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Presented by
Omkar Joshi (18OIL207)
M.Tech (Oils, Oleochemicals and surfactants Technology)
Institute of Chemical Technology, Mumbai
Institute of Chemical Technology, Mumbai 1
Contents
 Introduction
 Processing of Rice Bran
 Crude oil Refining both Physical and chemical
 Loss of 𝛄- Oryzanol in Alkali Refining.
 Novel Methods for Rice Bran Oil Refining
 Conclusion
Institute of Chemical Technology, Mumbai 2
Rice bran contains 15-20% of lipid, which on
further processing like extraction becomes
as Rice bran oil.
Institute of Chemical Technology, Mumbai 3
Branding of Oryzanol rich product
Institute of Chemical Technology, Mumbai 4
Fortune Rice Bran Oil Emani Rice Bran Oil
Institute of Chemical Technology, Mumbai 5
Scope for future growth
 Rice bran Production: 10 MMT
 Rice bran Oil Production~ 5 MMT
 Untapped Potential is nearly 5 MMT
Institute of Chemical Technology, Mumbai 6
Important Minor Constituent
 Tocols
 Oryzanol
 Phytosterols
 Several tocopherols
 newly discovered policosanol.
Institute of Chemical Technology, Mumbai 7
γ- Oryzanol
 It is a mixture of esters of ferrulic acid , sterols and
triterpenic alcohols.
 They are again classified as A,B, C.
 γ- Oryzanol A:
 Chemical Name: cycloartenyl ferulate
 Empirical formula: C40H58O4
 Melting Point: 165.2–166.5°C (Ohta & Shimizu, 1957).
Institute of Chemical Technology, Mumbai 8
Structure
Institute of Chemical Technology, Mumbai 9
γ- Oryzanol C
 Chemical Name: 24-methylenecycloartanyl ferulate
 Empirical formula: C41H60O4,
 Melting Point: 164–164.5°C (Ohta, 1960).
Institute of Chemical Technology, Mumbai 10
Structure
Institute of Chemical Technology, Mumbai 11
Health Benefits of γ- Oryzanol
 increase in amount of good HDL cholesterol
 90% of the women had some relief from hot flashes
during the period of Menopause after taking a
supplement of the purified concentrate for four to six
weeks.
 Good antioxidant stability.
Institute of Chemical Technology, Mumbai 12
Processing of Rice bran
 Lipases can enhance free fatty acids (FFA =5-25%), To
avoid that stabilization is necessary.
 Ways to stabilize bran:
 Pass through extruder
 Adjustment of pH through weak acids.
 Microwave heating.
Institute of Chemical Technology, Mumbai 13
Extraction of Crude Oil from Rice
Bran
 Solvent : Hexane
 Pallet diameter : 6-8 mm Increases yield (Orthoefer &
Eastman, 2004).
 Hexane refluxed in a Soxhlet apparatus for three hour
Extraction of 20.21% oil
 supercritical CO2 at 4350 psi (30 MPa) at 35°C
Extraction of 17.98% oil.
 Hexane is best choice (Ramsay et al. 1991).
Institute of Chemical Technology, Mumbai 14
Crude Oil Refining
Institute of Chemical Technology, Mumbai 15
Institute of Chemical Technology, Mumbai 16
Loss of 𝛄- Oryzanol in Alkali
Refining (Vanessa Pestana et.al.2008)
Institute of Chemical Technology, Mumbai 17
Novel Methods for Rice Bran Oil
Refining
 Simultaneous Degumming and Dewaxing through
Physical refining.
 Super degumming
 Molecular Distillation of Residue from Deodorizer
Distillate.
 Reducing oil losses in alkali refining with help of salt
as de-emulsifier
Institute of Chemical Technology, Mumbai 18
Simultaneous Degumming and
Dewaxing through Physical
refining.
Institute of Chemical Technology, Mumbai 19
(L. Rajam. et.
al. 2005)
Minor constituents of Rice bran oil
at different stages (L. Rajam et.
al.2005)
Institute of Chemical Technology, Mumbai 20
 Reduction of tocopherol content
 Retention of Oryzanol Content
Institute of Chemical Technology, Mumbai 21
Super Degumming
(Segers et al. (1983) )
Institute of Chemical Technology, Mumbai 22
Molecular Distillation of Residue
from Deodorizer Distillate.
