SE508869C2 - Method for producing UHT milk with improved taste properties - Google Patents
Method for producing UHT milk with improved taste propertiesInfo
- Publication number
- SE508869C2 SE508869C2 SE9700928A SE9700928A SE508869C2 SE 508869 C2 SE508869 C2 SE 508869C2 SE 9700928 A SE9700928 A SE 9700928A SE 9700928 A SE9700928 A SE 9700928A SE 508869 C2 SE508869 C2 SE 508869C2
- Authority
- SE
- Sweden
- Prior art keywords
- milk
- temperature
- treatment
- heat treatment
- takes place
- Prior art date
Links
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C9/00—Milk preparations; Milk powder or milk powder preparations
- A23C9/15—Reconstituted or recombined milk products containing neither non-milk fat nor non-milk proteins
- A23C9/1508—Dissolving or reconstituting milk powder; Reconstitution of milk concentrate with water; Standardisation of fat content of milk
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C3/00—Preservation of milk or milk preparations
- A23C3/02—Preservation of milk or milk preparations by heating
- A23C3/03—Preservation of milk or milk preparations by heating the materials being loose unpacked
- A23C3/033—Preservation of milk or milk preparations by heating the materials being loose unpacked and progressively transported through the apparatus
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C3/00—Preservation of milk or milk preparations
- A23C3/02—Preservation of milk or milk preparations by heating
- A23C3/03—Preservation of milk or milk preparations by heating the materials being loose unpacked
- A23C3/033—Preservation of milk or milk preparations by heating the materials being loose unpacked and progressively transported through the apparatus
- A23C3/037—Preservation of milk or milk preparations by heating the materials being loose unpacked and progressively transported through the apparatus in direct contact with the heating medium, e.g. steam
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Dairy Products (AREA)
Abstract
Description
15 20 25 30 1.35 508 869 Ytterligare ett ändamål med föreliggande uppfinning är att upphettningen sker vid en hög temperatur under en mycket kort tid, med bibehållen avdödningseffekt, vilket även medverkar till en skonsammare behandling av mjölken och därmed sammanhängande bättre smakupplevelse. Another object of the present invention is that the heating takes place at a high temperature for a very short time, while maintaining a killing effect, which also contributes to a gentler treatment of the milk and the associated better taste experience.
Dessa och andra ändamål har enligt uppfinningen uppnåtts genom att metoden av den inledningsvis beskrivna typen, getts kännetecknen av att förbehandling sker vid en temperatur av 4-15°C samt att värmebehandlingen sker vid en temperatur överstigande 150°C.These and other objects have been achieved according to the invention by giving the method of the type initially described, the characteristics that pretreatment takes place at a temperature of 4-15 ° C and that the heat treatment takes place at a temperature exceeding 150 ° C.
Föredragna utföringsformer av uppfinningen har vidare getts de av underkraven framgàende kännetecknen.Preferred embodiments of the invention have furthermore been given the features apparent from the subclaims.
En föredragen utföringsform av uppfinningen kommer nu närmare att beskrivas med hänvisning till bifogad ritning, vilken: Fig. 1 visar ett flödesschema över en anläggning för genomförandet av metoden.A preferred embodiment of the invention will now be described in more detail with reference to the accompanying drawing, which: Fig. 1 shows a flow chart of a plant for carrying out the method.
Då råmjölken inkommer till mejeriet håller den vanligtvis en temperatur av 4°C.When colostrum arrives at the dairy, it usually maintains a temperature of 4 ° C.
Den inkommande mjölken kan eventuellt lagras i mellantankar, vilken lagring sker under bibehållen tempertur. Då mjölken skall behandlas transporteras den i en rörledning 1 till en separator 2. Separator 2 kan vara av konventionell typ, men då man inte önskar att värma upp mjölken innan separering kan ävenledes en s.k. kallseparator 2 användas. Mjölken separeras enligt uppfinningen vid en tempertur av 4-15°C, varför en viss obetydlig uppvärmning kan ske innan mjölken når separatorn 2. Försök har visat att man får ett visst, men dock försumbart, ökat fettinnehåll i skummjölken vid separering vid låga temperaturer. Fördelen är dock att man får en skonsammare behandling av mjöken än vid separering vid konventionell temperatur. En kallseparator 2 skiljer sig i princip från en vanlig separator genom att avståndet mellan skivorna är något större, eftersom kall grädde har en högre viskositet än den uppvärmda grädden.The incoming milk can optionally be stored in intermediate tanks, which storage takes place while maintaining the temperature. When the milk is to be treated, it is transported in a pipeline 1 to a separator 2. Separator 2 can be of a conventional type, but since it is not desired to heat the milk before separation, a so-called cold separator 2 is used. The milk is separated according to the invention at a temperature of 4-15 ° C, so a certain insignificant heating can take place before the milk reaches the separator 2. Experiments have shown that a certain, but negligible, increased fat content in the skim milk is obtained when separating at low temperatures. The advantage, however, is that you get a gentler treatment of the milk than when separating at conventional temperature. A cold separator 2 differs in principle from an ordinary separator in that the distance between the slices is slightly larger, since cold cream has a higher viscosity than the heated cream.
