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Sommaire du brevet 2143938 

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Disponibilité de l'Abrégé et des Revendications

L'apparition de différences dans le texte et l'image des Revendications et de l'Abrégé dépend du moment auquel le document est publié. Les textes des Revendications et de l'Abrégé sont affichés :

  • lorsque la demande peut être examinée par le public;
  • lorsque le brevet est émis (délivrance).
(12) Demande de brevet: (11) CA 2143938
(54) Titre français: METHODE POUR L'OBTENTION DE PRODUITS GRAS A FAIBLE TENEUR EN MATIERES GRASSES
(54) Titre anglais: METHOD OF PRODUCING A FAT PRODUCT WITH A REDUCED FAT CONTENT
Statut: Réputée abandonnée et au-delà du délai pour le rétablissement - en attente de la réponse à l’avis de communication rejetée
Données bibliographiques
(51) Classification internationale des brevets (CIB):
  • A23C 15/16 (2006.01)
  • A01J 15/00 (2006.01)
(72) Inventeurs :
  • ARPH, STEN-OLOF (Suède)
  • LARSSON, MAGNUS (Suède)
(73) Titulaires :
  • ALFA LAVAL AB
(71) Demandeurs :
  • ALFA LAVAL AB (Suède)
(74) Agent: BORDEN LADNER GERVAIS LLP
(74) Co-agent:
(45) Délivré:
(86) Date de dépôt PCT: 1993-09-03
(87) Mise à la disponibilité du public: 1994-03-17
Licence disponible: S.O.
Cédé au domaine public: S.O.
(25) Langue des documents déposés: Anglais

Traité de coopération en matière de brevets (PCT): Oui
(86) Numéro de la demande PCT: PCT/SE1993/000716
(87) Numéro de publication internationale PCT: SE1993000716
(85) Entrée nationale: 1995-03-06

(30) Données de priorité de la demande:
Numéro de la demande Pays / territoire Date
9202574-1 (Suède) 1992-09-08

Abrégés

Abrégé anglais


A fat product containing milk fat with a reduced fat content is produced by mixing cream with a fat content of 40-80 %
with a desired amount of water phase containing stabilizing means and salt. The temperature is kept between 50-80° C during the
mixing operation. The obtained mixture, an oil-in-water emulsion, is cooled and worked in such a way that phase reversal takes
place. A partial stream of phase reversed product, now a water-in-oil emulsion, is returned to the inlet of a first cooling step and
is mixed with the starting mixture. The obtained end product consists of a stable water-in-oil emulsion. The product only contains
milk fat and has a fat content of 25-60 %. It contains only emulsifiers naturally occurring in the cream and has a casein content
below 2 %.

Revendications

Note : Les revendications sont présentées dans la langue officielle dans laquelle elles ont été soumises.


Claims
1. Method of producing a fat product with a reduced fat
content containing milk fat, c h a r a c t e r i z e d
in that cream with a fat content of 40-80 % is mixed
with a desired amount of water phase containing
stabilizing means and salt, at which the temperature
during the mixing operation is kept between 50-80°C,
after which the obtained mixture, an oil-in-water
emulsion, is cooled and worked in such a way that phase
reversal takes place, at which a partial stream of phase
reversed product, now a water-in-oil emulsion, is
returned to the inlet of a first cooling step and mixed
with the starting mixture and that the obtained end
product consists of a stable water-in-oil-emulsion,
which product only contains milk fat and has a fat
content of 25-60% and only contains emulsifiers
naturally occuring in the cream and has a casein content
below 2 %.
2. Method according to claim 1, c h a r a c t e -
r i z e d in that 5-50 %, preferably 5-25 % of the
amount of phase reversed product is returned to the
inlet of the first cooling step.
3. Method according to claim 1-2, c h a r a c t e -
r i z e d in that wholly or partly phase reversed
product from a first or a second working step is
returned to the inlet of the first cooling step.

Description

Note : Les descriptions sont présentées dans la langue officielle dans laquelle elles ont été soumises.


W 0 94/OS160 21~ 3 9 3 8 P ~ /SE93/00716
Method of producing a fat product with a reduced fat content
The present invention relates to a method of producing a
fat product containing milk fat with a reduced fat
content.
The interest in fat products based on milk fat or
mixtures of milk fat and vegetable oil is rising.
Hitherto one has often started with butter oil possibly
mixed with vegetable oil into which fat mixture a water
phase is admixed. The water phase may contain casein or
caseinate, skim milk powder or milk protein, whey
protein and possibly gelatin.
The content of dry solids in the water phase which is
mixed with the fat phase has been high in order to bind
the water in a sufficient high degree so that the end
product, a water-in-oil-emulsion shall be stable and not
give off free water.
Processes for production of products with a low fat
content starting from butter, have also been presented,
in which a water phase is mixed into earlier produced
butter. Such processes are described for example in
W0 91/07098 and in EP 368805.
During recent times patent applications have been
published which describe processes where products
containing milk fat are produced starting from cream
without any churning step. In EP 376407 there is
described a process for producing a fat product from
water, melted vegetable oils and cream. Similar
processes are also described in EP 385542 and EP 445857.
In order to obtain stable emulsions, emulsifiers are
SUBSTITUTE S~IEET

