Nothing Special   »   [go: up one dir, main page]

MY124490A - High carotene palm oil production by repeated neutralisation and low temperature deodorisation - Google Patents

High carotene palm oil production by repeated neutralisation and low temperature deodorisation

Info

Publication number
MY124490A
MY124490A MYPI96000148A MYPI19960148A MY124490A MY 124490 A MY124490 A MY 124490A MY PI96000148 A MYPI96000148 A MY PI96000148A MY PI19960148 A MYPI19960148 A MY PI19960148A MY 124490 A MY124490 A MY 124490A
Authority
MY
Malaysia
Prior art keywords
palm oil
deodorisation
low temperature
neutralisation
free fatty
Prior art date
Application number
MYPI96000148A
Inventor
Mohd Suria Affandi Yusoff Dr
Aini Bt Haji Idris Nor
Ismail Razali
Original Assignee
Malaysian Palm Oil Board
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 Malaysian Palm Oil Board filed Critical Malaysian Palm Oil Board
Priority to MYPI96000148A priority Critical patent/MY124490A/en
Publication of MY124490A publication Critical patent/MY124490A/en

Links

Landscapes

  • Fats And Perfumes (AREA)
  • Edible Oils And Fats (AREA)

Abstract

THE PRESENT INVENTION RELATES TO MODIFICATIONS TO THE CONVENTIONAL PROCESS OF REFINING CRUDE PALM OIL SO THAT THE CAROTENE CONTENT IS SUBSTANTIALLY RETAINED BUT DEVOID OF OTHER IMPURITES. THE MODIFICATIONS COMPRISE (I) REPEATING THE NEUTRALISATION STEP AT LEAST ONCE AT TEMPERATURE ABOUT 80?C TO REMOVE FREE FATTY ACIDS FROM THE PALM OIL; (II) REMOVING THE REMAINING FREE FATTY ACID AND OTHER IMPURITIES BY DEODORISATION AT RELATIVE LOW TEMPERATURES, I.E. ABOUT 150?C; (III) CRYSTALLISE AND FRACTIONATE THE PALM OIL AT RELATIVELY LOW TEMPERATURE, I.E. 65?C, TO MAINTAIN THE CLARITY OF THE FINAL PRODUCT. THE REFINED PALM OIL CONTAINS LESS THAN 0.1% FREE FATTY ACID, HAS A CAROTENE CONTENT RETAINED OF ABOUT 70%, A CLOUD POINT OF LESS THAN 10?C AND IODINE VALUE OF MORE THAN 60.
MYPI96000148A 1996-01-15 1996-01-15 High carotene palm oil production by repeated neutralisation and low temperature deodorisation MY124490A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
MYPI96000148A MY124490A (en) 1996-01-15 1996-01-15 High carotene palm oil production by repeated neutralisation and low temperature deodorisation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
MYPI96000148A MY124490A (en) 1996-01-15 1996-01-15 High carotene palm oil production by repeated neutralisation and low temperature deodorisation

Publications (1)

Publication Number Publication Date
MY124490A true MY124490A (en) 2006-06-30

Family

ID=81534517

Family Applications (1)

Application Number Title Priority Date Filing Date
MYPI96000148A MY124490A (en) 1996-01-15 1996-01-15 High carotene palm oil production by repeated neutralisation and low temperature deodorisation

Country Status (1)

Country Link
MY (1) MY124490A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8716505B2 (en) 2009-01-08 2014-05-06 Sime Darby Research Sdn. Bhd. Refining of edible oil

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8716505B2 (en) 2009-01-08 2014-05-06 Sime Darby Research Sdn. Bhd. Refining of edible oil

Similar Documents

Publication Publication Date Title
EP0333472A3 (en) Production of high concentration tocopherols and tocotrienols from palm oil by-products
US5679809A (en) Concentrate of polyunsaturated fatty acid ethyl esters and preparation thereof
DK0839896T3 (en) Refining edible oil, which has a high content of natural carotenes and vitamin E
EP1342787A3 (en) Arachidonic acid and methods for the production and use thereof
US4298622A (en) Method for producing wheat germ lipid products
WO2010080019A3 (en) Refining of edible oil
DK0737238T3 (en) Process for removing chlorophyll color impurities from vegetable oils
JPH04320645A (en) Production of enriched rice bran oil
US5849940A (en) Triglyceride fractionation
US3102129A (en) Process for producing monoglycerides of fatty acids
JPH0711285A (en) Method for purifying vegetable wax
US4100181A (en) Process for obtaining free fatty acids from soap stock
AU2004256204A1 (en) Process for preparing purified fatty acids
US4754090A (en) Process for the preparation of hexamethyl tetracosanes
MY124490A (en) High carotene palm oil production by repeated neutralisation and low temperature deodorisation
US2543055A (en) Crystallizing process
US5210242A (en) Process for soap splitting using a high temperature treatment
MX238306B (en) A process for making high purity fatty acid lower alkyl esters
US3345389A (en) Separation of fatty materials
US2369036A (en) Treating fatty bodies
US2640841A (en) Refining and bleaching of sugar cane wax
US1927850A (en) Refining of vegetal oils and fats
KR930000779B1 (en) Fish oil modifying method by mono sodium glutamate byproduct
EP0457401A1 (en) Mid-fraction production by fractional crystallization with stearin and olein fraction recycling to interesterification
MY110779A (en) Production of high concentration tocopherols and tocotrienols from palm oil by-product