MY184018A - Continuous process for dry fractionation of glyceride oils - Google Patents

Continuous process for dry fractionation of glyceride oils

Info

Publication number
MY184018A
MY184018A MYPI2014703630A MYPI2014703630A MY184018A MY 184018 A MY184018 A MY 184018A MY PI2014703630 A MYPI2014703630 A MY PI2014703630A MY PI2014703630 A MYPI2014703630 A MY PI2014703630A MY 184018 A MY184018 A MY 184018A
Authority
MY
Malaysia
Prior art keywords
glyceride oil
temperature
sop
oil
glyceride
Prior art date
Application number
MYPI2014703630A
Inventor
Hidayu Othman Noor
Md Noor Ahmadilfitri
Suria Affandi Yussof Mohd
Said Syed Saggaf Syed
Jaril Asis Ahmad
Original Assignee
Sime Darby Plantation Intellectual Property Sdn Bhd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sime Darby Plantation Intellectual Property Sdn Bhd filed Critical Sime Darby Plantation Intellectual Property Sdn Bhd
Priority to MYPI2014703630A priority Critical patent/MY184018A/en
Priority to PCT/MY2015/000059 priority patent/WO2016089196A1/en
Priority to DK15766668T priority patent/DK3227418T3/en
Priority to PL15766668T priority patent/PL3227418T3/en
Priority to EP15766668.6A priority patent/EP3227418B1/en
Priority to ES15766668T priority patent/ES2753402T3/en
Priority to PT157666686T priority patent/PT3227418T/en
Publication of MY184018A publication Critical patent/MY184018A/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B7/00—Separation of mixtures of fats or fatty oils into their constituents, e.g. saturated oils from unsaturated oils
    • C11B7/0075—Separation of mixtures of fats or fatty oils into their constituents, e.g. saturated oils from unsaturated oils by differences of melting or solidifying points

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Fats And Perfumes (AREA)

Abstract

The present invention provide a continuous dry fractionation process comprising the successive step of: (a) providing a liquid glyceride oil having a temperature that is at least 5?C higher than the solidification onset point (SOP) of the glyceride oil, the SOP of the glyceride oil being the minimum temperature at which the glyceride oil has a N-value of 0%; (b) precooling the liquid glyceride oil at a cooling rate of at least 1 ?C/min by passing the glyceride oil through a heat exchanger to reduce the temperature of the liquid glyceride oil with at least 5?C to a temperature that is not lower than 10?C below the SOP and not higher than 5?C above the SOP; (c) homogenizing the precooled glyceride oil to produce a prenucleated glyceride oil by passing the precooled glyceride oil through a homogenizer in which the temperature of the glyceride oil is kept a temperature within 1?C of the prenucleation temperature Tp for at least 0.5 hour, said Tp being 0.5-10?C below the SOP; (d) crystallizing the prenucleated glyceride oil to produce a crystallized glyceride oil containing separable fat crystals by passing the prenucleated glyeride oil through one or more crystallizers to reduce the temperature of the prenucleated glyceride oil with at least 10?C to a crystallization temperature Tc and keeping the glyceride oil at a temperature within 1?C of Tc for at least 1 hour; and (e) removing separable fat crystals from the crystallized glyceride oil and recovering an olein fraction of the glyceride oil. This continuous fractionation process enables the manufacture of a high quality olein fraction in high yield and in a relatively short period of time.
MYPI2014703630A 2014-12-03 2014-12-03 Continuous process for dry fractionation of glyceride oils MY184018A (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
MYPI2014703630A MY184018A (en) 2014-12-03 2014-12-03 Continuous process for dry fractionation of glyceride oils
PCT/MY2015/000059 WO2016089196A1 (en) 2014-12-03 2015-07-16 Continuous process for dry fractionation of glyceride oils
DK15766668T DK3227418T3 (en) 2014-12-03 2015-07-16 CONTINUOUS PROCEDURE FOR DRY FRACTIONING GLYCERID OILS
PL15766668T PL3227418T3 (en) 2014-12-03 2015-07-16 Continuous process for dry fractionation of glyceride oils
EP15766668.6A EP3227418B1 (en) 2014-12-03 2015-07-16 Continuous process for dry fractionation of glyceride oils
ES15766668T ES2753402T3 (en) 2014-12-03 2015-07-16 Continuous process for the dry fractionation of glyceride oils
PT157666686T PT3227418T (en) 2014-12-03 2015-07-16 Continuous process for dry fractionation of glyceride oils

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
MYPI2014703630A MY184018A (en) 2014-12-03 2014-12-03 Continuous process for dry fractionation of glyceride oils

Publications (1)

Publication Number Publication Date
MY184018A true MY184018A (en) 2021-03-17

Family

ID=54148603

Family Applications (1)

Application Number Title Priority Date Filing Date
MYPI2014703630A MY184018A (en) 2014-12-03 2014-12-03 Continuous process for dry fractionation of glyceride oils

Country Status (7)

Country Link
EP (1) EP3227418B1 (en)
DK (1) DK3227418T3 (en)
ES (1) ES2753402T3 (en)
MY (1) MY184018A (en)
PL (1) PL3227418T3 (en)
PT (1) PT3227418T (en)
WO (1) WO2016089196A1 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108837551B (en) * 2018-07-28 2024-04-02 湖南懋天世纪新材料有限公司 Superfine ammonium paratungstate evaporation crystallization device and crystallization method
CN110257169A (en) * 2019-06-12 2019-09-20 深圳精益油脂技术有限公司 A method of preparing the palm oil of low ethylene oxidic ester and low 3-MCPD ester content
AU2021234620B2 (en) * 2020-03-10 2023-12-07 LIEW, Heng Wen Dry fractionation of edible oil

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1120456A (en) * 1964-12-14 1968-07-17 Ranchers Cotton Oil Method of separating components of oleaginous mixtures by fractional crystallization
DE2901328C2 (en) * 1979-01-15 1985-07-25 Walter Rau Lebensmittelwerke GmbH & Co. KG, 4517 Hilter Process for the selective extraction of triglycerides or mixtures of triglycerides of higher fatty acids in crystalline form from natural fats
CA1301775C (en) * 1986-06-04 1992-05-26 Karel Petrus Agnes Maria Van Putte Fractionation of fat blends
DE4132892A1 (en) * 1991-10-04 1993-04-22 Krupp Maschinentechnik SUBSTANCE MIXING FACTIONING
US6140520A (en) * 1997-05-12 2000-10-31 Wisconsin Alumni Research Foundation Continuous crystallization system with controlled nucleation for milk fat fractionation
ATE445690T1 (en) * 2001-07-31 2009-10-15 Smet Engineering N V De METHOD AND DEVICE FOR DRY FRACTIONATION
EP1818088A1 (en) * 2006-01-20 2007-08-15 De Smet Engineering N.V. Crystallisers useful in fractionation processes for oils and fats
GB2496606B (en) * 2011-11-15 2014-01-22 Desmet Ballestra Engineering S A Nv Continuous fractionation of triglyceride oils

Also Published As

Publication number Publication date
DK3227418T3 (en) 2019-11-11
ES2753402T3 (en) 2020-04-08
PT3227418T (en) 2019-11-05
WO2016089196A1 (en) 2016-06-09
PL3227418T3 (en) 2020-06-15
EP3227418B1 (en) 2019-09-04
EP3227418A1 (en) 2017-10-11

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