EP0607120A1 - Cholesterol reduction - Google Patents

Cholesterol reduction

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Publication number
EP0607120A1
EP0607120A1 EP90915067A EP90915067A EP0607120A1 EP 0607120 A1 EP0607120 A1 EP 0607120A1 EP 90915067 A EP90915067 A EP 90915067A EP 90915067 A EP90915067 A EP 90915067A EP 0607120 A1 EP0607120 A1 EP 0607120A1
Authority
EP
European Patent Office
Prior art keywords
cholesterol
cyclodextrin
yolk
emulsion
milk
Prior art date
Legal status (The legal status 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 status listed.)
Withdrawn
Application number
EP90915067A
Other languages
German (de)
French (fr)
Other versions
EP0607120A4 (en
Inventor
David George Oakenfull
Gurcharn Singh Sidhu
Michael Laurence Rooney
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Commonwealth Scientific and Industrial Research Organization CSIRO
Original Assignee
Commonwealth Scientific and Industrial Research Organization CSIRO
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
Priority claimed from AU55112/90A external-priority patent/AU630446B2/en
Application filed by Commonwealth Scientific and Industrial Research Organization CSIRO filed Critical Commonwealth Scientific and Industrial Research Organization CSIRO
Publication of EP0607120A4 publication Critical patent/EP0607120A4/en
Publication of EP0607120A1 publication Critical patent/EP0607120A1/en
Withdrawn legal-status Critical Current

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Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23CDAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C7/00Other dairy technology
    • A23C7/04Removing unwanted substances other than lactose or milk proteins from milk
    • A23C7/043Removing unwanted substances other than lactose or milk proteins from milk using chemicals in liquid or solid state, e.g. flocculating, adsorbing or extracting agents
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L15/00Egg products; Preparation or treatment thereof
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L5/00Preparation or treatment of foods or foodstuffs, in general; Food or foodstuffs obtained thereby; Materials therefor
    • A23L5/20Removal of unwanted matter, e.g. deodorisation or detoxification
    • A23L5/27Removal of unwanted matter, e.g. deodorisation or detoxification by chemical treatment, by adsorption or by absorption
    • A23L5/273Removal of unwanted matter, e.g. deodorisation or detoxification by chemical treatment, by adsorption or by absorption using adsorption or absorption agents, resins, synthetic polymers, or ion exchangers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08BPOLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B37/00Preparation of polysaccharides not provided for in groups C08B1/00 - C08B35/00; Derivatives thereof
    • C08B37/0006Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid
    • C08B37/0009Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid alpha-D-Glucans, e.g. polydextrose, alternan, glycogen; (alpha-1,4)(alpha-1,6)-D-Glucans; (alpha-1,3)(alpha-1,4)-D-Glucans, e.g. isolichenan or nigeran; (alpha-1,4)-D-Glucans; (alpha-1,3)-D-Glucans, e.g. pseudonigeran; Derivatives thereof
    • C08B37/0012Cyclodextrin [CD], e.g. cycle with 6 units (alpha), with 7 units (beta) and with 8 units (gamma), large-ring cyclodextrin or cycloamylose with 9 units or more; Derivatives thereof
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23VINDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2002/00Food compositions, function of food ingredients or processes for food or foodstuffs

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Polymers & Plastics (AREA)
  • Food Science & Technology (AREA)
  • Nutrition Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)
  • Biochemistry (AREA)
  • Materials Engineering (AREA)
  • Medicinal Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Medicinal Preparation (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)
  • Meat, Egg Or Seafood Products (AREA)
  • Dairy Products (AREA)

Abstract

On enlève le cholestérol présent dans les émulsions aqueuses de produits à base de produits laitiers ou d'oeufs en mettant une cyclodextrine en contact avec les émulsions aqueuses, en formant un complexe cyclodextrine/cholestérol, normalement à une température comprise entre 20 °C et 60 °C, et en provoquant la précipitation du complexe de la solution en la refroidissant à une température au-dessous de 5 °C. Le complexe ainsi précipité est retiré et la cyclodextrine est régénérée par extraction du cholestérol à l'aide d'un solvant choisi parmi des mélanges d'hexane, d'acide acétique ou d'acide acétique/butanol.The cholesterol present in the aqueous emulsions of dairy products or eggs is removed by bringing a cyclodextrin into contact with the aqueous emulsions, by forming a cyclodextrin / cholesterol complex, normally at a temperature between 20 ° C and 60 ° C, and causing precipitation of the solution complex by cooling it to a temperature below 5 ° C. The complex thus precipitated is removed and the cyclodextrin is regenerated by extraction of cholesterol using a solvent chosen from mixtures of hexane, acetic acid or acetic acid / butanol.

