WO2008058844A1 - Procédé pour la production de lait moyenne-longue conservation et appareil pour la mise en œuvre de ce procédé - Google Patents

Procédé pour la production de lait moyenne-longue conservation et appareil pour la mise en œuvre de ce procédé Download PDF

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Publication number
WO2008058844A1
WO2008058844A1 PCT/EP2007/061639 EP2007061639W WO2008058844A1 WO 2008058844 A1 WO2008058844 A1 WO 2008058844A1 EP 2007061639 W EP2007061639 W EP 2007061639W WO 2008058844 A1 WO2008058844 A1 WO 2008058844A1
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WO
WIPO (PCT)
Prior art keywords
milk
unit
temperature
skimming
heating
Prior art date
Application number
PCT/EP2007/061639
Other languages
English (en)
Inventor
Settimio Coacci
Carlo Coacci
Original Assignee
Zinco Di S. Coacci & C. S.A.S.
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
Publication date
Application filed by Zinco Di S. Coacci & C. S.A.S. filed Critical Zinco Di S. Coacci & C. S.A.S.
Priority to EP07821993A priority Critical patent/EP2099310A1/fr
Publication of WO2008058844A1 publication Critical patent/WO2008058844A1/fr

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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; 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
    • A23C3/0332—Preservation of milk or milk preparations by heating the materials being loose unpacked and progressively transported through the apparatus in contact with multiple heating plates
    • 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
    • A23C7/00—Other dairy technology
    • A23C7/04—Removing unwanted substances other than lactose or milk proteins from milk
    • A23C7/046—Removing unwanted substances other than lactose or milk proteins from milk by centrifugation without using chemicals, e.g. bactofugation; re-use of bactofugate
    • 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
    • A23C2210/00—Physical treatment of dairy products
    • A23C2210/25—Separating and blending
    • A23C2210/256—Removal or separation of bacteria, or a fraction containing bacteria, by centrifugation; Bactofugation

