EP0816478B1 - Fat peroxidation process - Google Patents

Fat peroxidation process Download PDF

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Publication number
EP0816478B1
EP0816478B1 EP97401447A EP97401447A EP0816478B1 EP 0816478 B1 EP0816478 B1 EP 0816478B1 EP 97401447 A EP97401447 A EP 97401447A EP 97401447 A EP97401447 A EP 97401447A EP 0816478 B1 EP0816478 B1 EP 0816478B1
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EP
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Prior art keywords
fatty substance
reaction
radiation
peroxide
peroxidation
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German (de)
French (fr)
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EP0816478A1 (en
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Serge Petit
André Lombard
Michel Rival.
Christian Laine
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Rival De Services D'etudes De Promotions Et De Distribution "laboratoires Rivadis" Ste
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Rival De Services D'etudes De Promotions Et De Distribution "laboratoires Rivadis" Ste
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    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11CFATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C3/00Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
    • C11C3/006Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by oxidation

Definitions

  • the invention relates to a process for the peroxidation of fat body.
  • the products obtained by the process according to the invention make it possible to improve the formulations cosmetics and pharmaceuticals in which they are used.
  • the free radical initiation phase is either continuous, or discontinuous, and is characterized by a contribution energy in the form of heat, alone or in combination with ultraviolet radiation.
  • promoters radicals such as metal ions have also been described.
  • French patent FR-A-2,461,744 describes peroxidation of fatty substances by blowing air, under a temperature of the order of 50 to 100 ° C, with catalysis to ultraviolet radiation.
  • French patent FR-A-0 918 163 which is relates to drugs whose active ingredients are peroxides of fatty substances, specifies that these can be obtained by peroxidation processes in which ethylenic fatty substances are used either presence of oxygen at a preferred temperature higher than 20 ° C or in the presence of hydrogen peroxide.
  • oxygen is supplied by bubbling or by simple exposure to air, to pressure atmospheric.
  • training lipid peroxides is usually accompanied by formation of cytotoxic degradation products.
  • MDA malondialdehyde
  • the present invention aims for this a new fat peroxidation process which allows control the formation of toxic degradation products such as MDA by limiting them.
  • This process is characterized, among others, by reaction conditions allowing to obtain a peroxidized fatty substance having a level of MDA less than 30 ppm, and more particularly between 10 and 30 ppm, i.e. 0.1 to 0.3 ppm per 100 of the index peroxide.
  • the method according to the invention implements more energetic radiation than radiation ultraviolet, like for example, x-rays, rays gamma, beta rays.
  • alpha rays and neutrons are difficult to use because the energy of radiation must be such that it does not induce reactions significant nuclear power.
  • the fatty substances are peroxidized in the presence of the required amount of oxygen quickly and controlled, avoiding the formation of degradation products that appear if the reaction is conducted beyond the creation of peroxide compounds.
  • the fatty substance is placed in a transparent container radiation selected and partially filled so as to trap a sufficient volume of oxygen or air at the above the fat.
  • the volume of oxygen is calculated for correspond to the value of the desired peroxide index.
  • This oxygen (or the volume of air containing it) can be in liquid or gaseous form and is put under pressure because it is then directly dissolved within the fatty substance and can react instantly with radicals created by radiation.
  • the oxygen will advantageously be introduced under a pressure of 2.10 5 Pa (2 bars).
  • Initial pressurization is controlled by a pressure gauge.
  • the pressure indicated by the pressure gauge (taken at initial temperature), must have returned to a value indicating consumption total oxygen present by the fatty substance. In the case of the use of pure oxygen under pressure, this value will be close to zero.
  • An intense automatic stirring device can also be used during the ionization phase and just after.
  • the ionizing radiation is basically applied to initiate the reaction of peroxidation. However, it can also be applied throughout the duration of the reaction.
  • the addition, to a untreated fat, part of fat as well peroxidized and then playing the role of primer, allows reduce the duration of a peroxidation carried out according to conventional processes, and therefore to limit the formation of secondary degradation compounds.
  • the use of gamma radiation allows advantageously to obtain a peroxidized fatty substance having a rate of MDA lower than that obtained with the techniques already described and under more reaction conditions economical due to the reduction in operating time.
  • the invention preferably uses ionization parameters of sterilization units industrial particles (beta rays or electrons accelerated) or electromagnetic waves (gamma rays, X-rays).
  • the energy used is a function of the radiation employee.
  • the ionization parameters are calculated in order to allow the emission of a total energy between 10 and 100 Kgy.
  • the relatively short duration of the reaction understood between 4 and 10 hours avoids the formation of secondary degradation compounds of peroxides lipid.
  • the absence of oxygen within of the container is advantageous because it makes it possible to obtain a stable product.
  • a peroxidized fatty substance is obtained having a rate of MDA less than 30 ppm, and more particularly understood between 10 and 30 ppm, i.e. 0.1 to 0.3 ppm per 100 of the index peroxide.
  • the products thus obtained can be used pure or as a mixture, in particular in the constitution of products to therapeutic, cosmetic, dietetic use.
  • thermosensitive thermosensitive to fatty substances, before ionization of this latest. We can then benefit from sterilizing effects radiation used in applications requiring a sterile product.
  • This heat-sensitive active agent can be chosen in particular from the groups of antibiotics, fat-soluble vitamins, enzymes or proteins.
  • the peroxidized oils used in the process according to the invention are vegetable and / or animal. They are chosen from the group of ethylenic fatty substances such as olive oil, peanut, sesame, corn, sunflower, sweet almond, or from the group of polyunsaturated fatty acids such as olive oil. evening primrose, borage, blackcurrant, wheat germ, or in the group of animal oils such as those from fish. This list is not exhaustive.
  • Example 1 The fifteen liters of Example 1 are mixed with 30 liters of untreated sunflower oil.
  • the mixture has a peroxide number of 100, and an MDA level of 0.10 ppm per unit of peroxide.
  • the reaction conditions are those of Example 1, but the shell is only subjected to a single pass under ionizing radiation at 25 kGy.
  • the residual pressure is 1.10 5 Pa (1 bar), the peroxide index of 50, the MDA content of 0.2 per unit of peroxide.
  • the shell is placed in a thermostated bath at 95 ° C for 8 hours.
  • the reaction is stopped while the residual pressure is 1.10 4 Pa (0.1 bar).
  • the peroxide index is 120, and the MDA content is 0.3 ppm per unit of peroxide.

