CS226332B1 - Spreadable butter manufacturing method - Google Patents
Spreadable butter manufacturing method Download PDFInfo
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- CS226332B1 CS226332B1 CS533482A CS533482A CS226332B1 CS 226332 B1 CS226332 B1 CS 226332B1 CS 533482 A CS533482 A CS 533482A CS 533482 A CS533482 A CS 533482A CS 226332 B1 CS226332 B1 CS 226332B1
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Description
Predmetom vynálezu je spdsob výroby nátierkového masla o nízkej energetickej hodnotě.It is an object of the present invention to provide a method of producing a low energy spreading butter.
Doterajšie spdsoby výroby nátierkového masla spočívajú v našlahávaní látok mliečného, alebo nemliečného pdvodu do masla, alebo smotany za účelom zníženia váhového, alebo objemového poměru mliečneho tuku vo výrobku. Ďalšie spdsoby výroby spočívajú v homogenizácii zmesi smotany a látok mliečneho a nemliečneho pdvodu pri nižších teplotách a následnej fermentácii zmesi, vyššieho záhrevu a Salšej homogenizácii. Uvedeného spdsobu výroby sa dotýká aj AO 193760-79. Ďalšie spdsoby výroby sa zakladajú na tvorbě emulzií masla, resp. bezvodého mliečneho tuku s látkami mliečneho, alebo nemliečneho pdvodu Tohoto spdsobu výroby sa týká aj PV 6058/79· Uvedené spdsoby výroby sú náročnejšie na technologické zariadenie a neumožňujú kontinuálnu výrobu z ddvodu nutnosti biologického zrenia.Existing methods for producing spreading butter consist in whipping milk or non-milk substances into butter or cream to reduce the weight or volume ratio of milk fat in the product. Other methods of production consist in homogenizing the mixture of cream and dairy and non-dairy substances at lower temperatures and subsequent fermentation of the mixture, higher heating and saler homogenization. AO 193760-79 also relates to this production method. Other methods of production are based on the formation of butter emulsions, respectively. This method of production also applies to PV 6058/79 · The production methods mentioned are more demanding on the technological equipment and do not allow continuous production due to the necessity of biological maturation.
Nevýhody doterajšieho sposdbu výroby odstraňuje vynález, pri ktorom smotana, alebo zmes mlieka a masla, alebo bezvodého mliečneho tuku po přídavku mliečnych bielkovín, emulgátorov, stabilizátorov, príp. farbiva sa po záhreve homogenizuje a po přídavku smetanového zákysu, alebo organických kyselin sa za tepla plní do spotřebitelských obalov.Disadvantages of the prior art production method are eliminated by the invention in which a cream or a mixture of milk and butter, or anhydrous milk fat, after addition of milk proteins, emulsifiers, stabilizers, resp. the dyes are homogenized after heating and, after addition of creamy mash or organic acids, are filled into consumer packages with heat.
Výhodou spdsobu výroby podl’a vynálezu je poměrná jednduchosť technologie, nie je potřebné fermentácie zmesi a tým sa umožňuje kontinualizácia výrobného procesu. Spdsob výroby podTa vynálezu umožňuje výrobu nátierkového masla o nízkej energetickej hodnotě, o dobrých senzorických vlastnostiach aj v čase nedostatočného nákupu mlieka pri využití skladovanej suroviny.The advantage of the production method according to the invention is the relative simplicity of the technology, there is no need for the fermentation of the mixture and thus it is possible to continualise the production process. The process according to the invention makes it possible to produce a spreading butter of low energy value, of good sensory properties even at the time of inadequate milk purchase using the stored raw material.