Definitions

  • the present invention relates to the technical milk dairy field, with particular reference to the apparatuses for the production of the UHT long life milk.
  • the UHT heat treatment includes heating the pasteurized milk to very high temperatures (above 135°C) for a time limited to few seconds, in order to destroy the microorganisms and deactivate the heat-resistant enzymes present therein; the resulting product has appreciable organoleptic and nutritional factors, and can be stored at ambient temperature in suitable aseptic packages for some months.
  • the raw, just milked milk is conveyed into suitable tanks, which are installed at the farm, and is kept there at a constant temperature of 4 - 5°C; every day or every two days the milk is moved to tank trucks
  • the chosen treatment is usually the pasteurizing, which includes: milk heating process, in order to eliminate dangerous microorganisms; and skimming operation, which allows to separate the high-fat part of milk from the low-fat part thereof, so as to obtain cream and whole, partially skimmed or skimmed milk.
  • the pasteurized milk can be stored for further 48 - 72 hours before another heat treatment takes place, for example UHT.
  • milk obtained from a pre-established mixture of lean milk (fat-free, obtained by skimming operation) with cream or whole milk, previously pasteurized is subjected to the UHT treatment, in order to obtain UHT whole, partially skimmed or skimmed milk.
  • pasteurization UHT
  • time/temperature ratios e.g. heating at 72°C for 15 seconds
  • milk of the same origin can have different organoleptic and biological factors, according to the heat treatments it has undergone.
  • the heat effect, or damage to the milk can be quantified by revealing analytical indexes, identified for this purpose, related to some substances present in the milk, in case of UHT milk, for example, it is especially lactulose and furosine; thus, their concentration gives the information about the quality of the final product, destined to be sold, since it allows to trace the treated milk "heat story", going back also to the technology used.
  • the enclosed Figure 1 is a schematic view of a known apparatus for the production of the UHT processed milk: the tank C contains pasteurized milk kept at constant temperature (for example at 4 0 C) and feeds a functional tank SF, of lower capacity; the milk is conveyed from here to a heat exchanger SCN (inlet IN-C) , where it is subjected to a given flow of heat, by direct or indirect heating, so as to reach high temperatures (above 135°C) for few seconds, and then cooled.
  • a heat exchanger SCN inlet IN-C
  • the exchanger SCN includes a channel, which has a forward run RA and backward run RR; the latter are separated by a conductive wall, to allow the heat exchange between the coming fluid (milk) , aimed at getting heated, and the return one, aimed at getting cooled.
  • a heat introduction unit UIC functionally interposed between the forward run RA and the backward run RR, includes for example a steam injection system or a steam infusion system (direct milk heating method) or milk heating system by application, for example, of steam to some portions of the exchanger SCN channel (indirect milk heating method) .
  • Figure 2 shows, in a qualitative way, the milk time- temperature characteristic during the UHT heat treatment: as it can be seen therefrom, the milk remains at higher temperatures, approximately at 90 0 C for a time ⁇ ti, sufficient to eliminate pathogenic germs and to reduce drastically the bacterial charge, as it is known.
  • the milk is conveyed for example to another functional tank SF, necessary to feed an associated unit UC, where the milk is packaged into aseptic containers; this way, the obtained milk can be preserved for at least two - three months at ambient temperature.
  • the milk can be also subjected to more pasteurization treatments, aimed at lengthening its storability before the UHT process, this can occur more frequently in case of pasteurized milk imported from other states.
  • the main object of the present invention is to propose a newly conceived method for the production of medium-long life milk, which is aimed at obtaining a final product of confirmed quality, higher with respect to milk obtained by similar technologies of known type.
  • the aim is to achieve this object by providing a method, which includes a series of essential working steps for obtaining, from still raw milk, medium-long life milk, especially of the UHT type, subjected on the whole to a smaller heat stress with respect to methods of known type, with the same storage time and microbial killing obtained.
  • Another object of the present invention is to propose a method, whose carrying out is relatively cheap with respect to the advantages to be obtained.
  • a further object of the invention is to propose an apparatus for the production of medium-long life milk, in particular of the UHT processed type, which is newly conceived, reliable, functional and that allows obtaining a final product of higher quality than the product currently obtained with apparatuses of known type, since, on the whole, it is destined to be subjected to a smaller heat stress.
  • Another object of the present invention is to propose an apparatus, whose costs are relatively low with respect to the advantages to be obtained.
  • a method for the production of medium-long life milk from raw milk characterized in that it includes the subsequent steps: - heating said raw milk up to a first temperature; skimming the milk heated up to said first temperature, to separate a pre-selected quantity of fat; further rising the temperature of the so obtained milk, up to a second temperature, for a pre-selected time, so as to reduce microbes and make said milk suitable for storage, for consumption purposes and in sterile containers, for at least two weeks; cooling said milk; and packaging the milk into said sterile containers.
  • an apparatus for production of medium-long life milk including a tank for containment of raw milk, the apparatus being characterized in that it further includes: a first unit for heating the milk, coming from said tank, up to a first temperature; a unit, arranged functionally in cascade with said first unit, for skimming said milk, heated to said first temperature, with consequent separation of a pre-selected quantity of fat; a second unit, in turn arranged functionally in cascade with said skimming unit, for further rising the temperature of the milk obtained by skimming up to a second temperature for a certain time, so as to reduce microbes and make said milk suitable for storage, for consumption purposes, for at least two weeks; and a unit for packaging milk, connected functionally in cascade to said second unit.
