DK2989897T3 - Fremgangsmåde til fremstilling af farveløs ostemælk - Google Patents

Fremgangsmåde til fremstilling af farveløs ostemælk Download PDF

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Publication number
DK2989897T3
DK2989897T3 DK14182971.3T DK14182971T DK2989897T3 DK 2989897 T3 DK2989897 T3 DK 2989897T3 DK 14182971 T DK14182971 T DK 14182971T DK 2989897 T3 DK2989897 T3 DK 2989897T3
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DK
Denmark
Prior art keywords
retentate
milk
cheese
permeate
ultrafiltration
Prior art date
Application number
DK14182971.3T
Other languages
English (en)
Inventor
Sven-Rainer Döring
Original Assignee
Dmk Deutsches Milchkontor Gmbh
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
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Application filed by Dmk Deutsches Milchkontor Gmbh filed Critical Dmk Deutsches Milchkontor Gmbh
Application granted granted Critical
Publication of DK2989897T3 publication Critical patent/DK2989897T3/da

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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; PREPARATION THEREOF
    • A23C19/00—Cheese; Cheese preparations; Making thereof
    • 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; PREPARATION THEREOF
    • A23C19/00—Cheese; Cheese preparations; Making thereof
    • A23C19/02—Making cheese curd
    • A23C19/05—Treating milk before coagulation; Separating whey from curd
    • 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; PREPARATION THEREOF
    • A23C7/00—Other dairy technology
    • A23C7/04—Removing unwanted substances other than lactose or milk proteins from milk
    • A23C7/043—Removing unwanted substances other than lactose or milk proteins from milk using chemicals in liquid or solid state, e.g. flocculating, adsorbing or extracting agents
    • 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; PREPARATION THEREOF
    • A23C9/00—Milk preparations; Milk powder or milk powder preparations
    • A23C9/14—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment
    • A23C9/142—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment by dialysis, reverse osmosis or ultrafiltration
    • A23C9/1422—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment by dialysis, reverse osmosis or ultrafiltration by ultrafiltration, microfiltration or diafiltration of milk, e.g. for separating protein and lactose; Treatment of the UF permeate
    • 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; PREPARATION THEREOF
    • A23C9/00—Milk preparations; Milk powder or milk powder preparations
    • A23C9/14—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment
    • A23C9/142—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment by dialysis, reverse osmosis or ultrafiltration
    • A23C9/1427—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment by dialysis, reverse osmosis or ultrafiltration by dialysis, reverse osmosis or hyperfiltration, e.g. for concentrating or desalting
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/025—Reverse osmosis; Hyperfiltration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14—Ultrafiltration; Microfiltration
    • B01D61/145—Ultrafiltration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/08—Flat membrane modules
    • B01D63/082—Flat membrane modules comprising a stack of flat membranes
    • B01D63/0822—Plate-and-frame devices
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/10—Spiral-wound membrane modules
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/66—Polymers having sulfur in the main chain, with or without nitrogen, oxygen or carbon only
    • B01D71/68—Polysulfones; Polyethersulfones
    • 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; PREPARATION THEREOF
    • A23C2210/00—Physical treatment of dairy products
    • A23C2210/20—Treatment using membranes, including sterile filtration
    • A23C2210/206—Membrane filtration of a permeate obtained by ultrafiltration, nanofiltration or microfiltration
    • 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; PREPARATION THEREOF
    • A23C2210/00—Physical treatment of dairy products
    • A23C2210/25—Separating and blending
    • A23C2210/252—Separating a milk product in at least two fractions followed by treatment of at least one of the fractions and remixing at least part of the two fractions

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Water Supply & Treatment (AREA)
  • General Chemical & Material Sciences (AREA)
  • Nanotechnology (AREA)
  • Dairy Products (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Claims (10)