( Pattong Sawadikiat et. al.2013)
Institute of Chemical Technology, Mumbai 23
 Molecular Distillation used to separate heat-sensitive
materials based on the differences in molecular
weight, boiling point and vapour pressure (Martins et
al., 2006).
 The MD was operated at the feed temperature of 133 °C
and the pressure of 1.9 Pa in system. ( Pattong
Sawadikiat et. al.2013)
 Useful for high phospatide concentration.
Institute of Chemical Technology, Mumbai 24
Phytochemical contents, acid value
and fatty acid in different stages(
Pattong Sawadikiat et. al.2013)
Institute of Chemical Technology, Mumbai 25
 Potential use of Deodorizer Distillate as a raw material
for further production of phytosterol and γ-Oryzanol.
Institute of Chemical Technology, Mumbai 26
Reducing oil losses in alkali refining
with help of salt as de-emulsifier
Institute of Chemical Technology, Mumbai 27
 neutralisation carried out for removal of Free fatty acid
(FFA) resulted as soap formation.
 Micelle entraps oil molecule responsible for loss.
 Salt like NaCl, KCl, Na2SO4 and Tannic Acid used as
de emulsifier.
 Salt breaks emulsion and remove entrapped
oil(Aryusuk K. et. al. 2008).
Institute of Chemical Technology, Mumbai 28
Conclusion
 Physical Refining is much better way than alkali
refining method for rice bran oil.
 Soapstock formation avoided leading to no cost of
disposal.
 Higher the FFA, Higher oil loss.
 Higher the Viscosity, Higher oil loss.
 Salt act as deemulsifier and recover entrapped oil
Institute of Chemical Technology, Mumbai 29
Institute of Chemical Technology, Mumbai 30

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Methods for recovery of γ- Oryzanol from Rice bran oil refining

  • 1. Presented by Omkar Joshi (18OIL207) M.Tech (Oils, Oleochemicals and surfactants Technology) Institute of Chemical Technology, Mumbai Institute of Chemical Technology, Mumbai 1
  • 2. Contents  Introduction  Processing of Rice Bran  Crude oil Refining both Physical and chemical  Loss of 𝛄- Oryzanol in Alkali Refining.  Novel Methods for Rice Bran Oil Refining  Conclusion Institute of Chemical Technology, Mumbai 2
  • 3. Rice bran contains 15-20% of lipid, which on further processing like extraction becomes as Rice bran oil. Institute of Chemical Technology, Mumbai 3
  • 4. Branding of Oryzanol rich product Institute of Chemical Technology, Mumbai 4 Fortune Rice Bran Oil Emani Rice Bran Oil
  • 5. Institute of Chemical Technology, Mumbai 5
  • 6. Scope for future growth  Rice bran Production: 10 MMT  Rice bran Oil Production~ 5 MMT  Untapped Potential is nearly 5 MMT Institute of Chemical Technology, Mumbai 6
  • 7. Important Minor Constituent  Tocols  Oryzanol  Phytosterols  Several tocopherols  newly discovered policosanol. Institute of Chemical Technology, Mumbai 7
  • 8. γ- Oryzanol  It is a mixture of esters of ferrulic acid , sterols and triterpenic alcohols.  They are again classified as A,B, C.  γ- Oryzanol A:  Chemical Name: cycloartenyl ferulate  Empirical formula: C40H58O4  Melting Point: 165.2–166.5°C (Ohta & Shimizu, 1957). Institute of Chemical Technology, Mumbai 8
  • 9. Structure Institute of Chemical Technology, Mumbai 9
  • 10. γ- Oryzanol C  Chemical Name: 24-methylenecycloartanyl ferulate  Empirical formula: C41H60O4,  Melting Point: 164–164.5°C (Ohta, 1960). Institute of Chemical Technology, Mumbai 10
  • 11. Structure Institute of Chemical Technology, Mumbai 11
