EP1149123B1 - Peroxidised polyorganosiloxanes (pos), one of the methods for preparing them and their use as bleaching agent in dental compositions - Google Patents

Peroxidised polyorganosiloxanes (pos), one of the methods for preparing them and their use as bleaching agent in dental compositions Download PDF

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Publication number
EP1149123B1
EP1149123B1 EP99973300A EP99973300A EP1149123B1 EP 1149123 B1 EP1149123 B1 EP 1149123B1 EP 99973300 A EP99973300 A EP 99973300A EP 99973300 A EP99973300 A EP 99973300A EP 1149123 B1 EP1149123 B1 EP 1149123B1
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Prior art keywords
fpo
functional groups
pos
polyorganosiloxanes
functional
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German (de)
French (fr)
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EP1149123A1 (en
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Adrien Dromard
Gérard Mignani
Lucile Gambut
Frédéric DALLEMER
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Rhodia Chimie SAS
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    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/16Organic compounds
    • C11D3/37Polymers
    • C11D3/3703Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • C11D3/373Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds containing silicones
    • C11D3/3742Nitrogen containing silicones
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/16Organic compounds
    • C11D3/37Polymers
    • C11D3/3703Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • C11D3/373Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds containing silicones
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/16Organic compounds
    • C11D3/37Polymers
    • C11D3/3788Graft polymers
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/39Organic or inorganic per-compounds
    • C11D3/3945Organic per-compounds