PřikladlEXAMPLE
Do 1 000 kg mliekarensky ošetrenej smotany o obsahu tuku 40 g v 100 g sa přidá 40 kg sušeného mlieka, 7 kg koncentrátov mliečnych bielkovín, ,0 kg bobtnavého škrobu a 3>5 kg emulgátorov. Zmes sa premieša, zahřeje na 75 °c a homogenizuje pri tlaku 28 MPa. Po homogenizácii sa do zmesi vmieša 100 kg smetanového zékysu a zmes sa za tepla plní do spotřebitelských obalov.40 kg of milk powder, 7 kg of milk protein concentrates, 0 kg of swelling starch and 3> 5 kg of emulsifiers are added to 1000 kg of dairy cream with a fat content of 40 g in 100 g. The mixture is stirred, heated to 75 ° C and homogenized at 28 MPa. After homogenization, 100 kg of creamy chocolate is mixed into the mixture and the mixture is hot filled into consumer packages.
Příklad 2Example 2
Na 1 000 kg hotového výrobku sa použije 417 kg masla, 505 kg tekutého odstředěného mlieka, 40 kg sušeného mlieka, 5 kg koncentrátov mliečnyoh bielkovín a 4,4 kg emulgátora.For 1000 kg of finished product, 417 kg of butter, 505 kg of liquid skimmed milk, 40 kg of milk powder, 5 kg of milk protein concentrates and 4.4 kg of emulsifier are used.
Zmes sa zahřeje na 55 °C, homogenizuje pri tlaku 25 MPa. Po homogenizácii sa do zmesi přidá kyselina citrónová, alebo mliečná, alebo zmes kyseliny citrónovéj a mliečnej v takom množstve, aby aktívna kyslosť finálneho výrobku bola pH 5,8 a zmes sa za tepla plní do spotřebitelských obalov.The mixture is heated to 55 ° C, homogenized at 25 MPa. After homogenization, citric or lactic acid or a mixture of citric acid and lactic acid is added to the mixture in an amount such that the active acidity of the final product is pH 5.8 and the mixture is hot filled into consumer packages.
Příklad 3Example 3
Mlieko v množstve 515 kg sa zahrieva spolu s 340 kg bezvodného mlíečneho tuku, 50 kg sušeného mlieka s výhodou mlieka odstředěného, 5 kg emulgátora, 6 kg kuchyňskéj soli, a 4 kg želatiny a 6 kg bobtnavého škrobu na teplotu 80 °C. Zmes sa homogenizuje při tlaku 21 MPa a do zhomogenizovanej zmesi sa vmieša 79 kg smotanového zákysu a kyselina citrónová, alebo mliečna v takom množstve, aby výsledná aktívna kyslosť zmesi bola pH 5,3, a zmes sa za tepla plní do spotřebitelských obalov.The milk of 515 kg is heated with 340 kg of anhydrous milk fat, 50 kg of skimmed milk, preferably skimmed milk, 5 kg of emulsifier, 6 kg of kitchen salt, and 4 kg of gelatin and 6 kg of swelling starch to 80 ° C. The mixture is homogenized at a pressure of 21 MPa and 79 kg of creamy mash and citric or lactic acid are added to the homogenized mixture in a quantity such that the resulting active acidity of the mixture is pH 5.3, and the mixture is hot filled into consumer packages.
Claims (4)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CS533482A CS226332B1 (en) | 1982-07-13 | 1982-07-13 | Spreadable butter manufacturing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CS533482A CS226332B1 (en) | 1982-07-13 | 1982-07-13 | Spreadable butter manufacturing method |
Publications (1)
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CS226332B1 true CS226332B1 (en) | 1984-03-19 |
Family
ID=5398043
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CS533482A CS226332B1 (en) | 1982-07-13 | 1982-07-13 | Spreadable butter manufacturing method |
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CS (1) | CS226332B1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2604338A1 (en) * | 1986-09-27 | 1988-04-01 | Westfalia Separator Ag | PROCESS FOR MAKING BUTTER |
-
1982
- 1982-07-13 CS CS533482A patent/CS226332B1/en unknown
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2604338A1 (en) * | 1986-09-27 | 1988-04-01 | Westfalia Separator Ag | PROCESS FOR MAKING BUTTER |
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