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  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Cosmetics (AREA)
  • Fats And Perfumes (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Process for peroxidation of a fatty substance comprises subjecting the fatty substance to X-ray, gamma -ray or beta -ray radiation in the presence of oxygen, such that the peroxidised product contains less than 0.30 ppm malondialdehyde (MDA) per peroxide unit.

Description

L'invention concerne un procédé de peroxydation des corps gras. Les produits obtenus par le procédé selon l'invention permettent d'améliorer les formulations cosmétiques et pharmaceutiques dans lesquelles ils sont utilisés.The invention relates to a process for the peroxidation of fat body. The products obtained by the process according to the invention make it possible to improve the formulations cosmetics and pharmaceuticals in which they are used.

Les procédés de peroxygénation de corps gras sont nombreux, et l'utilisation pharmaceutique ou cosmétologique d'huiles peroxydées est connue depuis des siècles.The processes of peroxygenation of fatty substances are numerous, and pharmaceutical or cosmetic use peroxidized oils has been known for centuries.

Le principe des réactions chimiques de peroxydation des corps gras est désormais bien connu. Ces réactions comportent une première phase d'initiation correspondant à la création de radicaux libres, ces derniers pouvant ensuite réagir lors d'étapes ultérieures avec l'oxygène apporté au milieu pour former les composés de peroxydation (hydroperoxydes, endoperoxydes).The principle of chemical reactions of peroxidation of fatty substances is now well known. These reactions include a first initiation phase corresponding to the creation of free radicals, these the latter can then react in subsequent steps with the oxygen supplied to the medium to form the compounds peroxidation (hydroperoxides, endoperoxides).

