301 |
Method for making comminuted meats and extenders |
US868954 |
1978-01-12 |
US4161552A |
1979-07-17 |
Nicholas Melachouris |
Comminuted meats can be effectively extended using, in place of non-fat dry milk, the partially soluble modified whey solids derived by either (1) adding a divalent metal ion to a cheese whey solution and adjusting the pH to between about 6.0 and about 8.0 or (2) by adjusting the pH of a cheese whey solution containing at least 20% acid cheese whey to a value of between about 6.0 and about 8.0 to cause precipitation of the modified whey solids. Extension is equivalent or slightly better than that achieved using non-fat dry milk and/or modified non-fat dry milk with the added advantages of more uniform flavor and lower cost. |
302 |
Food composition containing whey colloidal precipitate |
US598873 |
1975-07-24 |
US4143174A |
1979-03-06 |
Syed M. M. Shah; Anthony J. Luksas |
A food-grade composition comprises a food of food-grade material, whey colloidal precipitate and water. The whey colloidal precipitate may effect the physical properties of clouding, stabilizing, gelling and emulsifying. The whey colloidal precipitate is a complex precipitate of whey in colloidal size ranges and is characterized by its ability to gell water and petroleum ether, is white in color, may be dried to a free-flowing powder and has no disagreeable whey taste. |
303 |
Process for preparing oxygenated cocktail |
US546982 |
1975-02-03 |
US4027045A |
1977-05-31 |
Igor Mikhailovich Fedotkin; Anatoly Konstantinovich Jukhimets; Leonid Panteleimonovich Odery |
According to the proposed process for preparing oxygenated cocktail, dispersed oxygen is continuously introduced into a continuously supplied thin (not in excess of 5 mm) layer of a foam-forming food liquid over the entire volume of said liquid. The disclosed apparatus for effecting said process comprises a vessel with a porous member arranged therein, which divides said vessel into two sealed off portions. The lower portion permanently communicates via a branch pipe with a forced oxygen supply source, whereas the upper portion serves as a container for the foam-forming liquid for preparing oxygenated cocktail and has a pipe for the supply of said food foam-forming liquid and a pipe for discharging prepared cocktail. The foam-forming food liquid may be fruit juice, kvass, beer, whey, buttermilk, herb infusion and other biologically adequate liquid products. |
304 |
Process for improving whipping properties of aqueous protein solutions |
US422213 |
1973-12-06 |
US3935323A |
1976-01-27 |
Joseph V. Feminella; Donald A. Grindstaff |
Aqueous solutions containing dissolved cheese whey protein exhibiting improved whipping properties are obtained by heating the solution to within the range of at least 90.degree. C. to less than 99.degree. C., thereafter cooling the solution to less than 60.degree. C., and whipping the solution within about 8 hours after heating. The process is particularly effective with protein solutions derived from cheese whey protein concentrates. |
305 |
Dispersible improved whey protein composition and method |
US36214973 |
1973-05-21 |
US3852506A |
1974-12-03 |
BURGE R; GROESBECK C; DOWD D |
The soapy taste of whey protein is rectified by finely grinding spray-dried spheres thereof and then agglomerating the subdivided particles into an agglomerate having a dry porous structure.
|
306 |
Confection and method of manufacture |
US3730735D |
1971-02-23 |
US3730735A |
1973-05-01 |
RASH K; COLMEY J; ZANZIG C |
Confection or candy mixes and products having relatively high levels of solubilized protein obtained by using partially delactosed and partially demineralized whey having an ash content of not more than about 6.5 percent in combination with a soluble caseinate.
|
307 |
Treatment of whey |
US3615664D |
1969-12-05 |
US3615664A |
1971-10-26 |
FRANCIS LEO H |
Liquid whey is subjected to concentration, crystallization of lactose and removal of lactose crystals. The resulting whey is clarified and electrodialyzed. It can be sold or used in liquid form, or may be further concentrated and dried to make a demineralized dry product with a reduction in ash content of at least 15 percent.
