CS258683B3 - The method of production of spreading butter - Google Patents
The method of production of spreading butter Download PDFInfo
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- CS258683B3 CS258683B3 CS879186A CS879186A CS258683B3 CS 258683 B3 CS258683 B3 CS 258683B3 CS 879186 A CS879186 A CS 879186A CS 879186 A CS879186 A CS 879186A CS 258683 B3 CS258683 B3 CS 258683B3
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Abstract
Riešenie je závislé na AO 226 332, pri ktarom do zmesi smotany, alebo zmesi mlieka a masla, alebo bezvodého mliečneho tuku sa pridajú mliečne bielkoviny, emulgátor, stabilizátor, zmes sa tepelne ošetří a homogenizuje pri teplotách 30 až 75 °C. Úprava aktívnej kyslosti zmesi sa vykoná prídavkom smetanového zákysu, čistých termofilných mliekárenských kultúr, kyseliny citrónovej, mliečnej, alebo zmesi uvedených látok.The solution is dependent on AO 226 332, where milk proteins, an emulsifier, a stabilizer are added to a mixture of cream, or a mixture of milk and butter, or anhydrous milk fat, the mixture is heat-treated and homogenized at temperatures of 30 to 75 ° C. The active acidity of the mixture is adjusted by adding sour cream, pure thermophilic dairy cultures, citric acid, lactic acid, or a mixture of the above substances.
Description
Vynález sa týká sposobu výroby nátierkov-ého masla podl'a, AO 226 332, pri ktorom smotana, alebo zmes mlieka a masla, alebo bezvodého- mliečneho tuku po- přídavku mliečnych bielkovín, emulgátorov-, stabilizátorov, prí-p. farbiva sa po záhreve na 55 až 95 °C homogenizuje a po- přídavku smotanového zákysu, alebo organických kyselin sa za tepla plní do spotřebitelských -obalov.BACKGROUND OF THE INVENTION The present invention relates to a process for the preparation of spread butter according to AO 226 332, wherein the cream, or a mixture of milk and butter, or anhydrous milk fat, is supplemented with milk proteins, emulsifiers, stabilizers, and the like. the dye is homogenized after heating to 55 DEG-95 DEG C. and added to the consumer packs by the addition of cream or organic acids.
Nevýhodou sposobu výroby podta uvedeného AO 226 332 je, že nie je možné dosiahnúť zvýšenú kys-losť výrobku len samotným prídavkom smotanového zákysu, ktorý působením použitých teplůt sa inaktiv-uje.A disadvantage of the production process of AO 226 332 is that it is not possible to achieve an increased acidity of the product only by the addition of a creamy additive which is inactivated by the heats used.
Nevýhody spůsobu výroby podlá AO číslo 226 332 odstraňuje vynález, pri ktorom sa smotana, alebo zmes mlieka a masla, alebo bezvodého mliečneho tuku po- přídavku mliečnych bielkovín, emulgátorov, stabilizáto-rov, kuchynskej soli, príp. farbiva zahřeje na teplotu 55 až 95 °G, po záhreve s-a ochladí na 35 až 75 °C a homogenizuje. Do zmesi sa vrnieša smotanový zákys, alebo term-o-filné mliekárenské kultúry. Výhodou spůsobu výroby po-dla vynálezu je, že na, dosiahnutie požadovaných kysl-ostí výrobku stačí nižší prídavok lorganických kyselin, alebo požadovaná kyslosť výrobku sa může dosiahnúť aj bez přídavku organických kyselin fermentáciou zmesi, čím sa dosiahne zlepšenie senzorických vlastností výrobku. Příklad 1Disadvantages of the method of manufacture according to AO number 226 332 removes the invention in which the cream, or a mixture of milk and butter, or anhydrous milk fat is added with milk proteins, emulsifiers, stabilizers, table salt, or salt. the dye is heated to 55-95 ° C, heated to -35 ° C to 75 ° C and homogenized. Cream blends or thermo-filed dairy cultures are mixed into the blend. An advantage of the process of the invention is that a lower addition of organic acids is sufficient to achieve the desired acidity of the product, or the desired acidity of the product can be achieved without the addition of organic acids by fermentation of the mixture, thereby improving the sensory properties of the product. Example 1
Do 1 000 kg mliekárensky ošetrenej smotany o obsahu tuku 40 g v 100 g sa přidá 40 kg sušeného odstředěného mlieka, 7 kg koncentrátov mliečnych bielkovín, 10 kg bobtnavého škrobu a 3,5 kg emulgátora. Zmes sa premieša, zahřeje na 55 °C a homogenizuje pri tlaku 28 MPa. Po homogenizácii sa do- zmesi vrnieša 50 1 smotanového zákysu a 50 1 termofilných čistých mliekárenských kultúr a zmes sa za tepla plní do spotřebitelských obalov. Příklad 2To 1000 kg of milk-treated cream with a fat content of 40 g in 100 g, add 40 kg of skimmed-milk powder, 7 kg of milk protein concentrates, 10 kg of swelling starch and 3.5 kg of emulsifier. The mixture is stirred, heated to 55 ° C and homogenized at 28 MPa. After homogenization, 50 liters of creamy starter and 50 liters of thermophilic clean dairy cultures are blended and the mixture is hot-filled into consumer packages. Example 2