Les produits obtenus par tous ces procédés sont caractérisés par leur indice de peroxyde, révélateur de la quantité d'oxygène fixée lors de la réaction de peroxydation.The products obtained by all these processes are characterized by their peroxide index, revealing the quantity of oxygen fixed during the reaction of peroxidation.

Dans l'ensemble des procédés décrits jusqu'à présent, la phase d'initiation des radicaux libres est soit continue, soit discontinue, et se caractérise par un apport d'énergie sous forme de chaleur, seule ou en combinaison avec des rayonnements ultraviolets. L'emploi de promoteurs de radicaux comme les ions métalliques a aussi été décrit.In all of the processes described so far, the free radical initiation phase is either continuous, or discontinuous, and is characterized by a contribution energy in the form of heat, alone or in combination with ultraviolet radiation. The employment of promoters radicals such as metal ions have also been described.

Le brevet français FR-A-2 461 744, par exemple, décrit une peroxydation de corps gras par soufflage d'air, sous une température de l'ordre de 50 à 100°C, avec une catalyse aux rayonnements ultaviolets.French patent FR-A-2,461,744, for example, describes peroxidation of fatty substances by blowing air, under a temperature of the order of 50 to 100 ° C, with catalysis to ultraviolet radiation.

D'autres procédés de peroxydation sont décrits par exemple dans le manuel "Introduction à la biochimie et à la technologie des aliments " Vol.1 par J.C Cheftel et H.Cheftel, Techniques et documentation-Lavoisier. Ces procédés font intervenir, lors de la phase d'initiation, des températures élevées, et des catalyseurs tels que des rayonnements lumineux ou des traces de métaux.Other peroxidation processes are described by example in the manual "Introduction to biochemistry and food technology "Vol.1 by J.C Cheftel and H.Cheftel, Techniques et documentation-Lavoisier. These processes involve, during the initiation phase, high temperatures, and catalysts such as light radiation or traces of metals.

De même, le brevet français FR-A-0 918 163, qui se rapporte à des médicaments dont les principes actifs sont des peroxydes de corps gras, précise que ces derniers peuvent être obtenus par les procédés de peroxydation dans lesquels des corps gras éthyléniques sont mis soit en présence d'oxygène à une température de préférence supérieure à 20°C soit en présence d'eau oxygénée.Similarly, French patent FR-A-0 918 163, which is relates to drugs whose active ingredients are peroxides of fatty substances, specifies that these can be obtained by peroxidation processes in which ethylenic fatty substances are used either presence of oxygen at a preferred temperature higher than 20 ° C or in the presence of hydrogen peroxide.

L'utilisation de l'ozone a également été citée, bien qu'aboutissant principalement à la création de composés oxygénés d'une autre nature (ozonides).The use of ozone was also cited, although mainly leading to the creation of compounds oxygenated of another nature (ozonides).

Dans tous les procédés cités, l'oxygène est apporté par bullage ou par simple exposition à l'air, à la pression atmosphérique.In all the processes mentioned, oxygen is supplied by bubbling or by simple exposure to air, to pressure atmospheric.

Ceci a pour inconvénient d'interdire l'utilisation d'initiateurs de radicaux puissants. En effet, une création de radicaux en trop grand nombre par rapport à l'oxygène présent dans le milieu entraínerait des réactions secondaires néfastes(changements de position de doubles liaisons, clivages de chaínes, polymérisations). Les initiateurs de radicaux employés sont donc limités à la chaleur ou aux ultra violets de faible énergie.This has the disadvantage of prohibiting the use powerful radical initiators. Indeed, a creation too many radicals compared to oxygen present in the environment would cause reactions harmful side effects (double position changes connections, cleavages of chains, polymerizations). The radical initiators employed are therefore limited to the heat or low energy ultra violet.