  • Figure 2 shows, in a qualitative way, a c, which describes a milk UHT heat treatment, from pasteurized milk at 4°C;
  • Figure 3 shows, in a qualitative way, a temperature- time feature, which describes a UHT heat treatment of milk obtained according to the invention, from raw milk at 4°C;
  • - Figure 4 is a functional block diagram of the apparatus proposed by the present invention, according to a first embodiment
  • Figure 5 is a schematic, enlarged view of a particularly significant element of Figure 4;
  • - Figure 6 is a functional block diagram of the apparatus proposed by the present invention, according to another embodiment;
  • the reference C indicates a tank containing raw milk at a constant temperature, for example 4°C, not yet heat treated, i.e. not yet subjected to any heating process
  • the reference SF indicates functional tanks, situated in some points of the proposed apparatus, in which functional introduction can be required for the plant good operation, as known to those skilled in the field.
  • the reference SC indicates a heat exchanger, which is connected to the functional tanks SF by conventional inlet IN-C and outlet OUT-C, in turn connected respectively to a tank C and to the unit UC of known type for milk packaging; said exchanger SC is different from the known one SCN, described in Figure 1, in that it includes, in a portion of the forward run, a deviation of the whole fluid (milk) outward of the exchanger SC, through an additional outlet OUT-A and a subsequent introduction of the fluid downstream, along the same forward run, through an additional inlet IN-A.
  • a first forward run RA x is defined, included between the conventional inlet IN-C and the additional outlet OUT-A, along which the milk is aimed to get heated up to a first temperature T 1 (see below), a short inactive section TI (indicated with a broken line and present only in case, in which the exchanger SC is obtained by adapting of a pre-existing exchanger, of known type SCN), and a second forward run RA 2 , originating from the first additional inlet IN-A.
  • a heat introduction unit UIC situated functionally between the second forward run RA 2 and the backward run RR, includes for example a steam injection system or a steam infusion system (direct milk heating method) or by a system of milk heating by application for example, of steam to some portions of the exchanger SC channel (indirect milk heating method) .
  • the reference US indicates a skimming unit of known type, which receives at its inlet I-US the milk heated to the first temperature I 1 , coming from the additional outlet OUT-A, and supplies at the outlet, from one side, milk containing a prefixed percentage of fat, coinciding with whole, partially skimmed or skimmed milk, and, from the other side, exceeding fat aimed at supplying a unit UPP for the production of cream, likewise of known type; which is obtained in known way, for example by a separating device S, that separates the high-fat part of milk from the low-fat part, and a titrator device T, that allows to recombine the lean milk with a part of fat according to prefixed percentage, to obtain whole, partially skimmed or skimmed milk.
  • the reference B indicates a device of known type, for the bactofugation of the whole, partially skimmed or skimmed
  • the operation of the apparatus proposed by the present invention will be described in the following, with constant reference to the qualitative time-temperature characteristic of Figure 3.
  • the raw milk in the inlet of the heat exchanger SC (conventional inlet IN-C) is conveyed along the first forward run RA 1 , along which it is heated up to a first temperature T x , included within a range of 50 - 60 0 C.
  • the milk goes out of the heat exchanger SC and feeds the skimming unit US through the functional tank SF; the milk going out of the skimming unit US (U-US outlet in Figure 4), whole, partially skimmed or skimmed, is sent to the inlet of the bactofugation device B, which, as it is known, acts as a certain destroyer of the microbial charge contained in the milk, through a centrifugal process.
  • the milk is not subjected to any heat treatment and it can be supposed to be maintained substantially at the same first temperature I 1 .
  • the milk leaving the bactofugation device B and the associated functional tank SF is conveyed again into the heat exchanger SC through the second forward run RA 2 , where, before reaching the heat introduction unit UIC, it is heated again up to a temperature of, for example, 90 0 C.
  • the UIC unit causes a rapid rise of the milk temperature up to a second temperature T 2 , for example of 140 0 C, for a very limited time ⁇ t 2 , followed by a rapid cooling up to a temperature, near, for example to 90 0 C.
  • the apparatus proposed by the invention, delivers advantageously less heat with high temperatures with respect to prior art technologies.
  • the milk leaving the UIC unit has the temperature of, for example, 90 0 C; it is conveyed along the backward run RR of the heat exchanger SC, where it is further cooled, so as to be conveyed into the functional tank SF and then packaged into sterile containers of the packaging unit UC
  • the above description characterizes the method for the production of medium-long life milk, likewise proposed by the present invention, including the following steps, in the order: heating the raw milk up to a first temperature I 1 ; - skimming the heated milk, to separate it from a preselected quantity of fat, to obtain for example whole, partially skimmed or skimmed milk, thus completing the pasteurization process; bactofugation of the so obtained milk, so as to obtain a certain microbial presence reduction; heating of the milk up to a temperature of, for example, 90 0 C; further rapid heating of the milk (UHT) up to the second temperature T 2 , for example of 140 0 C, followed by a rapid cooling of the milk up a temperature of about, for example 90 0 C; subsequent cooling of the milk, including a homogenization step of known type, and its packaging into sterile containers.
