 ;

Page 6: Hydrogenation .Ppt; Basestock and Process Control

Copyright M HUSNI RIZAL WTDP 2008 6

Types of Hydrogenation ;• fully hydrogenation ( IV ≤ 1 )• partial hydrogenation ( IV ≥ 1)

Hydrogenation cont.

Hydrogenation role in process of ;• Cocoa Butter Substitute• Cocoa Butter Replacer

Page 7: Hydrogenation .Ppt; Basestock and Process Control

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

Page 8: Hydrogenation .Ppt; Basestock and Process Control

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

Page 9: Hydrogenation .Ppt; Basestock and Process Control

Copyright M HUSNI RIZAL WTDP 2008 9

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.

Page 10: Hydrogenation .Ppt; Basestock and Process Control

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.

Page 11: Hydrogenation .Ppt; Basestock and Process Control

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.

Page 12: Hydrogenation .Ppt; Basestock and Process Control

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.

Page 13: Hydrogenation .Ppt; Basestock and Process Control

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.

Page 14: Hydrogenation .Ppt; Basestock and Process Control

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

Page 15: Hydrogenation .Ppt; Basestock and Process Control

Copyright M HUSNI RIZAL WTDP 2008 15

Chromatogram of RKO IV 17.61

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Copyright M HUSNI RIZAL WTDP 2008 16

Chromatogram of RKL IV 23.15

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Copyright M HUSNI RIZAL WTDP 2008 17

Chromatogram of RKS IV 6.24

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Copyright M HUSNI RIZAL WTDP 2008 18

Chromatogram of HRKO IV 0.44

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Copyright M HUSNI RIZAL WTDP 2008 19

Chromatogram of HRKL IV 8.69

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Chromatogram of HRKS IV 0.05

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Copyright M HUSNI RIZAL WTDP 2008 21

Chromatogram of RHKO IV 0.41

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Chromatogram of RHKL IV 8.39

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Chromatogram of RHKS IV 0.09

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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

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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

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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

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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

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Copyright M HUSNI RIZAL WTDP 2008 28

SFC and FAC of Kernel Stearin and Its Hydrogenated Derivatives

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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.

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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;