De plus, dans tous les procédés décrits, la formation des peroxydes lipidiques s'accompagne généralement par la formation de produits de dégradation cytotoxiques.In addition, in all the processes described, training lipid peroxides is usually accompanied by formation of cytotoxic degradation products.

Ces produits sont en particulier des aldéhydes tels que le malondialdéhyde (MDA), qui est une molécule dont la toxicité pour la peau est aujourd'hui reconnue.These products are in particular aldehydes such that malondialdehyde (MDA), which is a molecule whose toxicity for the skin is now recognized.

La présente invention vise pour cela un nouveau procédé de peroxydation des corps gras qui permet de maítriser la formation des produits de dégradation toxiques tels que le MDA en les limitant. Ce procédé se caractérise, entre autres, par des conditions réactionnelles permettant d'obtenir un corps gras peroxydé présentant un taux de MDA inférieur à 30 ppm, et plus particulièrement compris entre 10 et 30 ppm, soit 0,1 à 0,3 ppm pour 100 d'indice de peroxyde.The present invention aims for this a new fat peroxidation process which allows control the formation of toxic degradation products such as MDA by limiting them. This process is characterized, among others, by reaction conditions allowing to obtain a peroxidized fatty substance having a level of MDA less than 30 ppm, and more particularly between 10 and 30 ppm, i.e. 0.1 to 0.3 ppm per 100 of the index peroxide.

Le procédé de peroxydation d'un corps gras selon l'invention comprend les étapes consistant à :

  • a) introduire le corps gras dans un récipient susceptible d'être fermé ;
  • b) irradier le corps gras par un rayonnement X, gamma ou bêta, pour initier la réaction ;
    caractérisé par le fait qu'il comprend l'étape consistant, entre les étapes a) et b) à:
  • c) introduire de l'oxygène gazeux dans ledit récipient à une pression comprise entre 1.105 et 6.105 Pa (1 et 6 bars), et fermer le récipient, le corps gras une fois peroxydé présentant un taux de malondialdéhyde inférieur à 0,30 ppm par unité de peroxyde.
  • The process for the peroxidation of a fatty substance according to the invention comprises the steps consisting in:
  • a) introduce the fatty substance into a container capable of being closed;
  • b) irradiating the fatty substance with X, gamma or beta radiation, to initiate the reaction;
    characterized by the fact that it comprises the step consisting, between steps a) and b) of:
  • c) introducing gaseous oxygen into said container at a pressure between 1.10 5 and 6.10 5 Pa (1 and 6 bars), and closing the container, the fatty substance once peroxidized having a malondialdehyde level of less than 0.30 ppm per unit of peroxide.
  • Ainsi, le procédé selon l'invention met en oeuvre des rayonnements plus énergétiques que les rayonnements ultraviolets, comme par exemple, les rayons X, rayons gamma, rayons beta.Thus, the method according to the invention implements more energetic radiation than radiation ultraviolet, like for example, x-rays, rays gamma, beta rays.

    Par contre, les rayons alpha et les neutrons sont difficilement utilisables car l'énergie des rayonnements doit être telle qu'elle n'induit pas de réactions nucléaires significatives.However, alpha rays and neutrons are difficult to use because the energy of radiation must be such that it does not induce reactions significant nuclear power.

    Les corps gras sont peroxydés en présence de la quantité nécessaire d'oxygène, de façon rapide et contrôlée, évitant la formation de produits de dégradations qui apparaissent si la réaction est conduite au delà de la création des composés peroxydés.The fatty substances are peroxidized in the presence of the required amount of oxygen quickly and controlled, avoiding the formation of degradation products that appear if the reaction is conducted beyond the creation of peroxide compounds.