  • the milk rapid heating up to the second temperature T 2 is carried out in order to complete the microbial presence reduction, according to regulatory standards, so as to obtain safe food, which can be stored in sterile packages for at least two - three months; due to the previous bactofugation operation, operated mechanically, reducing in itself in substantial way the microbial charge, the subsequent required heat delivery is very moderate with respect to the prior art (actually, it continues for a very limited time ⁇ t 2 ) , and consequently, so is the resulting heat damage. It is pointed out that the heat delivery is really lower than the one necessary with a normal direct or indirect heating method, if the bactofugation should not be provided. The resulting considerable advantage lies in a much lower milk heat stress with respect to what happens with known processes, in accordance with registered low lactulose and furosine values, which prove the high quality of the so obtained milk, from the organoleptic and nutritional point of view.
  • the pasteurization process is only one and is performed in the same apparatus, in which the UHT treatment is performed, from the raw milk; whereas, in prior art, the milk could have been subjected to further pasteurization treatments in different places, and was transferred between the apparatuses for milk pasteurization and apparatuses for UHT process, and consequently even many days might pass from the milking step to the final packaging one.
  • a further advantage of the invention lies in the possibility to obtain the apparatus proposed by the present invention by easy adapting of apparatuses of known type, like the one shown in Figure 1; actually, in this case, it is possible to use the exchanger SCN of known type, with some simple changes applied thereto, thus making it equivalent to the heat exchanger SC shown in Figures 4, 5.
  • the pre-existing apparatuses can be modified at small costs, so as to carry out the present invention.
  • the proposed apparatus is not only aimed at the production of the UHT long life milk; it is possible, by controlling the heat delivery by the UIC unit (with both direct and indirect heating) , to obtain milk, that can be stored in sterile packages for few weeks, for example, at least two.
  • Another advantage of the invention lies in the fact that it has defined a functional, reliable apparatus, that can be easily obtained from the pre-existing apparatuses by simple adapting operations.
  • a further advantage of the present invention lies in the fact, that it has conceived an apparatus for the production of medium-long life milk, whose costs are relatively low with respect to the obtained advantages.
  • a further advantage of the present invention lies in the fact, that it has created a method for the production of medium-long life milk, which is newly conceived and which allows to obtain a final product of confirmed higher quality with respect to the similar technologies of known type. This has been achieved by having contrived a method, which includes a sequence of essential working steps, that obtain, beginning from raw milk, medium-long life milk, in particular of the UHT processed type, which is subjected on the whole to a lower heat stress with respect to the methods of known type, with the same storage time and microbial reduction obtained.
  • a further advantage of the present invention lies in the fact, that it has defined a method for the production of medium-long life milk, whose essential steps allow, with respect to the solutions of known type, to obtain a considerable energy saving, because the pasteurization, bactofugation and the final UHT treatment steps take place one after another during the same production cycle.
  • a yet further advantage of the present invention lies in the fact, that it has defined a method, that is carried out at the relatively limited costs with respect to the obtained advantages.
  • the bactofugation device B can be situated upstream of the skimming unit US (this variant has not been shown in Figures) , instead of downstream; then, the device B can be substituted with a milk microfiltration device of known type, not shown in the enclosed Figures, situated upstream or downstream of the skimming unit US .
  • the method proposed by the invention can include the bactofugation step before the milk skimming; the bactofugation step, provided before or after skimming, can be likewise substituted with a milk microfiltration step, of known type.
  • a first heating unit Ui functionally interposed between the functional tanks SF, associated to the tank C and the skimming unit US, respectively, for heating the milk up to the first temperature T 1
  • a second unit U 2 situated downstream of the bactofugation device B and aimed at carrying out the same heat treatments as described above, which before were carried out in the second forward run RA 2 , inside the UIC unit and inside the backward run RR.
  • the first unit U 1 and the second unit U 2 functionally equivalent to the heat exchanger SC, have not been shown in the enclosed figures.
  • Another method for the production of medium-long life milk is defined from what has been said in relation to the embodiment, likewise remaining within the protective scope of the present invention, and including as follows: heating the raw milk up to a first temperature T 1 ; skimming the heated milk, to separate it from a preselected quantity of fat; so as to obtain whole, partially skimmed or skimmed milk, thus completing the pasteurization process; - heating of milk up to a temperature of, for example, 90 0 C; further heating of milk (UHT) , up to a second temperature T 2 , for example of 140 0 C, followed by its cooling up to a temperature of about, for example, again 90 0 C: the duration of this step is substantially equal to ⁇ ti; a subsequent cooling of milk, including a homogenization step of known type, and its packaging into sterile containers.
  • This embodiment of the apparatus, and the resulting working steps, differ from the first embodiment in that they include a longer UHT heat treatment, at high temperatures, to which corresponds a bigger heat delivery, with the same microbe reduction obtained; besides this, all the advantageous technical-functional characteristic features of the invention, pointed out above, remain valid.

