序号 专利名 申请号 申请日 公开(公告)号 公开(公告)日 发明人
181 Improvement in the manufacture of flour US112046D US112046A 1871-02-21
182 EXTRACTION OF COMPOUNDS FROM DAIRY PRODUCTS EP04706899.4 2004-01-30 EP1589820B1 2008-07-09 FLETCHER, Andrew; FLETCHER, Katrina; CATCHPOLE, Owen; GREY, John
The present invention relates to processes for the treatment of dairy products and dairy process streams to produce lipids and substantially defatted protein streams. More specifically it relates to the use of near critical fluid extraction techniques to extract lipids from liquid dairy products and dairy process streams. Preferred solvents for use in the described near critical extraction techniques are ether based solvents that are partially miscible with water. A particularly preferred solvent for use in the invention is dimethyl ether.
183 EXTRACTION OF COMPOUNDS FROM DAIRY PRODUCTS EP04706899 2004-01-30 EP1589820A4 2006-05-24 FLETCHER ANDREW; FLETCHER KATRINA; CATCHPOLE OWEN; GREY JOHN
The present invention relates to processes for the treatment of dairy products and dairy process streams to produce lipids and substantially defatted protein streams. More specifically it relates to the use of near critical fluid extraction techniques to extract lipids from liquid dairy products and dairy process streams. Preferred solvents for use in the described near critical extraction techniques are ether based solvents that are partially miscible with water. A particularly preferred solvent for use in the invention is dimethyl ether.
184 METHODS TO REDUCE FREE FATTY ACIDS AND CHOLESTEROL IN ANHYDROUS ANIMAL FAT EP99966080 1999-12-09 EP1137342A4 2005-10-19 AWAD AZIZ CHAFIC; GRAY JAMES IAN
A process for removing free fatty acids (FFA) and preferably cholesterol from liquid anhydrous animal fats is described. The process uses a dilute solution of alkali metal base to form a salt of the FFA and then an alkali metal salt to precipitate the FFA from the animal fat. Preferably, a cyclodextrin is used in the process to remove cholesterol. Liquid vegetable fats are used in blends with the processed animal fat to produce a spreadable mixture for table use. The processed animal fat can be reconstituted to whole milk with the FFA and cholesterol removed for various commercial uses.
185 CONTINUOUS CRYSTALLIZATION SYSTEM WITH CONTROLLED NUCLEATION FOR MILK FAT FRACTIONATION EP98924753 1998-05-07 EP0985005A4 2003-05-07 HARTEL RICHARD W; BAOMIN LIANG; YUPING SHI
An apparatus and method (10) of fractionating mixed triglycerides, more particularly anhydrous milk fat, are disclosed. The apparatus and method provide for the separation of the steps of nucleation and crystal growth. Precise control of energy input (27) for nucleation and crystal growth in a static environment at higher temperatures than the nucleation temperature result in the production of a solid fraction characterized by higher yields and a uniform maximum melting temperatures (MMT).
186 CONTINUOUS CRYSTALLIZATION SYSTEM WITH CONTROLLED NUCLEATION FOR MILK FAT FRACTIONATION EP98924753.1 1998-05-07 EP0985005A1 2000-03-15 HARTEL, Richard, W.; BAOMIN, Liang; YUPING, Shi
An apparatus and method (10) of fractionating mixed triglycerides, more particularly anhydrous milk fat, are disclosed. The apparatus and method provide for the separation of the steps of nucleation and crystal growth. Precise control of energy input (27) for nucleation and crystal growth in a static environment at higher temperatures than the nucleation temperature result in the production of a solid fraction characterized by higher yields and a uniform maximum melting temperatures (MMT).
187 Structured lipid containing dairy fat EP89904880.5 1989-03-31 EP0449819B1 1994-11-30 BABAYAN, Vigen, K.; BLACKBURN, George, L.; BISTRIAN, Bruce, R.
The present invention features a transesterification product of a mixture of fatty acids and triglycerides which include dairy fat as a primary component. This composition shows unexpected benefits in nutritional applications either as a food or as an enteral or parenteral supplement. The method of nutritional support using this composition is also disclosed.
188 Spreadable water-in-oil emulsion based on a high-melting butterfat fraction and a liquid oil EP82200346.3 1982-03-22 EP0063389B2 1993-11-10 Verhagen, Laurentius Adrianus Maria; Bodor, Janos
189 Flavour concentrate EP89203218.6 1989-12-18 EP0377239B1 1993-06-09 Haring, Petrus Gerardus Maria; Potman, Ronald Peter
190 A fat or oil composition in powdery or granular form and a process for producing the same EP88200638.0 1988-04-06 EP0289069B1 1993-03-31 Hamaguchi, Takashi
A powdery or granular fat or oil composition in the form of a powder or granules having a water content of 15 % by weight or less, a maximum particle diameter of not greater than 10 mm, an average particle diameter of not greater than 5 mm and an angle of repose of not greater than 70 %. The composition is produced simply by mixing only a fat or oil, a base material capable of occlusion or absorption of the fat or oil and a liquid polyol at a temperature at which the fat or oil is molten.
191 Process for the preparation of a flavoured foodstuff as well as a foodstuff obtainable by such a process EP88201374.1 1988-07-01 EP0298552B1 1991-09-18 Haring, Petrus Gerardus Maria
192 Dried fat emulsion product and method of producing the same EP90101038.9 1990-01-19 EP0385081A3 1990-11-22 Burros, Byron; Einerson, Mark A.; Tran, Kha