Genom separeringen erhåller man ut från separatorn 2, grädde i en ledning 3 och skummjök i en ledning 4. Såväl grädden som skummjölken håller en fortsatt låg temperatur av 4-15°C. Grädden leds i sin rörledning 3 till en standardiseringsutrustning 5 i vilken man kan få en exakt del grädde till återinblandning i skummjölken vilket ger en mjölkprodukt med önskad fetthalt. Överskottet av grädde leds i en rörledning 6 ut från standardiseringsutrustningen 5 för separat behandling.Through the separation, out of the separator 2, cream is obtained in a line 3 and skimmed milk in a line 4. Both the cream and the skimmed milk maintain a continued low temperature of 4-15 ° C. The cream is led in its pipeline 3 to a standardization equipment 5 in which one can get an exact part of cream for remixing in the skim milk, which gives a milk product with the desired fat content. The excess cream is led in a pipeline 6 out of the standardization equipment 5 for separate treatment.
Genom separering och standardisering vid den förhållandevis låga temperturen av 4-15°C, får man en betydligt skonsammare förbehandling av den mjölk som skall vidarebehandlas till UHT-mjölk. Konventionell mejerihantering och förbehandling av UHT-mjölk innebär varmseparering vid 55°C och oftast en förpastörisering vid 72°C under 15 sekunder, eller vid liknande tid-temperatur kombinationer. Dessa uppvärmningar innebär onödig temperaturpåverkan på mjölken som i ett senare skede 10 15 20 25 30 (CV u» 01 5 0 8 8 6 9 skall utsättas för betydligt högre temperaturer i avsikt att erhålla en kommersiellt steril produkt.By separation and standardization at the relatively low temperature of 4-15 ° C, a much gentler pre-treatment of the milk to be further processed into UHT milk is obtained. Conventional dairy handling and pre-treatment of UHT milk involves heat separation at 55 ° C and usually a pre-pasteurization at 72 ° C for 15 seconds, or at similar time-temperature combinations. These heatings have an unnecessary effect on the temperature of the milk which, at a later stage, must be exposed to significantly higher temperatures in order to obtain a commercially sterile product.
Fiörledning 4 med den i skummjölken äterinblandade grädden leds till en UHT- utrustning 7 av konventionell typ. UHT-utrustningen 7 innehåller vanligen ocksä en homogenisator vilken är placerad företrädesvis efter upphettningen av mjölken, med som ävenledes kan vara placerad före upphettningen. Homogeniseringen görs för att fä en mjölkprodukt där fettkulorna sönderdelats till smä, likstora fettkulor. Om mjölken inte homogeniseras fär man s.k. gräddsättning, d.v.s. fettkulorna, som är lättare, samlas i den övre delen av den färdiga förpackningen. Nästan all konsumtionsmjölk är idag homogeniserad.Conduction 4 with the cream mixed with the skimmed milk is led to a UHT equipment 7 of conventional type. The UHT equipment 7 usually also contains a homogenizer which is preferably placed after the heating of the milk, but which can also be placed before the heating. The homogenization is done to obtain a milk product where the fat globules are broken down into small, equal-sized fat globules. If the milk is not homogenized, you get so-called creaming, i.e. the fat balls, which are lighter, accumulate in the upper part of the finished package. Almost all drinking milk today is homogenized.
Själva UHT-behandlingen sker enligt uppfinningen genom att mjölken värms till en temperatur över 150°C under ett kort tidsintervall. Företrädesvis sker uppvärmningen till 150-175°C under en tid av O,1-2 sekunder, beroende pä avdödningskravet, dvs beroende pä den ingående mjölkens bakterie- och sporinnehäll.The UHT treatment itself takes place according to the invention by heating the milk to a temperature above 150 ° C for a short time interval. Preferably, the heating takes place to 150-175 ° C for a period of 0, 1-2 seconds, depending on the killing requirement, ie depending on the bacterial and spore content of the constituent milk.