1. Fremgangsmåde til fremstillingen af farveløs ostemælk, i hvilken (a) ostemælk udsættes for en ultrafiltrering og hvorved et første permeat PI og et første retentat RI fremstilles, hvor ultrafiltreringen udføres under anvendelse af membraner, der har en porediameter fra 5,000 til 50,000 Dalton, (b) permeatet PI udsættes for en omvendt osmose og hvorved et andet permeat P2 og et andet retentat R2 fremstilles, hvor den omvendte osmose udføres under anvendelse af semipermeable membraner, der har en selektivitet fra 10 til 1,000 Dalton, (c) det andet retentat R2 behandles med et adsorptionsmiddel og hvorved et yderligere retentat R2* fremstilles, (d) det således opnåede retentat R2* kombineres med retentatet RI og permeatet P2.
2. Fremgangsmåde ifølge krav 1, kendetegnet ved, at ultrafiltreringen (trin a) udføres ved en temperatur i området fra 10 til 55 °C.
3. Fremgangsmåde ifølge krav 2, kendetegnet ved, at ultrafiltreringen (trin a) udføres ved en temperatur i området fra 12 til 20 °C.
4. Fremgangsmåde ifølge mindst ét af kravene 1 til 3, kendetegnet ved, at ultrafiltreringen (trin a) udføres under anvendelse af spiralviklede membraner eller plade-ramme-moduler lavet af polysulfon eller polyethylenmembraner.
5. Fremgangsmåde ifølge mindst ét af kravene 1 til 4, kendetegnet ved, at den omvendte osmose (trin b) udføres ved en temperatur i området fra 10 til 55 °C.
6. Fremgangsmåde ifølge mindst ét af kravene 1 til 5, kendetegnet ved, at det anvendte adsorptionsmiddel er aktivt kul.
7. Fremgangsmåde ifølge mindst ét af kravene 1 til 6, kendetegnet ved, at det anvendte adsorptionsmiddel er et ionbytterresin.
8. Fremgangsmåde ifølge mindst ét af kravene 1 til 7, kendetegnet ved, at adsorptionen udføres ved temperaturer i området fra 10 til 55 °C.
9. Fremgangsmåde til udvinding af riboflavin, i hvilken (a) ostemælk udsættes for en ultrafiltrering og hvorved et første permeat PI og et første retentat RI fremstilles, hvor ultrafiltreringen udføres under anvendelse af membraner der har en porediameter fra 5,000 til 50,000 Dalton, (b) permeatet PI udsættes for en omvendt osmose og hvorved et andet permeat P2 og et andet retentat R2 fremstilles, hvor den omvendte osmose udføres under anvendelse af semipermeable membraner der har en selektivitet fra 10 til 1,000 Dalton, (c) det andet riboflavin-indeholdende retentat R2 behandles med et adsorptionsmiddel og hvorved et yderligere retentat R2* fremstilles, hvor det anvendte adsorptionsmiddel er aktivt kul, og (d) adsorptionsmidlet behandles med et egnet desorptionsmiddel, hvor mængden af riboflavin opløst deri desorberes og isoleres ved at skille desorptionsmidlet fra.
10. Fremgangsmåde ifølge krav 9, kendetegnet ved, at det anvendte desorptionsmiddel er ethanol eller isopropylalkohol.
DK14182971.3T 2014-08-30 2014-08-30 Fremgangsmåde til fremstilling af farveløs ostemælk DK2989897T3 (da)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP14182971.3A EP2989897B1 (de) 2014-08-30 2014-08-30 Verfahren zur Herstellung von farbloser Kesselmilch

Publications (1)

Publication Number Publication Date
DK2989897T3 true DK2989897T3 (da) 2018-05-07

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
DK14182971.3T DK2989897T3 (da) 2014-08-30 2014-08-30 Fremgangsmåde til fremstilling af farveløs ostemælk

Country Status (4)

Country Link
US (1) US20160058026A1 (da)
EP (1) EP2989897B1 (da)
CN (1) CN105519671A (da)
DK (1) DK2989897T3 (da)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DK3583853T3 (da) * 2018-06-18 2021-04-12 Dmk Deutsches Milchkontor Gmbh Fremgangsmåde til fremstilling af sur valle med formindsket lactoseindhold

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5238106B2 (da) * 1973-03-09 1977-09-27
NL7808199A (nl) * 1978-08-04 1980-02-06 Stichting Bedrijven Van Het Werkwijze voor het concentreren van wei of van ultra- filtratiepermeaat van wei of melk.
FI864637A7 (fi) * 1986-06-04 1987-12-05 Dairy Technology Ltd Yksivaiheinen laktoosin valmistusmenetelmä.
DE3942028A1 (de) * 1989-12-20 1991-06-27 Kali Chemie Ag Verfahren zur fraktionierung von milch oder milcherzeugnissen
GB9212718D0 (en) * 1992-06-16 1992-07-29 Rohm & Haas Treatment of food products and by-products
WO1994012268A1 (en) * 1992-11-27 1994-06-09 Napro Biotherapeutics, Inc. Processing taxane solutes using membranes
JPH06225776A (ja) * 1992-12-07 1994-08-16 Kyowa Hakko Kogyo Co Ltd リボフラビンの製造法
WO1999015023A2 (en) * 1997-09-22 1999-04-01 Kiwi Co-Operative Dairies Limited Recovery process
US20020001651A1 (en) * 2000-01-24 2002-01-03 Norris Leslie Marie Method of altering and improving taste characteristics of edible consumables with monomeric or oligomeric polyphenolic compounds
DE10036085C1 (de) 2000-07-25 2002-01-24 Westfalia Separator Food Tec G Verfahren zur Entkeimung von Milch
US20030026845A1 (en) * 2001-06-18 2003-02-06 Etzel Lisa R. Process for preparing protein isolate from milk, whey, colostrum, and the like
US8449938B2 (en) * 2002-05-14 2013-05-28 Valio Ltd Lactose-free milk product and processes for producing the same
US7169428B2 (en) * 2002-08-27 2007-01-30 Select Milk Producers Inc. Dairy compositions and method of making
CN1806668A (zh) * 2005-01-19 2006-07-26 吉林省高等院校科技开发研究中心 从蚕豆、绿豆淀粉加工排放水中提取复合保健功能因子的方法
DK176760B1 (da) * 2007-10-03 2009-06-29 Arla Foods Amba Process for producing lactose-free milk
US8986768B2 (en) * 2008-08-29 2015-03-24 Valio Ltd. Low-lactose and lactose-free milk product and process for production thereof

Also Published As

Publication number Publication date
EP2989897A1 (de) 2016-03-02
EP2989897B1 (de) 2018-02-21
CN105519671A (zh) 2016-04-27
US20160058026A1 (en) 2016-03-03

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