Dried fat emulsion products having improved resistance to oxidation at elevated temperatures are produced by the two stage encapsulation of oil or fat globules with a hydrophilic film forming material. An aqueous dispersion of an edible fat or oil, a hydrophilic film forming material, a carbohydrate and water is emulsified to form an oil-in-water emulsion concentrate in which fat globules are encapsulated by the film forming material. After formation of the emulsion concentrate, a second portion of a hydrophilic film forming material is added to the emulsion concentrate in an amount substantially equivalent to the amount of film former in the aqueous dispersion, to provide an additional coating layer of film forming material encapsulating the fat globules. This second portion of film forming material may be added to the emulsion prior to or subsequent to drying of the emulsion concentrate.

193 A fat or oil composition in powdery or granular form and a process for producing the same EP88200638.0 1988-04-06 EP0289069A3 1990-07-18 Hamaguchi, Takashi

A powdery or granular fat or oil composition in the form of a powder or granules having a water content of 15 % by weight or less, a maximum particle diameter of not greater than 10 mm, an average particle diameter of not greater than 5 mm and an angle of repose of not greater than 70 %. The composition is produced simply by mixing only a fat or oil, a base material capable of occlusion or absorption of the fat or oil and a liquid polyol at a temperature at which the fat or oil is molten.

194 Production of whipping cream EP82302689.3 1982-05-25 EP0095001B1 1987-09-16 Bratland, Arthur
195 Apparatus for melting refrigerated butter EP80201237.7 1980-12-29 EP0055306B1 1985-03-27 Van Vlaenderen, Johannes M. H.
196 Spreadable water-in-oil emulsion based on a high-melting butterfat fraction and a liquid oil EP82200346.3 1982-03-22 EP0063389B1 1984-06-13 Verhagen, Laurentius Adrianus Maria; Bodor, Janos
197 Production of whipping cream EP82302689.3 1982-05-25 EP0095001A1 1983-11-30 Bratland, Arthur

A method of making cream involves separating high and low melting point fractions from butter oil, and emulsifying one of the fractions with a low fat milk fraction enriched in membrane substances. Emulsification of the high melting point fraction can give whipping creams of low fat content and temperature sensitivity and good viscosity, especially if the cream is homogenised, pasteurised and then homogenised again and if the cooled cream is tempered by warming and recooling. Emulsification of the low melting fat fraction yields cream churnable to butter which spreads at refrigerator temperatures. The low fat milk fraction may be the serum separated in the production of the butter oil, but there may be used instead or in addition buttermilk or butter serum from another source. The butter fat fraction may be emulsified together with a non-milk fat.

198 Spreadable water-in-oil emulsion based on a high-melting butterfat fraction and a liquid oil EP82200346.3 1982-03-22 EP0063389A1 1982-10-27 Verhagen, Laurentius Adrianus Maria; Bodor, Janos

The invention relates to a spreadable water-in-oil emulsion based on a high melting butterfat fraction and a liquid oil which is free of solid fat crystals at 5°C and to a process for producing said emulsion. The use of a high melting fraction obtained by dry fractionation at 15-30°C, as one of the fat components of the fatty phase of the emulsion enables the incorporation of up to 80% of liquid oil, preferably an oil having a relatively high level of polyunsaturated fatty acids.

199 Low-calorie spread based on a low-melting butterfat fraction EP82200349.7 1982-03-22 EP0062938A1 1982-10-20 Verhagen, Laurentius Adrianus Maria; Warnaar, Leendert Gerardus

The invention relates to a low-calorie spread based on a low-melting butterfat fraction, which has an improved spreadability at 10°C as compared with low-calorie butter. The low-melting butterfat fraction is an olein preferably obtained by dry fractionation of butterfat within the temperature range of 20-30°C.

200 Apparatus for melting refrigerated butter EP80201237.7 1980-12-29 EP0055306A1 1982-07-07 Van Vlaenderen, Johannes M. H.

The invention relates to an apparatus for melting refrigerated butter, cream or similar substances. According to the invention, a block (3) of butter to be melted is forced by a mechanically energized punch (4) through a grating (2), which grating (2) is composed of heated tubes (102) that are substantially triangular in transverse section. The block of butter is faced by angular top edges (7) of the tubes (102). The wall (12) of the grating tubes facing away from the block (3) of butter is preferably furnished with a heat barrier (11), the angular edges (9) of this wall being as sharp-cornered as possible and preferably equipped with aprons (13) which are at least substantially perpendicular to the plane of the grating.

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