Definitions

  • the field of the invention is that of applicable peroxidized systems especially in money laundering.
  • the oxidizing properties of these systems are more particularly appreciated in teeth whitening applications (e.g. toothpaste).
  • peroxidized systems referred to in the context of this presentation are functionalized polymers.
  • the present invention relates to perorganized polyorganosiloxanes (POS) thus as one of their preparation processes.
  • the invention also relates to silicone precursors of these POSs. peroxides.
  • the present invention includes an application aspect which comprises the use of peroxidized POSs according to the invention as active ingredient in laundering. More specifically, the invention relates to dental compositions, for example toothpastes, including peroxidized POS as a bleaching agent.
  • H 2 O 2 hydrogen peroxide
  • persalts percarbonates, perborates, calcium peroxides
  • H 2 O 2 will designate H 2 O 2 as such and its persalts.
  • the disadvantages of hydrogen peroxide are not negligible.
  • H 2 O 2 must be used in high concentration to be effective. This point is particularly troublesome given the aggressiveness of H 2 O 2 .
  • hydrogen peroxide has the disadvantage of being unstable.
  • European patent application No. 796 874 relates to a process for the preparation of polymers comprising peroxycarboxylic groups.
  • These peroxycarboxylic polymers are more specifically copolymers of N-vinylpyrolidone / maleic anhydride.
  • the hydrogen peroxide that we react with this copolymer allows the transformation of the carboxyls derived from the anhydride into peroxycarboxylic functions.
  • the performance of these copolymers peroxycarboxylates, in terms of bleaching, are not revealed by this request patent.
  • the peroxycarboxylated copolymers lack selectivity with respect to the teeth.
  • instability problems can be feared for teeth whitening applications of these copolymers.
  • PCT patent application WO 97/02 011 discloses dental oral compositions comprising conventional ingredients such as abrasives, binders, humectants, surfactants, sources of fluorine ions or other sweeteners, as well as two other essential ingredients for namely, on the one hand, an aminoalkylsilicone such as a polydimethylsiloxane comprising aminoalkyl units of the propylaminoethylamine type in the chains and at their ends and, on the other hand, a polydimethylsiloxane comprising pendant groups of polyoxyethylene and / or polyoxypropylene type and having a surfactant action.
  • an aminoalkylsilicone such as a polydimethylsiloxane comprising aminoalkyl units of the propylaminoethylamine type in the chains and at their ends and, on the other hand, a polydimethylsiloxane comprising pendant groups of polyoxyethylene and / or polyoxypropylene type and
  • This oral composition is presented as having improved anti-plaque and anti-bacterial properties, which complement excellent cleaning performance.
  • This oral composition can also comprise bleaching agents belonging to the family of inorganic peracid salts (persulfates, perborates, percarbonates and metal peroxides). These oral compositions are not satisfactory in terms of stability, toxicity, selectivity with respect to the teeth and efficacy of bleaching by oxidation.
  • Polyorganosiloxanes comprising ester groups of peracids carboxylic acids have been described in GB 897,973 and US 3,726,943; they can be useful as vulcanizing agents, as polymerization initiator, as coupling agents ...
  • Another essential objective of the invention is to provide a system for peroxidized bleaching especially for dental bleaching applications which allows to control the reactivity of the peroxide function, so as to limit as far as possible its transformation into aggressive free radicals.
  • Another essential objective of the invention is to provide a system for peroxidized bleaching usable in particular in dental bleaching and endowed with significantly improved storage stability.
  • Another essential objective of the invention is to provide a system for peroxide bleaching applied in dental bleaching (oral composition for treatment and maintenance of the teeth), having a better selectivity with respect to teeth to whiten.
  • Another essential objective of the invention is to provide an oxidizing system peroxidized, capable of being used as a controlled release system of oxidizing peroxide functions.
  • Another essential objective of the invention is to provide a process for obtaining of the aforementioned peroxidized oxidizing system, which is simple to implement and economic.
  • Another essential objective of the invention is to prescribe the use of the system peroxidized oxidant mentioned above, as a teeth whitening agent.
  • Another essential objective of the invention is to provide a composition dental with an effective, stable and selective bleaching agent.
  • these silicones functionalized with Fpo acyl peroxide are endowed with a specific affinity for the constituent materials of teeth (in hydroxyapatite) so these are selective vectors specific to route the chemical whitening functions to the teeth. It goes without saying that optimizes the efficiency of said functions. It follows that it is possible to reduce the doses, which is entirely in line with the decrease in the aggressiveness of the agent laundering.
  • these peroxide functional silicones are hydrophobic and have so the advantage of preserving the Fpo functions of water, which is an element major instability for them.
  • the new peroxidized polyorganosiloxanes with Fpo functions can be linear and / or branched and / or crosslinked polymers according to the percentage by weight of DTQ siloxyl patterns which they include.