  • 12. Health Benefits of γ- Oryzanol  increase in amount of good HDL cholesterol  90% of the women had some relief from hot flashes during the period of Menopause after taking a supplement of the purified concentrate for four to six weeks.  Good antioxidant stability. Institute of Chemical Technology, Mumbai 12
  • 13. Processing of Rice bran  Lipases can enhance free fatty acids (FFA =5-25%), To avoid that stabilization is necessary.  Ways to stabilize bran:  Pass through extruder  Adjustment of pH through weak acids.  Microwave heating. Institute of Chemical Technology, Mumbai 13
  • 14. Extraction of Crude Oil from Rice Bran  Solvent : Hexane  Pallet diameter : 6-8 mm Increases yield (Orthoefer & Eastman, 2004).  Hexane refluxed in a Soxhlet apparatus for three hour Extraction of 20.21% oil  supercritical CO2 at 4350 psi (30 MPa) at 35°C Extraction of 17.98% oil.  Hexane is best choice (Ramsay et al. 1991). Institute of Chemical Technology, Mumbai 14
  • 15. Crude Oil Refining Institute of Chemical Technology, Mumbai 15
  • 16. Institute of Chemical Technology, Mumbai 16
  • 17. Loss of 𝛄- Oryzanol in Alkali Refining (Vanessa Pestana et.al.2008) Institute of Chemical Technology, Mumbai 17
  • 18. Novel Methods for Rice Bran Oil Refining  Simultaneous Degumming and Dewaxing through Physical refining.  Super degumming  Molecular Distillation of Residue from Deodorizer Distillate.  Reducing oil losses in alkali refining with help of salt as de-emulsifier Institute of Chemical Technology, Mumbai 18
  • 19. Simultaneous Degumming and Dewaxing through Physical refining. Institute of Chemical Technology, Mumbai 19 (L. Rajam. et. al. 2005)
  • 20. Minor constituents of Rice bran oil at different stages (L. Rajam et. al.2005) Institute of Chemical Technology, Mumbai 20
  • 21.  Reduction of tocopherol content  Retention of Oryzanol Content Institute of Chemical Technology, Mumbai 21
  • 22. Super Degumming (Segers et al. (1983) ) Institute of Chemical Technology, Mumbai 22
  • 23. Molecular Distillation of Residue from Deodorizer Distillate. ( Pattong Sawadikiat et. al.2013) Institute of Chemical Technology, Mumbai 23
  • 24.  Molecular Distillation used to separate heat-sensitive materials based on the differences in molecular weight, boiling point and vapour pressure (Martins et al., 2006).  The MD was operated at the feed temperature of 133 °C and the pressure of 1.9 Pa in system. ( Pattong Sawadikiat et. al.2013)  Useful for high phospatide concentration. Institute of Chemical Technology, Mumbai 24
  • 25. Phytochemical contents, acid value and fatty acid in different stages( Pattong Sawadikiat et. al.2013) Institute of Chemical Technology, Mumbai 25
  • 26.  Potential use of Deodorizer Distillate as a raw material for further production of phytosterol and γ-Oryzanol. Institute of Chemical Technology, Mumbai 26
  • 27. Reducing oil losses in alkali refining with help of salt as de-emulsifier Institute of Chemical Technology, Mumbai 27
  • 28.  neutralisation carried out for removal of Free fatty acid (FFA) resulted as soap formation.  Micelle entraps oil molecule responsible for loss.  Salt like NaCl, KCl, Na2SO4 and Tannic Acid used as de emulsifier.  Salt breaks emulsion and remove entrapped oil(Aryusuk K. et. al. 2008). Institute of Chemical Technology, Mumbai 28
  • 29. Conclusion  Physical Refining is much better way than alkali refining method for rice bran oil.  Soapstock formation avoided leading to no cost of disposal.  Higher the FFA, Higher oil loss.  Higher the Viscosity, Higher oil loss.  Salt act as deemulsifier and recover entrapped oil Institute of Chemical Technology, Mumbai 29
  • 30. Institute of Chemical Technology, Mumbai 30