    Pour mettre en oeuvre le procédé selon l'invention, le corps gras est placé dans un récipient transparent au rayonnement choisi et rempli partiellement de façon à emprisonner un volume suffisant d'oxygène ou d'air au dessus du corps gras. Le volume d'oxygène est calculé pour correspondre à la valeur de 1 'indice de peroxyde souhaité. Cet oxygène(ou le volume d'air le renfermant) peut être sous forme liquide ou gazeuse et est mis sous pression car il est alors directement dissous au sein du corps gras et peut réagir instantanément avec les radicaux créés par les rayonnements.To implement the method according to the invention, the fatty substance is placed in a transparent container radiation selected and partially filled so as to trap a sufficient volume of oxygen or air at the above the fat. The volume of oxygen is calculated for correspond to the value of the desired peroxide index. This oxygen (or the volume of air containing it) can be in liquid or gaseous form and is put under pressure because it is then directly dissolved within the fatty substance and can react instantly with radicals created by radiation.

    On introduira de manière avantageuse l'oxygène sous une pression de 2.105 Pa (2 bars).The oxygen will advantageously be introduced under a pressure of 2.10 5 Pa (2 bars).

    La mise sous pression initiale est contrôlée au moyen d'un manomètre. A la fin de la réaction, la pression indiquée par le manomètre (prise à température initiale), doit être revenue à une valeur indiquant la consommation totale de l'oxygène présent par le corps gras. Dans le cas de l'utilisation d'oxygène pur sous pression, cette valeur sera voisine de zéro.Initial pressurization is controlled by a pressure gauge. At the end of the reaction, the pressure indicated by the pressure gauge (taken at initial temperature), must have returned to a value indicating consumption total oxygen present by the fatty substance. In the case of the use of pure oxygen under pressure, this value will be close to zero.

    Un dispositif d'agitation automatique intense peut aussi être utilisé au cours de la phase d'ionisation et juste après.An intense automatic stirring device can also be used during the ionization phase and just after.

    De manière avantageuse, le rayonnement ionisant est appliqué essentiellement pour initier la réaction de peroxydation. Cependant, il peut également être appliqué pendant toute la durée de la réaction.Advantageously, the ionizing radiation is basically applied to initiate the reaction of peroxidation. However, it can also be applied throughout the duration of the reaction.

    Dans une variante de l'invention, l'addition, à un corps gras non traité, d'une partie de corps gras ainsi peroxydé et jouant alors le rôle d'amorce, permet de réduire la durée d'une peroxydation effectuée selon des procédés classiques, et donc de limiter la formation de composés de dégradation secondaires.In a variant of the invention, the addition, to a untreated fat, part of fat as well peroxidized and then playing the role of primer, allows reduce the duration of a peroxidation carried out according to conventional processes, and therefore to limit the formation of secondary degradation compounds.

    Dans le procédé selon la présente invention, l'utilisation des radiations gammas, notamment, permet d'obtenir avantageusement un corps gras peroxydé présentant un taux de MDA inférieur à celui obtenu avec les techniques déjà décrites et dans des conditions réactionnelles plus économiques du fait de la réduction du temps d'opération.In the method according to the present invention, the use of gamma radiation, in particular, allows advantageously to obtain a peroxidized fatty substance having a rate of MDA lower than that obtained with the techniques already described and under more reaction conditions economical due to the reduction in operating time.

    De manière pratique l'invention utilise de préférence les paramètres d'ionisation des unités de stérilisations industrielles à particules (rayons beta ou électrons accélérés) ou à ondes électromagnétiques (rayons gamma, rayons X).In practical terms, the invention preferably uses ionization parameters of sterilization units industrial particles (beta rays or electrons accelerated) or electromagnetic waves (gamma rays, X-rays).

    L'énergie utilisée est fonction du rayonnement employé. Les paramètres d'ionisation sont calculés afin de permettre l'émission d'une énergie totale comprise entre 10 et 100 Kgy.The energy used is a function of the radiation employee. The ionization parameters are calculated in order to allow the emission of a total energy between 10 and 100 Kgy.

    La relative courte durée de la réaction, comprise entre 4 et 10 heures permet d'éviter la formation des composés de dégradation secondaire des peroxydes lipidiques. En fin de réaction, l'absence d'oxygène au sein du récipient est avantageuse car elle permet d'obtenir un produit stable.The relatively short duration of the reaction, understood between 4 and 10 hours avoids the formation of secondary degradation compounds of peroxides lipid. At the end of the reaction, the absence of oxygen within of the container is advantageous because it makes it possible to obtain a stable product.