Description

CHOLESTEROL REDUCTION
Technical Field
This invention concerns a method for removing cholesterol from agueouε emulsions, especially from milk, dairy products and eggs.
Background Art
It is widely accepted that serious health r ks attach to high plasma cholesterol levels. In Australia, coronary heart disease is responsible for more than 50,000 deaths every year, and death from coronary heart disease is twice as frequent as death from cancer. Dairy products, in particular, are perceived as contributing significantly to dietary cholesterol butterfat, for example, contains approximately 3mg cholesterol per gram. Egg yolk is high on any list of cholesterol-containing foods. An average hen's egg yolk is almost 2% cholesterol, ie 20 mg/g, or 5-8 times the concentration found in butterfat. Consequently there is considerable interest internationally in reducing the cholesterol level of dairy products.
The present invention is based on the recognition that cholesterol can be separated from aqueous emulsions by precipitation as a complex with a cyclodextrin.
Disclosure of Invention
This invention provides a method for removing cholesterol from aqueous emulsions which comprises: i) contacting such an emulsion with a cyclodextrin to form a cyclodextrin-cholesterol complex; ii) causing the complex to precipitate; iii) separating the complex-precipitate.
The cyclodextrin may be added directly to the emulsion in powder form in which case ' the. emulsion acts as an aqueous solvent for the cyclodextrin or may be predissolved in water prior to addition to the emulsion.
In instances where a material containing cholesterol is not in emulsion form it should be dispersed in a suitable liquid to form an emulsion prior to contacting with the cyclodextrin. However materials already in such form, such as milk or cream, may be contacted directly with the cyclodextrin without any pre- reatment.
The term "emulsion" as used herein is intended to include micellar solutions or cholesterol-containing fat associated with protein as in lipoproteins.
In a typical process according to this invention an aqueous emulsion containing cholesterol is shaken at 20 C to to 60 C with an aqueous solution of β-cyclodextrin . A cyclodextrin-cholesterol complex is formed which precipitates from solution on cooling to 20 , prefei-ably below 5 C. The precipitate is removed, for example, by centrifugation.
Surprisingly it has been found that the cyclodextrin used in the method of the invention can work quite effectively at lower temperatures even though the conventional thinking would suggest that higher temperatures should be required to obtain a satisfactory degree of complex formation. The cholesterol containing fats in many biological materials are solid at low temperature. It is therefore to be expected that the solid fats will reduce the rate of adsorption of cholesterol by the cyclodextrin in comparison with the liquid form of the fats at higher temperatures. It is believed that the size of cholesterol containing globules of fats in the emulsions is a factor in ensuring that a satisfactory removal rate is realised. When the fat globules are very small, as in the case of milk, the cholesterol tends to accumulate at the surface of the globules with the result that it can readily transfer to the cyclodextrin even though the fat globules are solid.
The low temperature capability of a preferred method of the invention is particularly useful in relation to biological materials, such as with milk, cream or eggs which can spoil if they are not chilled.
Thus in a preferred aspect of the invention the temperature at which the complexation is carried out is below 18 C. More preferably a temperature range of 0-8 C is appropriate. Where such low complexation temperatures are used it is preferred that the fats in the emulsion be of sufficiently small size to ensure that at least 30% of the cholesterol is reacted to form a complex precipitate within 20 minutes of being mixed with the cyclodextrin. -