Försök har visat att en uppvärmning enligt uppfinningen ger en produkt vilken uppfyller kraven pä kommersiell sterilitet. l en UHT-utrustning 7 av konventionell typ, kan uppvärmningen av mjölken antingen ske direkt genom änginjektion eller änginfusion eller indirekt genom att mjölken värmes i nägon form av värmeväxlare, eller med en kombination av dessa metoder.Experiments have shown that a heating according to the invention gives a product which meets the requirements of commercial sterility. In a UHT equipment 7 of conventional type, the heating of the milk can take place either directly by meadow injection or meadow infusion or indirectly by heating the milk in some form of heat exchanger, or with a combination of these methods.
Den färdigbehandlade mjölken transporteras i en rörledning 8 vidare till en eller flera förpackningsmasklner 9. Förpackningsmaskinerna 9 är aseptiska och kan t.ex. vara av den typ som förpackar mjölken i parallellepipediska förpackningsbehällare av engängstyp.The finished milk is transported in a pipeline 8 on to one or more packaging machines 9. The packaging machines 9 are aseptic and can e.g. be of the type that packs the milk in disposable parallelepiped packaging containers.
Vid viss UHT-behandling av mjölk kan man få viss instabilitet med avseende pä enzymaktivitet, vilket kan åtgärdas genom att mjölken efter UHT-behandlingen avkyles i ett eller flera steg vid temperaturer mellan 55-65°C i intervall mellan 2-10 minuter, exenpelvis 65°C under 5-8 minuter, varefter man kyler färdigt till förpackningstempertur.With some UHT treatment of milk, there may be some instability with respect to enzyme activity, which can be remedied by cooling the milk after the UHT treatment in one or more steps at temperatures between 55-65 ° C in intervals between 2-10 minutes, for example 65 ° C for 5-8 minutes, after which it is completely cooled to packaging temperature.
Enzyminaktiveringen kräver hällarceller av rörtyp eller liknande, vilka kan integreras i UHT-utrustningen 7.Enzyme inactivation requires tube-type pouring cells or the like, which can be integrated into the UHT equipment 7.
Genom uppvärmningen av mjölken förändras mjölken kemiskt, vilket gör att mjölkens smak förändras. Man eftersträvar således att en så liten kemisk päverkan som möjligt sker vid UHT-behandlingen av mjölken. Smak är en subjektiv faktor, men genom uppmätningar av lactulose i mjölken kan man indirekt fä ett mätt pä smakpäverkan. Desto högre temperaturbelastning som mjölken utsatts för, desto högre värde pä lactuloseinnehället i mjölken. Försök med förbehandling samt UHT- behandling av mjölk enligt uppfinningen har visat att man får lägre värden pä lactuloseinnehället och därmed indirekt en bättre smak på den färdiga UHT-mjölken. 508 869 Som framgått av ovanstående metod att behandla mjölken erhà||er man en aseptisk produkt, som genom den skonsamma behandlingen ger avsevärt förbättrade smakegenskaper.By heating the milk, the milk changes chemically, which changes the taste of the milk. The aim is thus to have as little chemical impact as possible during the UHT treatment of the milk. Taste is a subjective factor, but by measuring lactulose in the milk, one can indirectly get a measured effect on taste. The higher the temperature load to which the milk is exposed, the higher the value of the lactulose content in the milk. Experiments with pretreatment and UHT treatment of milk according to the invention have shown that lower lactulose content is obtained and thus indirectly a better taste of the finished UHT milk. 508 869 As shown by the above method of treating the milk, an aseptic product is obtained which, by the gentle treatment, gives considerably improved taste properties.