    On obtient un corps gras peroxydé présentant un taux de MDA inférieur à 30 ppm, et plus particulièrement compris entre 10 et 30 ppm, soit 0,1 à 0,3 ppm pour 100 d'indice de peroxyde.A peroxidized fatty substance is obtained having a rate of MDA less than 30 ppm, and more particularly understood between 10 and 30 ppm, i.e. 0.1 to 0.3 ppm per 100 of the index peroxide.

    Les produits ainsi obtenus peuvent être utilisés purs ou en mélange, dans la constitution notamment de produits à usage thérapeutique, cosmétique, diététique.The products thus obtained can be used pure or as a mixture, in particular in the constitution of products to therapeutic, cosmetic, dietetic use.

    Dans un mode de mise en oeuvre particulièrement avantageux du procédé, il est prévu d'additionner un actif thermo-sensible au corps gras, avant l'ionisation de ce dernier. On peut alors bénéficier des effets stérilisants des rayonnements utilisés dans le cadre d'applications nécessitant un produit stérile.In a particularly embodiment advantageous of the process, it is planned to add an active thermosensitive to fatty substances, before ionization of this latest. We can then benefit from sterilizing effects radiation used in applications requiring a sterile product.

    Cet actif thermo-sensible pourra être choisi notamment dans les groupes des antibiotiques, des vitamines liposolubles, des enzymes ou des protéines.
    Les huiles peroxydées utilisées dans le procédé selon l'invention sont végétales et/ou animales. Elles sont choisies dans le groupe des corps gras éthyléniques tels que l'huile d'olive, d'arachide, de sésame, de maïs, de tournesol, d'amande douce, ou dans le groupe des acides gras polyinsaturés comme l'huile d'onagre, de bourrache, de cassis, de germe de blé, ou encore dans le groupe des huiles animales comme celles issues du poisson. Cette liste n'est pas limitative.
    This heat-sensitive active agent can be chosen in particular from the groups of antibiotics, fat-soluble vitamins, enzymes or proteins.
    The peroxidized oils used in the process according to the invention are vegetable and / or animal. They are chosen from the group of ethylenic fatty substances such as olive oil, peanut, sesame, corn, sunflower, sweet almond, or from the group of polyunsaturated fatty acids such as olive oil. evening primrose, borage, blackcurrant, wheat germ, or in the group of animal oils such as those from fish. This list is not exhaustive.

    Les exemples suivants illustrent la présente invention sans en limiter les possibilités et les variantes de mise en oeuvre.The following examples illustrate the present invention without limiting the possibilities and variants in action.

    Exemple 1Example 1

    Dans un obus cylindrique en polyéthylène de 20 litres et de 20 cm de diamètre, équipé d'un orifice muni d'un robinet permettant son remplissage, et d'un manomètre, on dispose 15 Kg d'huile de tournesol. 10 litres d'oxygène gazeux sont introduits. La pression indiquée est très légèrement supérieure à 2.105 Pa (2 bars). L'obus est disposé sur le chariot de gamma stérilisation. La durée d'exposition est de 8 heures, en quatre passages de 2 heures sur la source émettrice.In a cylindrical polyethylene shell of 20 liters and 20 cm in diameter, equipped with an orifice provided with a tap allowing its filling, and a manometer, there are 15 kg of sunflower oil. 10 liters of gaseous oxygen are introduced. The pressure indicated is very slightly higher than 2.10 5 Pa (2 bars). The shell is placed on the sterilization gamma cart. The duration of exposure is 8 hours, in four passages of 2 hours on the emitting source.