|
308 |
Process of treating whey |
US3447930D |
1966-04-14 |
US3447930A |
1969-06-03 |
FRANCIS LEO H |
1,155,654. Treating wheys. FOREMOST DAIRIES Inc. 13 April, 1967 [14 April, 1966], No. 16978/67. Heading A2B. A process of treating liquid whey (e.g. cheese whey) having not less than 80% by weight of its heat denaturable protein in substantially undenatured form, comprises the steps of concentrating the whey without substantial denaturation of the heat denaturable protein, clarifying the concentrate, electrodialysing the clarified concentrate to reduce the ash content by at least 15% by weight and then removing some lactose. The pH of the concentrate may be adjusted before the clarifying step and during the electrodialysing step. The electrodialysed concentrate may be further concentrated with or without effecting protein denaturation before the lactose removal step. The delactosed product may be used in the concentrated form or may be subjected to further concentration with or without effecting protein denaturation, a further delactosing step and a drying (e.g. spray-drying) step. The product may be used in infant foods or ice cream. |
309 |
Protein-rich feed material and method of making |
US36400364 |
1964-04-30 |
US3390999A |
1968-07-02 |
LEIF JANTZEN |
|
310 |
Whipping products and process of manufacture |
US29746252 |
1952-07-07 |
US2765232A |
1956-10-02 |
RODGERS NELSON E; HENIKA RICHARD G; MIERSCH RAYMOND E |
|
311 |
Whey products and process of manufacture |
US18449850 |
1950-09-12 |
US2661295A |
1953-12-01 |
FRANCIS LEO H; RODGERS NELSON E |
|
312 |
Lactalbumin of improved taste for human consumption |
US12623649 |
1949-11-08 |
US2606181A |
1952-08-05 |
PRATT WILLIAM J; TINKLER FRANK H |
|
313 |
Milk treatment process |
US30881739 |
1939-12-12 |
US2336634A |
1943-12-14 |
PECBLES DAVID D |
|
314 |
Process for coagulating proteins in liquor |
US17940337 |
1937-12-13 |
US2188908A |
1940-02-06 |
LAVETT CHARLES O |
|
315 |
Process for the recovery of a soluble protein powder from whey |
US13728637 |
1937-04-16 |
US2129222A |
1938-09-06 |
ABRAHAM LEVITON |
|
316 |
Method for the manufacture of stable powdered food products containing milk sugar |
US73341234 |
1934-07-02 |
US2126807A |
1938-08-16 |
PEEBLES DAVID D |
|
317 |
Process of producing food products from whey. |
US1902091417 |
1902-01-27 |
US735148A |
1903-08-04 |
RAMAGE ALEXANDER SYDNEY |
|
318 |
A METHOD FOR THE PREPARATION OF A SERUM PROTEIN CONCENTRATE |
PCT/IB2013056610 |
2013-08-13 |
WO2014027305A1 |
2014-02-20 |
REBIÈRE CHRISTIAN |
The present invention relates to a method for the preparation of a concentrate of serum proteins with reduced lactose content from a sample of lactoserum, wherein said concentrate is characterized in that it comprises a concentration of 0.5 grams of lactose per kilogram of protein, the concentrate obtainable from said process and food products containing said concentrate. |
319 |
PROTEIN BEVERAGE AND METHOD OF MAKING THE SAME |
PCT/US2012031707 |
2012-03-30 |
WO2012135774A3 |
2012-12-27 |
SHERWOOD SHERWOOD; RITTMANIC STEVEN ANTHONY; JENKINS DAVID A |
A protein beverage composition and a method of making it relate to a beverage including a protein essentially free of caseinate and derived from an aqueous protein isolate collected from membrane-filtration isolation of the protein and without substantial drying, wherein the protein beverage composition exhibits a pH ranging from about 2.0 to about 4.6. Substantial solubility of the protein is maintained in the beverage composition, and the protein beverage is essentially free of active microbes known to be harmful to human health, both at the time of packaging of the protein beverage and for a time period of at least one year after packaging. |
320 |
PROCESS FOR DEMINERALIZING WHEY AND PRODUCT THEREFROM |
PCT/US2008085297 |
2008-12-03 |
WO2009073673A9 |
2010-11-25 |
BATCHELDER BRUCE T |
A process has been found for demineralizing whey which results in usable by-product streams, comprising softening the whey, and then applying bipolar electrodialysis to the softened whey to recover valuable by-products and product streams, demineralized whey, dilute acid and dilute caustic. |