In order to ensure a high level of removal, the molar ratio of cyclodextrin to cholesterol should not be lower than 0.5, more preferably it should exceed 2. The ratio may be such as to ensure removal of at least 15% of the cholesterol from the emulsion, more preferably 40%.
The invention is suitable for decreasing the concentrat on of cholesterol in egg yolk, or egg yolk products such as yolk plasma, whole yolk solutions and egg white and yolk. More specifically the method of the invention when applied to such egg components or products comprises steps such as the . following:
i) preparing yolk, yolk plasma or egg white and yolk mixture for maximum contact with cyclodextrin, suitable procedures- being dilution with milk, water or salt solution, homogenisation, enzyme treatment, and addition of lipid;
ϋ) treating the yolk preparation with cyclodextrin;
iii) separating the precipitated cholesterol-cyclodextrin complex, typically by centrifugation.
An optional step following (iii) is the regeneration of a whole yolk product by addition of the yolk granules and concentration, or by removal of salt and concentration.
The diluted egg yolk or liquid whole egg is brought to the original concentration by removal of water and/or salt using a semi-permeable membrane. If necessary the granules-free''yolk is re-mixed with yolk granules, the purpose being to reconstitute the original " composition of liquid whole egg.
In a particularly preferred embodiment of the invention the yolk or yolk product is exposed to the action of the cyclodextrin in" the presence of egg white. We have found that, surprisingly, egg white or a component thei-eof can be responsible for up to a three-fold increase in the amount of cholesterol removed from egg yolk on treatment with cyclodextrin.
Desirably the concentration of cyclodextrin use in treatments relating to eggs according to this invention should not be less than about 2% (w/v). Cholesterol removal diminishes rapidly when lower concentrations are used, on the other hand cholesterol removal may be substantially enhanced at higher concentrations.
Primarily, the term cyclodextrin in thi specification means β-cyclodextrin, but it is to ' be understood to include α cyclodextrin, cyclodextrinε modified to promote their cholesterol attracting and retaining properties, and substituted cyclodextrins, which are soluble or insoluble in water and are capable of forming a complex precipitate with cholesterol .
Best Modes for Carrying Out the Invention
The invention will now be described with reference to the following examples:
EXAMPLE 1
Extraction of Cholesterol from an Oi1-in-Water Emulsion Cholesterol, labelled with 14C was emulsified with oleic acid, onoolein and taurocholic acid in phosphate buffer (pH
7.0). This emulsion was shaken with β-cyclodextrin in powder form (0.1-2% w/v) at temperatures ranging from 20 to 60 C and subsequently cooled to below 5 C. The cyclodextrin-cholesterol complex was removed by centrifugation. In a typical experiment, the adsorbent removed 85% of the cholesterol from the emulsion (As shown in
Table 1) . TABLE 1 - Removal of cholesterol from an emulsion by β-cyclodextrin
Activity of Labelled Cholesterol
05 (DPM)
Untreated Emulsion 7049
After exposure to the cyclodextrin 1095
10 EXAMPLE 2
Extraction of Cholesterol from Milk Milk was shaken with powdered β-cyclodextrin (1% w/v) for one hour at 40 C. On cooling in ice followed by centrifugation, the adsorbent was found to have removed 70% of the cholesterol from the fat (as
15 shown in Table 2) .
TABLE 2 Removal of cholesterol from milk by β-cyclodextrin.
Concentration of Molar ratio cholesterol in of CP:CH*
20 milk
(mg/g fat)
Untreated milk 3.20 30
After exposure to the cyclodextrin 0.96
_.. * Molar ratio of β-cyclodextrin to cholesterol
EXAMPLE 3
Extraction of Cholesterol from Cream Cream containing 18% fat was shaken with powdered β-cyclodextrin (2% w/v) for one
30 , j_ Λ„ hour at 40o C„. O_n cool,i.ng a.n i.ce f ÷ol ,l ■,owedj br_y cent *.ri -f ÷ugatJ.i-on, the cyclodextrin was found to have removed 79% of the cholesterol from the fat (as shown in Table 3).