Claims (3)
Priority Applications (9)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE9700928A SE508869C2 (en) | 1997-03-14 | 1997-03-14 | Method for producing UHT milk with improved taste properties |
PCT/SE1998/000413 WO1998041102A1 (en) | 1997-03-14 | 1998-03-09 | A method of producing uht milk with improved flavour qualities |
EP98909915A EP0984702A1 (en) | 1997-03-14 | 1998-03-09 | A method of producing uht milk with improved flavour qualities |
CN98805117A CN1255832A (en) | 1997-03-14 | 1998-03-09 | Method of producing UHT milk with improved flavour qualities |
EA199900831A EA001568B1 (en) | 1997-03-14 | 1998-03-09 | A method of producing uht milk with improved flavour quantities |
AU64281/98A AU6428198A (en) | 1997-03-14 | 1998-03-09 | A method of producing uht milk with improved flavour qualities |
BR9808264-7A BR9808264A (en) | 1997-03-14 | 1998-03-09 | Process for the production of uht milk. |
US09/709,419 US6372276B1 (en) | 1997-03-14 | 2000-11-13 | Method for producing sterile, stable milk |
US09/883,247 US6652900B2 (en) | 1997-03-14 | 2001-06-19 | Method and plant for producing a sterile milk product |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE9700928A SE508869C2 (en) | 1997-03-14 | 1997-03-14 | Method for producing UHT milk with improved taste properties |
Publications (3)
Publication Number | Publication Date |
---|---|
SE9700928D0 SE9700928D0 (en) | 1997-03-14 |
SE9700928L SE9700928L (en) | 1998-09-15 |
SE508869C2 true SE508869C2 (en) | 1998-11-09 |
Family
ID=20406157
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SE9700928A SE508869C2 (en) | 1997-03-14 | 1997-03-14 | Method for producing UHT milk with improved taste properties |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP0984702A1 (en) |
CN (1) | CN1255832A (en) |
AU (1) | AU6428198A (en) |
BR (1) | BR9808264A (en) |
EA (1) | EA001568B1 (en) |
SE (1) | SE508869C2 (en) |
WO (1) | WO1998041102A1 (en) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6326044B1 (en) | 1997-06-19 | 2001-12-04 | Tetra Laval Holdings & Finance S.A. | Filter apparatus and method for the production of sterile skimmed milk |
US6652900B2 (en) | 1997-03-14 | 2003-11-25 | Tetra Laval Holdings & Finance S.A. | Method and plant for producing a sterile milk product |
US6372276B1 (en) | 1997-03-14 | 2002-04-16 | Tetra Laval Holdings & Finance S.A. | Method for producing sterile, stable milk |
US6737096B2 (en) | 2000-03-29 | 2004-05-18 | Tetra Laval Holdings & Finance S.A. | Method and apparatus for producing a sterile milk product |
SE521186C2 (en) | 2001-11-30 | 2003-10-07 | Tetra Laval Holdings & Finance | Method and apparatus for testing the cleaning efficiency of a filter in a filter system |
ES2528761T3 (en) * | 2010-03-25 | 2015-02-12 | Molkerei Alois Müller GmbH & Co. KG | Procedure for the manufacture of milk for the manufacture of cheeses from raw milk |
LT2988601T (en) | 2013-04-25 | 2017-07-10 | Arla Foods Amba | Improved milk and milk-related products |
CN103454301B (en) * | 2013-09-18 | 2015-12-23 | 宜兰食品工业股份有限公司 | The detection method of heat stability of protein in a kind of milk powder |
CN104670578A (en) * | 2013-11-30 | 2015-06-03 | 山东工大机械有限公司 | Instantaneous sterilizing type constant temperature device for beer |
DE102016200571B4 (en) * | 2016-01-18 | 2019-12-05 | Universität Hohenheim | Process for the production of long-life milk and stable milk produced by the process |
PL237308B1 (en) * | 2018-02-23 | 2021-04-06 | Okregowa Spoldzielnia Mleczarska W Lowiczu | Method for producing milk with extended shelf life and with increased content of vitamin D3 |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB8606524D0 (en) * | 1986-03-17 | 1986-04-23 | Mini Of Agricultural Fisheries | Deactivating heat stable enzymes |
SU1676568A1 (en) * | 1988-11-04 | 1991-09-15 | Всесоюзный Научно-Исследовательский И Экспериментально-Конструкторский Институт Продовольственного Машиностроения | Sterilize milk production method |
RU2048155C1 (en) * | 1992-01-27 | 1995-11-20 | Прокопенко Борис Евгеньевич | Continuous-action distiller |
-
1997
- 1997-03-14 SE SE9700928A patent/SE508869C2/en not_active IP Right Cessation
-
1998
- 1998-03-09 CN CN98805117A patent/CN1255832A/en active Pending
- 1998-03-09 BR BR9808264-7A patent/BR9808264A/en not_active Application Discontinuation
- 1998-03-09 WO PCT/SE1998/000413 patent/WO1998041102A1/en not_active Application Discontinuation
- 1998-03-09 EA EA199900831A patent/EA001568B1/en not_active IP Right Cessation
- 1998-03-09 EP EP98909915A patent/EP0984702A1/en not_active Withdrawn
- 1998-03-09 AU AU64281/98A patent/AU6428198A/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
SE9700928L (en) | 1998-09-15 |
WO1998041102A1 (en) | 1998-09-24 |
EA001568B1 (en) | 2001-04-23 |
EA199900831A1 (en) | 2000-04-24 |
BR9808264A (en) | 2000-05-16 |
CN1255832A (en) | 2000-06-07 |
AU6428198A (en) | 1998-10-12 |
SE9700928D0 (en) | 1997-03-14 |
EP0984702A1 (en) | 2000-03-15 |
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Legal Events
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NUG | Patent has lapsed |