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  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Dairy Products (AREA)

Abstract

L'invention concerne un procédé pour la production de lait moyenne-longue conservation, avec des facteurs de qualité supérieure, puisqu'il est obtenu à partir de lait cru uniquement, par des étapes de cycle de traitement et de traitement thermique, bactofugation et titration. Le procédé comprend les opérations consistant à : chauffer le lait cru jusqu'à une première température T1 ; écrémer le lait ; bactofugation ; nouvelle élévation de la température du lait jusqu'à une seconde température T2 pendant un temps limité, pour obtenir une réduction des microbes pour rendre le lait approprié pour le stockage, pour des objectifs de consommation et dans des conteneurs stériles, pendant au moins deux-trois mois ; refroidir et conditionner le lait ainsi obtenu.
PCT/EP2007/061639 2006-11-16 2007-10-30 Procédé pour la production de lait moyenne-longue conservation et appareil pour la mise en œuvre de ce procédé WO2008058844A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP07821993A EP2099310A1 (fr) 2006-11-16 2007-10-30 Procédé pour la production de lait moyenne-longue conservation et appareil pour la mise en uvre de ce procédé

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ITBO2006A000782 2006-11-16
ITBO20060782 ITBO20060782A1 (it) 2006-11-16 2006-11-16 Metodo per la produzione di latte a medio-lunga conservazione ed apparato destinato ad attuarlo

Publications (1)

Publication Number Publication Date
WO2008058844A1 true WO2008058844A1 (fr) 2008-05-22

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Country Status (3)

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EP (1) EP2099310A1 (fr)
IT (1) ITBO20060782A1 (fr)
WO (1) WO2008058844A1 (fr)