35 TABLE 3 Removal of cholesterol from cream by β-cyclodextrin.
Concentration Molar ratio of cholesterol of CD:CH in cream (mg/g fat)
Untreated cream 3.10
After exposure to the cyclodextrin 0.65 15
EXAMPLE 4
Removal of cholesterol from egg yolk plasma
The yolk from White Leghorn eggs was diluted 1:1 with isotonic saline (0.16 M NaCl) and the mixture centrigued at 20,000 rpm (50,000 g) for 30 min at 10°C. The yolk granules (about 12% of the yolk) sedimented and the supernatant solution (about 20% w/v) after dilution with water, was used for cholesterol removal by treating with the powdered cyclodextrin (concentration ranging from 0.5 to 3.5% w/v for 20 minutes at temperatures ranging from 10-50 C). Cyclodextrin was then centrigued off at low speed. Cholesterol was determined in the solution by a chemical method.
TABLE 4 - TREATMENT OF YOLK PLASMA
Cyclodextrin Cholesterol Molar" Cholesterol Concentration Concentration Ratio in Yolk Plasma CD:CH
(% w/v) (mg/ml) left % removed 5
Dilution 1+1
0 5.40 1 4.87 0.7 90.2 9.-8 2 4.13 1.6 76.5 23.5 0
0 6.66 1. 5.80 0.47 87.0 13.0
0 5.83 2 4.73 1.4 81.0 19.0
Dilution 1+3 5
0 2.62 2 1.62 4.2 61.5 38.5
EXAMPLE 5
Removal of cholesterol from whole yolk 0
Yolk from White Leghorn hens' eggs (39.2 g) was diluted with 2M sodium chloride (13 ml) and stirred to dissolve the granules. The mixture was diluted with 0.5M sodium chloride and treated with powdered cyclodextrin at various dilutions as described $ for Example 4.
0
5 TABLE 5 '- TREATMENT OF WHOLE YOLK
Cyclodextrin Cholesterol Cholesterol
Concentration Concentration
(% w/v) in Yolk Plasma (mg/ml) % left % removed
Dilution 1+2.25 5.25 80 20
EXAMPLE 6
Removal of cholesterol from liquid whole egg
The yolks and whites of Australorp and Leghorn hens' eggs were mixed and beaten lightly. The mixture was then diluted with water or 0.5M sodium chloride and cholesterol extracted with cyclodextrin as for Examples 4 and 5.
TABLE 6 - TREATMENT OF WHOLE EGG PULP
Cyclodextrin Cholesterol Molar Cholesterol
Concentration Concentration ratio in Yolk Plasma of (% w/v) (mg/ml) CD:CH % left % removed
Australorp
Dilution 1+3 (NaCl)
2 1.13 6.-1 5 . 95 Leghorn
Dilution 1+3 (water)
2 1.54 4.4 .14 86
Australorp
Dilution 1+2 (NaCl) 2 2.41 2.8 37 63
Leghorn
Dilution 1+4 (NaCl)
2 1.40 4.9 11 89
Labelled milk (LM) was prepared by evaporating 4 ml of a chloroform solution containing 0.25 μCi 'of ^C-labelled cholesterol in a round bottomed flask containing 10 g of fine silica beads. Milk (50 ml) was added and mixed at 20 C for 30 in. using a rotary evaporator. Radioactive cholesterol readily exchanged with the cholesterol already in the milk.
Labelled scrambled egg mix (SEM) or labelled egg yolk low density lipoprotein (LDL) were prepared by introducing l ''C-labelled cholesterol by the same method as described for LM. The scrambled egg mix was prepared by combining the yolk and white from whole egg and mixing with an equal volume of full cream homogenised milk.
EXAMPLE 7 Labelled milk (LM) was mixed with β-cyclodextrin • and samples were maintained at different temperatures with different contact times. They were then cooled to 0 C, centrifuged and the cholesterol removed determined from the loss of radioactivity. The results are shown in Table 7. (This 5 Table demonstrates the improved efficiency at low temperatures.)
TABLE 7 Removal of cholesterol from milk by β-cyclodextrin.
Cyclodextrin Contact Temp DPM
10 Cholesterol
(% w/v) time (°C) Initial Fin.
(min. ) (%) CD:CH
1 0 10 40 1188 1 0 30 40 1188
15
1.0 10 8 1188 1.0 30 8 1188
1. 10 4 1188 1. 20 4 1188 1. 30 4 1188
20 2 5 4 1952 2 10 4 1952 2, 15 4 1952 2, 20 4 1952
EXAMPLE 8 2.5
Labelled scrambled egg mix (SEM) was mixed with β-cyclodextrin and samples were maintained at different temperatures with different contact times. They were then cooled to 0 C, centrifuged and the cholesterol removed was 30 etermined from the loss of radioactivity. The results are shown in Table 8.
35