  • Each Fpo acyl peroxide function belongs to a peroxycarboxylic acid, halide - chloride - or salt residue.
  • peroxycarboxylic residues are linked to the silicon of the POS chain by a hydrocarbon ball joint (that is to say comprising in particular carbon and hydrogen atoms), aliphatic and / or alicyclic and / or aromatic and / or heterocyclic optionally comprising one or more heteroatoms: N, O, S ..., possibly.
  • a hydrocarbon ball joint that is to say comprising in particular carbon and hydrogen atoms
  • aliphatic and / or alicyclic and / or aromatic and / or heterocyclic optionally comprising one or more heteroatoms: N, O, S ..., possibly.
  • the advantageous stabilizing action of Fstab on Fpo is a preferred characteristic of the functionalized POSs according to the invention.
  • the Fstabs are located on the functional substituents (pendant) E and / or G. Without this being limiting, it is preferable that the Fstabs are carried at least by the or the E, so as to be close to the Fpo to be stabilized. It is not forbidden to think that the stabilizing effect of Fstab is thus improved.
  • the optional functional substituents G each include, in addition to the one or more Fstab, a ball joint which ensures the connection with the silicone chain.
  • the ball joints of the substituents G are identical or different from each other, which meet the same definition as that given above for the ball joints of substituents E.
  • peroxidized POSs obtained by hydrosilylation of olefinic precursors of substituents E and G are preferred in accordance with the invention.
  • These hydrosilylation reactions can be carried out at a temperature of the order of 15 to 200 ° C, preferably of the order of 20 to 100 ° C, in the presence of a catalyst based on a metal from the group of platinum.
  • a catalyst based on a metal from the group of platinum Mention may in particular be made of the complex platinum derivatives described in US Pat. Nos. 3,715,334, 3,775,452, 3,814,730, 3,159,601, 3,159,662.
  • the quantities of platinum catalysts used are of the order of 1 to 300 parts per million, expressed as metal relative to the reaction medium.
  • the olefinic precursors used in these hydrosilylations do not comprise the acyl peroxide functions Fpo, but their non-peroxygenated forms F'po or any intermediate forms thereof. It is preferable in accordance with the invention to provide protection for the precursor functions F'po before hydrosilylation.
  • the POS grafted by hydrosilylation and carrying the F'po precursor functions are optionally purified and then subjected to an oxidation which allows the transformation of the F'po functions into Fpo functions.
  • the functional substituents E of Peroxidized POSs each include a ball joint comprising at least one pattern bicarboxylated and / or benzoxylated and / or imide.
  • the ball joint (s) of the functional substituent (s) E comprise at least one bicarboxylic motif
  • the Fpo function is obtained from an anhydride which is transformed, on the one hand, in an acyl peroxide function Fpo and, on the other hand, in an acid function Fstab carboxylic stabilization of neighboring Fpo.
  • the peroxidized POSs according to the invention are stable and have a high power whitening.
  • the present invention relates to a process for the preparation of POSs as defined above.
  • This process is characterized in that it essentially consists in oxidizing the polysiloxane precursors of the targeted peroxidized POSs.
  • This oxidation is carried out using at least one oxidant preferably chosen from the group comprising: H 2 O 2 , O 2 , O 3 and their mixtures,
  • These peroxidized POS precursors of POS are distinguished from the targeted peroxidized POS in that they comprise one or more F'po functions, Fpo precursors and consisting of: by carboxyl residues: with X 'corresponding to the same definition as that given for X above; and / or by acid anhydride residues
  • F'po functions can be final or included in a cycle.
  • the polysiloxane precursors with functional F'po can be obtained by cohydrolysis of chlorosilanes and non-alkoxysilanes functionalized and chlorosilanes or alkoxysilanes functionalized with substituents E and G.
  • the stage which follows the cohydrolysis can be a polycondensation and polymerization of hydrolysis products in the presence of diorganosiloxanes cyclic or a redistribution step in the presence of polydiorganosiloxanes.
  • the starting materials used can be hydrogenated polyorganosiloxanes which can be functionalized by reacting them according to a hydrosilylation reaction (addition with olefinic precursors of substituents E and G.). See above for more details on this hydrosilylation.
  • the polyorganosiloxane precursors carry functions F'po succinic anhydride linked to the silicon atoms by a ball joint - (CH 2 ) 3 -.
  • the precursors - POS present before the oxidation step to transform the F'po en Fpo, a molar purity ⁇ 90%, preferably ⁇ 95%.
  • this purification step is carried out by any known and appropriate method such as, for example, devolatilization or fractional precipitation in an organic solvent such as methanol.
  • the oxidizing agents could be hydrogen peroxide, oxygen, ozone and their mixtures.
  • the catalyst used can be a strong base, for example, a mineral base such as KOH or NaOH or even a strong acid, for example, a mineral acid such as H 2 SO 4 or organic such as MeSO 3 H.
  • the solvents used in these cases are, for example, ethyl acetate or Me SO 3 H.