W094/05160 ~93~ PCT/SE93/00
added to the mixture of cream, vegetable fat and water
prior to the phase reversal.
When producing fat products containing only milk fat
starting from cream there is sometimes a problem to
obtain the desired phase reversal from the oil-in-water
emulsion, the cream, to the desired water-in-oil
emulsion which is the desired state for the fat product.
These problems are more accentuated when the fat content
of the fat mixture is low.
The present invention relates to a method to obtain a
satisfactory and stable phase reversal when producing a
fat product only containing milk fat.
The method according to the invention is mainly charac-
terized in that cream with a fat content of 40-80 % is
mixed with a desired amount of water phase containing
stabilizing means, preferably gelatin, salt and aroma
substances. The temperature during the mixing step is
kept between 50-80C. After the mixing operation the
mixture, an oil-in-water emulsion, is cooled and worked
such that phase reversal takes place. A partial stream
of phase reversed product, now a water-in-oil emulsion,
is returned to the inlet of a first cooling step and
mixed with the starting mixture. The obtained end
product consists of a stable water-in-oil emulsion. The
product has a fat content of 25-60 % and contains only
emulsifiers naturally occuring in the cream. The casein
content of the product is below 2 %.
When the expression % is mentioned in the description
weight percent is intended, if nothing else is said.
S~JBSTITUTE S~EE~ET

W O 94/05160 2 1 9 3 9 3 8 PC~r/SE93/00716
According to the invention 5-50 %, preferably 5-25 %, of
the amount of phase reversed product is returned to the
inlet of the first cooling step. A fat mixture with a
lower fat content brings about larger problems for the
phase reversal and in order to obtain a stable phase
reversal a larger amount is recirculated when the fat
mixture contains a smaller amount of fat.
The amount of phase reversed product which is returned
to the inlet of the first cooling step bears an inverted
relation to the fat content in the end product. With a
low fat content of the same a higher amount of phase
reversed product is returned, at a higher fat content
the amount of recirculated, phase reversed product may
be lowered. With a fat content of ~ 40 % fat in the end
product stable conditions are obtained when recircu-
lating 20-25 % phase reversed product.
The working which the fat mixture is subjected to in
order to obtain phase reversal usually comprises an
initial cooling in one or several cooling steps to a
temperature below 22C. After that the mixture is worked
under a certain time, e.g. 2-10 minutes in one or
several working units, at which the fat starts to
crystallize and the temperature of the mixture rises
somewhat. After this working the product is cooled
further. As soon as the phase reversal has started a
part of the product is returned. This is suitably
carried through in such a way that a partial stream is
taken away and returned prior to the passage of the
second cooling step. If it is considered suitable phase
reversed product may be taken away and returned also
after the final cooling step.
SlJBSTITUTE SHEE~

W094/OS160 ~39 PCT/SE93/OC
The method according to the invention may be practised
as follows.
A fat mixture containing
Cream - 75 % 21.0 kg
Stabilizing means1,2 kg
NaCl 0,4 kg
Water ad 40 kg 17,3 kg
is produced. The mixing temperature was in the interval
50-60C.
The mixture was treated in coolers and a working unit to
the following temperature after each step.5
First cooling step < 18C
Working unit < 22C
Second cooling step < 20C
After the working step 5-25 ~ of the mixture was
returned to the inlet of the first cooling step.
SUBSTITUTE SHEET

Dessin représentatif

Désolé, le dessin représentatif concernant le document de brevet no 2143938 est introuvable.

États administratifs

2024-08-01 : Dans le cadre de la transition vers les Brevets de nouvelle génération (BNG), la base de données sur les brevets canadiens (BDBC) contient désormais un Historique d'événement plus détaillé, qui reproduit le Journal des événements de notre nouvelle solution interne.

Veuillez noter que les événements débutant par « Inactive : » se réfèrent à des événements qui ne sont plus utilisés dans notre nouvelle solution interne.

Pour une meilleure compréhension de l'état de la demande ou brevet qui figure sur cette page, la rubrique Mise en garde , et les descriptions de Brevet , Historique d'événement , Taxes périodiques et Historique des paiements devraient être consultées.

Historique d'événement

Description Date
Le délai pour l'annulation est expiré 1998-09-03
Demande non rétablie avant l'échéance 1998-09-03
Réputée abandonnée - omission de répondre à un avis sur les taxes pour le maintien en état 1997-09-03
Demande publiée (accessible au public) 1994-03-17

Historique d'abandonnement

Date d'abandonnement Raison Date de rétablissement
1997-09-03
Titulaires au dossier

Les titulaires actuels et antérieures au dossier sont affichés en ordre alphabétique.

Titulaires actuels au dossier
ALFA LAVAL AB
Titulaires antérieures au dossier
MAGNUS LARSSON
STEN-OLOF ARPH
Les propriétaires antérieurs qui ne figurent pas dans la liste des « Propriétaires au dossier » apparaîtront dans d'autres documents au dossier.
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Description du
Document 
Date
(aaaa-mm-jj) 
Nombre de pages   Taille de l'image (Ko) 
Description 1994-03-16 4 134
Revendications 1994-03-16 1 32
Abrégé 1994-03-16 1 40
Courtoisie - Lettre d'abandon (taxe de maintien en état) 1997-10-05 1 185
Taxes 1996-08-26 1 64
Taxes 1995-08-16 1 76
Rapport d'examen préliminaire international 1995-03-05 8 159
Courtoisie - Lettre du bureau 1995-04-12 1 14