    A chaque passage l'énergie transmise est de 25 KGy. Au total 100 Kgy sont transmis. Après chaque passage on lit la pression sur le manomètre. Dans ce cas la pression décroít grossièrement d'un quart à chaque mesure, pour être pratiquement nulle après le dernier passage. On note un rougissement du milieu réactionnel après le deuxième passage. Ce rougissement disparaít à la fin de la réaction. L'huile de tournesol présente alors un indice de peroxyde voisin de 300, et un taux de MDA inférieur à 30 ppm, soit 0,1 ppm par unité de peroxyde.At each pass the energy transmitted is 25 KGy. At total 100 Kgy are transmitted. After each pass we read the pressure on the pressure gauge. In this case the pressure decreases roughly a quarter for each measurement, to be practically zero after the last pass. We note a reddening of the reaction medium after the second passage. This blush disappears at the end of the reaction. Sunflower oil then has a peroxide index close to 300, and an MDA level below 30 ppm, i.e. 0.1 ppm per unit of peroxide.

    Exemple 2Example 2

    Les quinze litres de l'exemple 1 sont mélangés à 30 litres d'huile de tournesol non traitée. Le mélange présente un indice de peroxyde de 100, et un taux de MDA de 0,10 ppm par unité de peroxyde.The fifteen liters of Example 1 are mixed with 30 liters of untreated sunflower oil. The mixture has a peroxide number of 100, and an MDA level of 0.10 ppm per unit of peroxide.

    Exemple 3Example 3

    Les conditions réactionnelles sont celles de l'exemple 1, mais l'obus n'est soumis qu'à un seul passage sous rayonnement ionisant à 25 kGy. La pression résiduelle est 25 de 1.105 Pa (1 bar), l'indice de peroxyde de 50, la teneur en MDA de 0,2 par unité de peroxyde.The reaction conditions are those of Example 1, but the shell is only subjected to a single pass under ionizing radiation at 25 kGy. The residual pressure is 1.10 5 Pa (1 bar), the peroxide index of 50, the MDA content of 0.2 per unit of peroxide.

    L'obus est placé dans un bain thermostaté à 95°C pendant 8 heures. On arrête la réaction alors que la pression résiduelle est de 1.104 Pa (0,1 bars). L'indice de peroxyde est de 120, et la teneur en MDA de 0,3 ppm par unité de peroxyde.The shell is placed in a thermostated bath at 95 ° C for 8 hours. The reaction is stopped while the residual pressure is 1.10 4 Pa (0.1 bar). The peroxide index is 120, and the MDA content is 0.3 ppm per unit of peroxide.

    Exemple 4Example 4

    Une huile de Calophylum Inophyllum est traitée avec les conditions de l'exemple 1.Les calculs sont effectués pour obtenir un indice de peroxyde de 50 et un taux de MDA inférieur à 0,3 ppm par unité de peroxyde. Cette huile appliquée sur des érythèmes solaires, permet d'obtenir une sédation rapide des manifestations douloureuses liés à l'érythème.An oil of Calophylum Inophyllum is treated with the conditions of example 1 The calculations are carried out to obtain a peroxide index of 50 and an MDA level less than 0.3 ppm per unit of peroxide. This oil applied to solar erythemas, provides a rapid sedation of painful manifestations related to erythema.

    Claims (13)