Cited By (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102010025664A1 (de) * 2010-06-30 2012-01-05 Unternehmensgruppe Theo Müller GmbH & Co. KG Verfahren und Vorrichtung zum Herstellen von haltbarer Milch
WO2013089563A1 (fr) * 2011-12-15 2013-06-20 Tine Sa Procédé de production de lait ou de produits laitiers
RU2566566C1 (ru) * 2014-02-07 2015-10-27 ТОО "Марс-2" Рекомбинированное молоко, пастеризованное 1,5 % жирности и способ его производства
RU2580644C2 (ru) * 2014-02-07 2016-04-10 ТОО "Марс-2" Сгущенный молочный продукт из рекомбинированного молока и способ его производства
RU2579680C2 (ru) * 2014-02-07 2016-04-10 ТОО "Марс-2" Cыр из рекомбинированного молока и способ его производства
RU2579682C2 (ru) * 2014-02-07 2016-04-10 ТОО "Марс-2" Йогуртовый напиток из рекомбинированного молока и способ его производства
RU2579696C2 (ru) * 2014-02-07 2016-04-10 ТОО "Марс-2" Молочный продукт пастеризованный из рекомбинированного молока и способ его производства
RU2579686C2 (ru) * 2014-02-07 2016-04-10 ТОО "Марс-2" Молочный продукт стерилизованный и способ его производства
RU2579685C2 (ru) * 2014-02-07 2016-04-10 ТОО "Марс-2" Сливки из рекомбинированного молока и способ их производства
RU2579674C2 (ru) * 2014-02-07 2016-04-10 ТОО "Марс-2" Молочный продукт из рекомбинированного молока и способ его производства
RU2595413C2 (ru) * 2014-02-07 2016-08-27 ТОО "Марс-2" Сгущенное рекомбинированное молоко и способ его производства
RU2595419C2 (ru) * 2014-02-07 2016-08-27 ТОО "Марс-2" Рекомбинированное молоко стерилизованное 3,5% жирности и способ его производства
RU2595417C2 (ru) * 2014-02-07 2016-08-27 Товарищество с ограниченной ответственностью "Марс-2" Рекомбинированное молоко 0,5% жирности, стерилизованное и способ его производства
RU2595416C2 (ru) * 2014-02-07 2016-08-27 ТОО "Марс-2" Молочный продукт и способ его производства
RU2595411C2 (ru) * 2014-02-07 2016-08-27 ТОО "Марс-2" Йогуртовый напиток 1,4 % жирности из рекомбинированного молока и способ его производства
RU2595414C2 (ru) * 2014-02-07 2016-08-27 ТОО "Марс-2" Молочный продукт из рекомбинированного молока и способ его производства
RU2595418C2 (ru) * 2014-02-07 2016-08-27 ТОО "Марс-2" Молочный продукт 1,5% жирности из рекомбинированного молока и способ его производства
RU2595412C2 (ru) * 2014-02-07 2016-08-27 ТОО "Марс-2" Йогуртовый напиток 3,5 % жирности из рекомбинированного молока и способ его производства
RU2596407C2 (ru) * 2014-02-07 2016-09-10 ТОО "Марс-2" Рекомбинированные сливки, обработанные ультравысокой температурой, 30 % жирности и способ их производства
RU2601130C2 (ru) * 2014-02-07 2016-10-27 Товарищество с ограниченной ответственностью "Марс-2" Рекомбинированные сливки 38 % жирности из рекомбинированного молока и способ их производства
RU2601127C2 (ru) * 2014-02-07 2016-10-27 Товарищество с ограниченной ответственностью "Марс-2" Йогурт 1,5% жирности из рекомбинированного молока и способ его производства
US10285412B2 (en) 2009-09-16 2019-05-14 Gea Mechanical Equipment Gmbh Method for producing fresh milk having a longer shelf life

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WO2002069724A1 (fr) * 2001-03-08 2002-09-12 Tetra Laval Holdings & Finance Sa Procede de pretraitement du lait prealable a la microfiltration

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Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2477502B2 (fr) † 2009-09-16 2020-01-01 GEA Mechanical Equipment GmbH Procédé de production de lait frais à conservation prolongée
US10285412B2 (en) 2009-09-16 2019-05-14 Gea Mechanical Equipment Gmbh Method for producing fresh milk having a longer shelf life
DE102010025664A1 (de) * 2010-06-30 2012-01-05 Unternehmensgruppe Theo Müller GmbH & Co. KG Verfahren und Vorrichtung zum Herstellen von haltbarer Milch
WO2013089563A1 (fr) * 2011-12-15 2013-06-20 Tine Sa Procédé de production de lait ou de produits laitiers
RU2595413C2 (ru) * 2014-02-07 2016-08-27 ТОО "Марс-2" Сгущенное рекомбинированное молоко и способ его производства
RU2595416C2 (ru) * 2014-02-07 2016-08-27 ТОО "Марс-2" Молочный продукт и способ его производства
RU2579696C2 (ru) * 2014-02-07 2016-04-10 ТОО "Марс-2" Молочный продукт пастеризованный из рекомбинированного молока и способ его производства
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