Na 1 000 kg hotového- výrobku sa použije 417 kg masla, 445 kg tekutého odstredené- 4 ho mlieka, 40 kg sušeného odstředěného mlieka, 5 kg koncentrátov mliečnych bielkovín a 4,4 kg emulgátora. Zmes sa za-hreje na 95 °-C, vychladí na 75 °C, homogenizuje pri tlaku 25 MPa. Po ho-mogenizácil sa do zmesi přidá kyselina citrónová, alebo mliečna, alebo zmes kyseliny citrónovej a mliečnej v- pomere 1: 1 v takom množstve, aby aktívna kyslosť finálneho- výrobku bola pH 5,8 a zmes sa za tepla plní do spotřebitelských obalov. Příklad 3417 kg of butter, 445 kg of liquid skim milk, 40 kg of skimmed milk powder, 5 kg of milk protein concentrates and 4.4 kg of emulsifier are used per 1 000 kg of finished product. The mixture is heated to 95 ° C, cooled to 75 ° C, homogenized at 25 MPa. After homogenization, citric acid or lactic acid, or a 1: 1 mixture of citric acid and lactic acid, is added to the mixture in such a way that the active acidity of the final product is pH 5.8 and the mixture is hot-filled into consumer packaging . Example 3
Odstředěné mlieko v množstve 515 kg sa zahrieva spolu s 340 kg bezvodého- mliečneho tuiku, 50 kg sušeného odstředěnéhomlieka, 5 kg emulgátora, 5 kg kuchynskej soli, 4 kg želatiny a 6 kg bobtnavého škrobu na teplotu 80 °C. Zmes sa homogenizuje pri teplote 55 °C a tlaku 21 MPa a do zhomogenizovanej zmesi sa vrnieša 50 kg smotanového zákysu, 29 kg termofilných mliekárenských kultúr a kyselina citrónová v taikom množstve, aby výsledná aktívna kyslosť zmesi bola pH 5,3 a zmes sa za tepla plní do- spotřebitelských obalov. Příklad 4 D-o 1 000 kg mliekárensky ošetrenej smotany o obsahu tuku 40 g v 100 g sa přidá 40 kg sušeného- odstředěného- mlieka, 7 kg koncentrátov mliečnych bielkovín, 10 kg bobtnavého škrobu, 3,5 kg emulgátorov. Zmes sa premieša, zahřeje na 75 °C, ochladí na 30 °C, přidá sa 20 kg smotanového zákysu, zmes sa homogenizuje pri tlaku 20 MP-a a naplní do spotřebitelských obalov. P r í k 1 a d 5515 kg of skimmed milk is heated together with 340 kg of anhydrous milk fat, 50 kg of skimmed milk powder, 5 kg of emulsifier, 5 kg of cooking salt, 4 kg of gelatin and 6 kg of intumescent starch to 80 ° C. The mixture is homogenized at 55 ° C and 21 MPa and 50 kg of cream creamer, 29 kg of thermophilic dairy cultures and citric acid are added to the homogenized mixture in such a quantity that the resulting acidity of the mixture is pH 5.3 and the mixture is hot. it fulfills consumer packaging. EXAMPLE 4 D-1000 kg of dairy-treated cream with a fat content of 40 g in 100 g is added 40 kg of dried-skimmed milk, 7 kg of milk protein concentrates, 10 kg of swelling starch, 3.5 kg of emulsifiers. The mixture is stirred, heated to 75 ° C, cooled to 30 ° C, 20 kg of cream creamer is added, the mixture is homogenized at 20 MPa and filled into consumer packages. Example 5
Do 100 kg mliekárensky ošetrenej smotany o obsahu tuku 42 g v-100 g sa přidá 45 kg sušeného- odstředěného- mlieka, 10 kg termicky modifikovaného škrobu, 3 kg emulgátorov. Zmes sa zahřeje na 55 °C a zhomogenizuje pri tlaku 20 MPa. Do zmesi sa vmieša 30 kg smotanového zákysu a s-a naplní do spotřebitelských obalov.To 100 kg of milk-treated cream with a fat content of 42 g in-100 g, add 45 kg of dried-skimmed milk, 10 kg of thermally modified starch, 3 kg of emulsifiers. The mixture is heated to 55 ° C and homogenized at 20 MPa. 30 kg of cream creamer is mixed into the mixture and filled into consumer packaging.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS879186A CS258683B3 (en) | 1986-12-01 | 1986-12-01 | The method of production of spreading butter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS879186A CS258683B3 (en) | 1986-12-01 | 1986-12-01 | The method of production of spreading butter |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CS879186A1 CS879186A1 (en) | 1987-12-17 |
| CS258683B3 true CS258683B3 (en) | 1988-09-16 |
Family
ID=5438955
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CS879186A CS258683B3 (en) | 1986-12-01 | 1986-12-01 | The method of production of spreading butter |
Country Status (1)
| Country | Link |
|---|---|
| CS (1) | CS258683B3 (en) |
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1986
- 1986-12-01 CS CS879186A patent/CS258683B3/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| CS879186A1 (en) | 1987-12-17 |
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