  • the oxidizing agent is oxygen, it is possible to use a catalyst comprising Co 2+ .
  • this oxidation step can take place at temperature and pressure room.
  • the peroxidized POSs according to the invention are particularly suitable as bleaching agent and more particularly as a bleaching agent teeth, taking into account their properties of selectivity with respect to non-toxicity teeth, of controlled reactivity of the Fpo peroxide functions (limitation of the production of free radicals), non-toxicity and high efficiency at low doses.
  • the present invention also relates to a dental composition (for example an oral composition) - in particular toothpaste - characterized in that it comprises peroxygenated POSs as defined above at as a bleaching agent.
  • a dental composition for example an oral composition
  • toothpaste - characterized in that it comprises peroxygenated POSs as defined above at as a bleaching agent.
  • Example 1 preparation of a precursor - POS (B) of a peroxide POS according to the invention, this precursor being a polydimethylsiloxane with ends trimethylsilyles and carrying functional substituents of the -propyl-oxy-benzoic type
  • reaction medium After returning to ambient temperature, the reaction medium is neutralized by gradual addition over 1 h 30 min of 1 l of 36% hydrochloric acid (11 moles). The reaction medium becomes milky and it is filtered on a No. 4 frit under vacuum. A white filter cake is obtained which is washed with water (250 ml). To carry out the purification of the allyloxybenzoic acid present in the filter cake, one proceeds by recrystallization.
  • the filter cake 5 l of absolute ethanol and 750 ml of distilled water are charged into the 10 l reactor.
  • the reaction mass is brought to reflux (80 ° C.) and distilled water is gradually added until a single clear phase is obtained, namely 1.75 l of distilled water.
  • reaction mass is then transferred to a 10 l container which is cooled by ice.
  • the medium is left to recrystallize for 16 h and then filtered through a No. 4 frit under vacuum.
  • the cake is washed with distilled water (2 l used three times). Crystals are obtained which are dried under vacuum of 200 mmHg and at 70 ° C. The yield is 35%.
  • the protected product can be purified by vacuum distillation.
  • reaction medium After returning to ambient temperature, the reaction medium is filtered on a cardboard filter under pressure and then the reaction mass is returned to a single-color flask fitted with a magnetic bar.
  • the product is isolated by devolatilization at 120 ° C under vacuum of 1 mmHg.
  • the product thus isolated is deprotected by hydrolysis with distilled water (200 ml) which is poured onto the product to be deprotected in 1 hour 15 minutes and heating to 90 ° C. for 16 hours.
  • the medium becomes whitish.
  • the water is removed at 110 ° C. under a vacuum of 2 mmHg for 4 h 15 min. 58.40 g of hydrosilylated oil of structure B are then obtained.
  • the method used here is fractional precipitation. It is dissolve the grafted oil obtained in 1.3 in a hot alcohol. This alcohol can be more particularly methanol. Then the polymer is precipitated by addition water of basic pH. The operation is repeated another time. The third operation consists in hot solubilizing the silicone polymer in methanol and then adding water at acidic pH. The polymer thus purified is heated to 115 ° C. under a vacuum of 20 mmHg to remove residual water or alcohol. The product is finally placed in the oven at 100 ° C. under atmospheric pressure. A polymer of purity greater than 95% is obtained in weight.
  • Example 2 preparation of a precursor - POS (C) of a peroxide POS according to the invention, this precursor being a polydimethylsiloxane with ends trimethylsilyl and carrying functional substituents of the -propylanhydride type succinic
  • the polymer After placing the middle reaction in a single-color flask fitted with a magnetic bar, the polymer is isolated silicone grafted by devolatilizing the excess oligomer by heating to 180 ° C. under vacuum 2 mmHg. A silicone oil of structure C and of purity equal to 94% is obtained in weight.
  • Example 3 preparation of a precursor - POS (E) of a peroxide POS according to the invention, this precursor being a polydimethylsiloxane with ends trimethylsilyl and carrying functional substituents of the -propyl-succinimide type benzoic
  • EXAMPLE 5 OBTAINING A PEROXIDE POS IN WHICH THE FPO FUNCTIONS (-OO-) OF THE SUBSTITUTES E ARE INCLUDED IN PERACID CARBOXYL REMAINS FROM THE PRECURSOR POS AS EXAMPLE 2 (REMAINING ANHYDRIDES REMAINING)
  • EXAMPLE 6 OBTAINING A PEROXIDE POS IN WHICH THE FPO FUNCTIONS (-OO-) OF THE SUBSTITUTES ARE INCLUDED IN PERACID CARBOXYLIC RESIDUES FROM THE PRECURSOR POS AS EXAMPLE 2 (REMAINING ANHYDRIDES REMAINING)
  • EXAMPLE 8 OBTAINING A PEROXIDE POS IN WHICH THE FPO FUNCTIONS (-OO-) OF THE SUBSTITUTES ARE INCLUDED IN PERACID CARBOXYLIC RESIDUES FROM THE PRECURSOR POS AS EXAMPLE 2 (REMAINING ANHYDRIDES REMAINING)
  • Example 5 is reproduced with the difference that no KOH is used.
  • EXAMPLE 9 OBTAINING A PEROXIDE POS IN WHICH THE FPO FUNCTIONS (-OO-) OF THE SUBSTITUTES E ARE INCLUDED IN PERACID CARBOXYL REMAINS FROM THE PRECURSOR POS AS EXAMPLE 2 (REMAINING ANHYDRIDES REMAINING)
  • Example 6 is reproduced with the difference that the drop of KOH is replaced by a drop of H 3 PO 4 (85% in water).
  • EXAMPLE 10 OBTAINING A PEROXIDE POS IN WHICH THE FPO FUNCTIONS (-OO-) OF THE SUBSTITUTES E ARE INCLUDED IN PERACID CARBOXYLIC RESIDUES FROM THE POS PRECURSOR AS IN EXAMPLE 1 (PENDANT BENZOIC REMAINS)
  • EXAMPLE 11 EVALUATION OF THE WHITENING POWER OF THE POS PEROXIDE OF EXAMPLE 6