Claims

- 16-
9. A method according o any one of the claims -1 to 6 and 8 wherein the complexing is carried out at a temperature below 18°C. •
10. A method according to claim 9 wherein the cholesterol containing components of the emulsion are presented in a form to ensure at least 30% of the cholesterol is complexed within 20 minutes of contact between the cyclodextrin and cholesterol when the molar ratio of cyclodextrin to cholesterol is 2.
11. A method according to anyone of the preceding claims wherein the emulsion comprises milk, , cream, egg yolk, egg yolk products, egg yolk plasma, whole yolk solutions or yolk-albumen mixtures.
12. A method according to claim 11 wherein the emulsion comprises yolk, yolk plasma or yolk-albumen mixture and the emulsion is subjected to pre-treatment to improve the extent and rate of complexing.
13. A method according to claim 12 wherein the pre-treatment comprises at' least one of the steps of dilution with water, dilution with milk, dissolution with salt solution, homogenisation, enzyme treatment, addition of lipid or combinations of these steps.
14. A method according to claim 13 wherein the emulsion comprises a yolk-^albumen mixture which is diluted with at least 40% by volume of milk prior to contact with the cyclodextrin.
15. A method according to any one of the preceding claims wherein the precipitated cyclodextrin-cholesterol complex is subjected to a regeneration step whereby the - -
choleεterol is removed from the complex to .provide free cyclodextrin.
16. A method according to claim 15 wherein cyclodextrin is regenerated by extracting cholesterol with an appropriate solvent chosen from hexane, acetic acid or acetic acid/butanol mixture (l:v; v/v) .
17. Products which have been treated in accordance with the method of any one of claims 1 to 16.
EP90915067A 1990-01-23 1990-10-12 Cholesterol reduction Withdrawn EP0607120A1 (en)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
AUPJ830890 1990-01-23
AU8308/90 1990-01-23
AU55112/90 1990-05-17
AU55112/90A AU630446B2 (en) 1989-05-19 1990-05-17 Cholesterol removal from eggs, dairy products and other aqueous emulsions
PCT/AU1990/000489 WO1991011114A1 (en) 1990-01-23 1990-10-12 Cholesterol reduction

Publications (2)

Publication Number Publication Date
EP0607120A4 EP0607120A4 (en) 1992-10-03
EP0607120A1 true EP0607120A1 (en) 1994-07-27

Family

ID=25630776

Family Applications (1)

Application Number Title Priority Date Filing Date
EP90915067A Withdrawn EP0607120A1 (en) 1990-01-23 1990-10-12 Cholesterol reduction

Country Status (5)

Country Link
EP (1) EP0607120A1 (en)
JP (1) JPH05505516A (en)
CA (1) CA2071217A1 (en)
NZ (1) NZ235649A (en)
WO (1) WO1991011114A1 (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4313919A1 (en) * 1993-04-28 1994-11-03 Sueddeutsche Kalkstickstoff Process for removing cholesterol derivatives from egg yolk
IL106581A (en) * 1993-08-04 2000-08-31 Yissum Res Dev Co Removal of cholesterol from edibles
US5738898A (en) * 1995-03-31 1998-04-14 Board Of Trustees Operating Michigan State University Process for reducing sterols in eggs
US5484624A (en) * 1995-03-31 1996-01-16 Board Of Trustees Operating Michigan State University Method for reduction of cholesterol in egg materials
US6110517A (en) * 1997-08-02 2000-08-29 Se Jong University Method for removing cholesterol from milk and cream
WO1999017620A1 (en) * 1997-10-06 1999-04-15 Eugene Science Inc. Process for reducing the content of cholesterol in dairy products
US6129945A (en) * 1998-12-10 2000-10-10 Michael E. George Methods to reduce free fatty acids and cholesterol in anhydrous animal fat
DE102012220689A1 (en) * 2012-11-13 2014-05-15 Wacker Chemie Ag Method for reducing the content of sterols in milk and cream

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2601959B1 (en) * 1986-07-24 1988-12-02 Monserbio Gie PROCESS FOR REMOVAL OF CHOLESTEROL FROM ANIMAL FATTY MATERIAL AND DEPLETED CHOLESTEROL FATTY MATERIAL OBTAINED
FR2626145B1 (en) * 1988-01-22 1990-07-06 Monserbio PROCESS FOR THE REMOVAL OF STEROID COMPOUNDS CONTAINED IN A SUBSTANCE OF BIOLOGICAL ORIGIN

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO9111114A1 *

Also Published As

Publication number Publication date
CA2071217A1 (en) 1991-07-24
EP0607120A4 (en) 1992-10-03
WO1991011114A1 (en) 1991-08-08
JPH05505516A (en) 1993-08-19
NZ235649A (en) 1993-03-26

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