    1. A method for the peroxidation of a fatty substance, comprising the steps consisting in:
      a) introducing the fatty substance into a receptacle able to be closed;
      b) irradiating the fatty substance with X-rays or gamma or beta radiation in order to initiate the reaction;
      characterised by the fact that it comprises the steps consisting in, between steps a) and b):
      c) introducing gaseous oxygen into the said receptacle at a pressure of between 1.105 and 6.105 Pa (1 and 6 bar) and closing the receptacle,
      the fatty substance once peroxidised having a malondialdehyde content of less than 0.30 ppm per unit of peroxide.
    2. A method according to Claim 1, in which the ionising radiation is applied essentially in order to initiate the peroxidation reaction.
    3. A method according to Claim 1, in which the ionising radiation is applied throughout or substantially throughout the reaction.
    4. A method according to Claims 1 to 3, consisting in adding to the fatty substance prior to any normal peroxidation a small quantity of ionised fatty substance fulfilling the role of initiator in order to reduce the duration of the reaction.
    5. A method according to Claims 1 to 4, consisting in introducing gaseous oxygen at a pressure of 2.105 Pa (2 bar).
    6. A method according to Claims 1 to 5, consisting in, prior to the reaction, fixing the quantities of oxygen and radiation according to the peroxide index required in the peroxidised fatty substance.
    7. A method according to Claims 1 to 6, consisting in subjecting the fatty substance to gamma radiation, the energy transmitted being between 10 and 100 kGy.
    8. A method according to Claims 1 to 7, consisting in choosing the fatty substance from amongst animal and/or vegetable fatty substances.
    9. A method according to Claims 1 to 8, consisting in preferably using ethylenic vegetable oils such as olive, ground nut, sesame, maize, sunflower or sweet almond oil, or polyunsaturated vegetable oils such as evening primrose, borage, blackcurrant or wheatgerm oil, or from the group of animal oils such as those coming from fish.
    10. A method according to Claims 1 to 9, consisting in choosing reaction conditions making it possible to obtain a peroxidised fatty substance comprising an MDA content preferably of between 0.10 and 0.3 ppm per unit of peroxide.
    11. A method according to Claims 1 to 10, consisting in adding a heat-sensitive active agent to the fatty substance, prior to subjecting it to the ionising radiation.
    12. A method according to Claims 1 to 11, consisting in adding a heat-sensitive active agent chosen in particular from the groups consisting of antibiotics, liposoluble vitamins, enzymes or proteins.
    13. A method according to Claims 1 to 12, consisting in stirring the fatty substance during the subjecting to the ionising radiation and/or just afterwards.
    EP97401447A 1996-06-28 1997-06-20 Fat peroxidation process Expired - Lifetime EP0816478B1 (en)

    Applications Claiming Priority (2)

    Application Number Priority Date Filing Date Title
    FR9608143 1996-06-28
    FR9608143A FR2750432B1 (en) 1996-06-28 1996-06-28 FAT BODY PEROXIDATION PROCESS

    Publications (2)

    Publication Number Publication Date
    EP0816478A1 EP0816478A1 (en) 1998-01-07
    EP0816478B1 true EP0816478B1 (en) 2003-10-22

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    Application Number Title Priority Date Filing Date
    EP97401447A Expired - Lifetime EP0816478B1 (en) 1996-06-28 1997-06-20 Fat peroxidation process

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    EP (1) EP0816478B1 (en)
    AT (1) ATE252629T1 (en)
    DE (1) DE69725654D1 (en)
    FR (1) FR2750432B1 (en)

    Families Citing this family (1)

    * Cited by examiner, † Cited by third party
    Publication number Priority date Publication date Assignee Title
    US6395779B1 (en) * 1999-01-29 2002-05-28 Neoteric Cosmetics, Inc. Method of treatment using peroxidized lipids

    Family Cites Families (4)

    * Cited by examiner, † Cited by third party
    Publication number Priority date Publication date Assignee Title
    US3597344A (en) * 1968-05-10 1971-08-03 Atomic Energy Commission High energy radiation treatment of tall oil
    JPS57140701A (en) * 1981-02-26 1982-08-31 Yasumitsu Kigoshi Insecticide useful for man
    FR2539142B1 (en) * 1983-01-06 1985-07-05 Daniel Pierre PROCESS FOR THE PREPARATION OF PEROXIDATED FATS, PRODUCTS OBTAINED BY THIS PROCESS AND MIXTURES OF SUCH PRODUCTS WITH ADDITIVES AND APPLICATIONS OF SUCH PRODUCTS
    SU1393843A1 (en) * 1985-12-20 1988-05-07 Институт Физической Химии Им.Л.В.Писаржевского Method of purifying hair fat

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    EP0816478A1 (en) 1998-01-07
    ATE252629T1 (en) 2003-11-15
    FR2750432A1 (en) 1998-01-02
    FR2750432B1 (en) 1998-09-04
    DE69725654D1 (en) 2003-11-27

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