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Abstract

The invention concerns polyorganosiloxanes (POS) grafted with peroxide functions and functions stabilizing the latter. Said stabilized peroxidised POS are designed to form a novel oxidizing system useful as bleaching agents, for example or dental or detergent compositions. The invention aims at and succeeds in providing peroxygenated bleaching agents more stable and more efficient than those known in prior art. The inventive stabilized and peroxidised POS correspond for example to the formula (a). The invention also concerns a method for making said peroxidised POS, the precursors thereof and their uses as bleaching agents in dental compositions (toothpaste or detergent compositions).

Description

Le domaine de l'invention est celui des systèmes peroxydés applicables notamment dans le blanchiment. Les propriétés oxydantes de ces systèmes sont plus particulièrement appréciées dans les applications de blanchiment dentaire (e.g. dentifrices).The field of the invention is that of applicable peroxidized systems especially in money laundering. The oxidizing properties of these systems are more particularly appreciated in teeth whitening applications (e.g. toothpaste).

Les systèmes peroxydés visés dans le cadre du présent exposé sont des polymères fonctionnalisés.The peroxidized systems referred to in the context of this presentation are functionalized polymers.

La présente invention concerne des polyorganosiloxanes (POS) peroxydés ainsi que l'un de leurs procédés de préparation.The present invention relates to perorganized polyorganosiloxanes (POS) thus as one of their preparation processes.

L'invention se rapporte également à des précurseurs silicones de ces POS peroxydés.The invention also relates to silicone precursors of these POSs. peroxides.

Enfin, la présente invention comporte un aspect application qui comprend l'utilisation des POS peroxydés selon l'invention comme ingrédient actif en blanchiment. Plus précisément, l'invention vise des compositions dentaires, par exemple dentifrices, comprenant les POS peroxydés comme agent de blanchiment.Finally, the present invention includes an application aspect which comprises the use of peroxidized POSs according to the invention as active ingredient in laundering. More specifically, the invention relates to dental compositions, for example toothpastes, including peroxidized POS as a bleaching agent.

Il est connu dans le domaine du blanchiment, en particulier du blanchiment dentaire, d'utiliser le peroxyde d'hydrogène H2O2 ou ses persels (percarbonates, perborates, peroxydes de calcium). Dans la suite du présent exposé, H2O2 désignera l'H2O2 en tant que telle et ses persels. Les inconvénients de l'eau oxygénée ne sont pas négligeables. En premier lieu, H2O2 doit être employée en forte concentration pour être efficace. Ce point est particulièrement gênant compte tenu de l'agressivité de l'H2O2. En second lieu, on sait que l'action de blanchiment est liée à l'effet donneur d'oxygène. Or cet effet n'est pas l'effet prépondérant que l'on peut obtenir avec l'eau oxygénée. Cette dernière se comporte essentiellement comme un promoteur de radicaux libres délétères, qui ne participent pas à la fonction blanchiment et qui auraient même plutôt tendance à la contrarier. En troisième lieu, l'eau oxygénée a pour inconvénient d'être instable.It is known in the field of whitening, in particular dental whitening, to use hydrogen peroxide H 2 O 2 or its persalts (percarbonates, perborates, calcium peroxides). In the remainder of this description, H 2 O 2 will designate H 2 O 2 as such and its persalts. The disadvantages of hydrogen peroxide are not negligible. First, H 2 O 2 must be used in high concentration to be effective. This point is particularly troublesome given the aggressiveness of H 2 O 2 . Second, we know that the bleaching action is linked to the oxygen-giving effect. However, this effect is not the predominant effect that can be obtained with hydrogen peroxide. The latter behaves essentially as a promoter of deleterious free radicals, which do not participate in the bleaching function and which would even rather tend to thwart it. Third, hydrogen peroxide has the disadvantage of being unstable.

Il existe donc un besoin clairement identifié pour un substitut du peroxyde d'hydrogène pour ces applications dans le domaine du blanchiment et en particulier du blanchiment dentaire (dentifrices).There is therefore a clearly identified need for a peroxide substitute of hydrogen for these applications in the field of bleaching and in particular teeth whitening (toothpaste).

Pour tenter de résoudre la problématique sus-visée, il a été proposé dans le brevet US N° 5 698 326 des composés peracides constitués par un support inorganique formé par de la silice et porteur de fonctionnalités peracides. Ces composés peuvent être obtenus en faisant réagir de la silice substituée par un reste siloxylalkylaminé avec un anhydride triméllitique dont on oxyde ensuite la fonction carboxylique du noyau benzyle, pour la transformer en fonction peracide. Cela correspond à la formule suivante :

Figure 00020001
Selon ce brevet, le greffage de la fonction peracide sur le support inorganique en silice, est sensé permettre une stabilisation de la fonction peracide. En réalité, il s'avère que cette stabilité pourrait encore être améliorée. En outre, il est à craindre que ces silices peroxydées soient difficilement dispersibles dans des compositions relativement visqueuses telles que les dentifrices.In an attempt to resolve the above-mentioned problem, it has been proposed in US Pat. No. 5,698,326 peracid compounds constituted by an inorganic support formed by silica and carrying peracid functionalities. These compounds can be obtained by reacting silica substituted with a siloxylalkylamine residue with a trimellitic anhydride, the carboxylic function of the benzyl ring of which is then oxidized, to transform it into a peracid function. This corresponds to the following formula:
Figure 00020001
According to this patent, the grafting of the peracid function on the inorganic silica support is supposed to allow stabilization of the peracid function. In reality, it turns out that this stability could be further improved. In addition, it is to be feared that these peroxidized silicas are difficult to disperse in relatively viscous compositions such as toothpaste.

La demande de brevet européen N° 796 874 concerne un procédé pour la préparation de polymères comprenant des groupes peroxycarboxyliques. Ces polymères peroxycarboxyliques sont plus précisément des copolymères de N-vinylpyrolidone / anhydride maléique. Le peroxyde d'hydrogène que l'on fait réagir avec ce copolymère permet la transformation des carboxyles issus de l'anhydride en fonctions peroxycarboxyliques. Les performances de ces copolymères peroxycarboxylés, en terme de blanchiment, ne sont pas révélées par cette demande de brevet. Par ailleurs, il semble que dans l'application blanchiment dentaire, les copolymères peroxycarboxylés manquent de sélectivité vis-à-vis des dents. En outre, on peut craindre des problèmes d'instabilité pour des applications blanchiment dentaire de ces copolymères.European patent application No. 796 874 relates to a process for the preparation of polymers comprising peroxycarboxylic groups. These peroxycarboxylic polymers are more specifically copolymers of N-vinylpyrolidone / maleic anhydride. The hydrogen peroxide that we react with this copolymer allows the transformation of the carboxyls derived from the anhydride into peroxycarboxylic functions. The performance of these copolymers peroxycarboxylates, in terms of bleaching, are not revealed by this request patent. Furthermore, it seems that in the teeth whitening application, the peroxycarboxylated copolymers lack selectivity with respect to the teeth. In addition, instability problems can be feared for teeth whitening applications of these copolymers.

La demande de brevet PCT WO 97/02 011 divulgue des compositions orales dentaires comprenant des ingrédients classiques tels que des abrasifs, des liants, des humectants, des surfactants, des sources d'ions fluor ou autres édulcorants, ainsi que deux autres ingrédients essentiels à savoir, d'une part, un aminoalkylsilicone tel qu'un polydiméthylsiloxane comprenant des motifs aminoalkyles du type propylaminoéthylamine dans les chaínes et à leurs extrémités et, d'autre part, un polydiméthylsiloxane comportant des groupements pendants de type polyoxyéthylène et/ou polyoxypropylène et ayant une action de surfactant.
Il n'est nullement question dans ce document de polyorganosiloxanes fonctionnalisés par des motifs peroxydes. Cette composition orale est présentée comme ayant des propriétés anti-plaque et anti-bactérienne améliorée, qui complètent d'excellentes performances de nettoyage. Cette composition orale peut également comprendre des agents de blanchiment appartenant à la famille des sels inorganiques de peracides (persulfates, perborates, percarbonates et peroxydes métalliques).
Ces compositions orales ne donnent pas satisfaction en matière de stabilité, de toxicité, de sélectivité vis-à-vis des dents et d'efficacité de blanchiment par oxydation.
PCT patent application WO 97/02 011 discloses dental oral compositions comprising conventional ingredients such as abrasives, binders, humectants, surfactants, sources of fluorine ions or other sweeteners, as well as two other essential ingredients for namely, on the one hand, an aminoalkylsilicone such as a polydimethylsiloxane comprising aminoalkyl units of the propylaminoethylamine type in the chains and at their ends and, on the other hand, a polydimethylsiloxane comprising pendant groups of polyoxyethylene and / or polyoxypropylene type and having a surfactant action.
There is no question in this document of polyorganosiloxanes functionalized with peroxide units. This oral composition is presented as having improved anti-plaque and anti-bacterial properties, which complement excellent cleaning performance. This oral composition can also comprise bleaching agents belonging to the family of inorganic peracid salts (persulfates, perborates, percarbonates and metal peroxides).
These oral compositions are not satisfactory in terms of stability, toxicity, selectivity with respect to the teeth and efficacy of bleaching by oxidation.

Des polyorganosiloxanes comprenant des groupes esters de peracides carboxyliques ont été décrits dans GB 897,973 et US 3,726,943 ; ils peuvent être utiles comme agents de vulcanisation, comme amorceur de polymérisation, comme agents de couplage...Polyorganosiloxanes comprising ester groups of peracids carboxylic acids have been described in GB 897,973 and US 3,726,943; they can be useful as vulcanizing agents, as polymerization initiator, as coupling agents ...

Dans un tel état de la technique, l'un des objectifs essentiels des inventeurs fut de mettre au point un nouveau système oxydant utilisable notamment dans le blanchiment, ce système oxydant de type peroxydé se devant d'être plus stable et plus efficace que les systèmes connus de l'art antérieur.In such a state of the art, one of the essential objectives of the inventors was to develop a new oxidizing system usable in particular in the bleaching, this peroxidized oxidizing system is having to be more stable and more efficient than the systems known from the prior art.

Un autre objectif essentiel de l'invention est de fournir un système de blanchiment peroxydé notamment pour les applications de blanchiment dentaire qui permette de contrôler la réactivité de la fonction peroxyde, de manière à limiter autant que faire se peut sa transformation en radicaux libres agressifs.Another essential objective of the invention is to provide a system for peroxidized bleaching especially for dental bleaching applications which allows to control the reactivity of the peroxide function, so as to limit as far as possible its transformation into aggressive free radicals.

Un autre objectif essentiel de l'invention est de fournir un système de blanchiment peroxydé utilisable notamment en blanchiment dentaire et doué d'une stabilité au stockage significativement améliorée.Another essential objective of the invention is to provide a system for peroxidized bleaching usable in particular in dental bleaching and endowed with significantly improved storage stability.

Un autre objectif essentiel de l'invention est de fournir un système de blanchiment peroxydé appliqué dans le blanchiment dentaire (composition orale pour le traitement et l'entretien des dents), ayant une meilleure sélectivité vis-à-vis des dents à blanchir.Another essential objective of the invention is to provide a system for peroxide bleaching applied in dental bleaching (oral composition for treatment and maintenance of the teeth), having a better selectivity with respect to teeth to whiten.

Un autre objectif essentiel de l'invention est de fournir un système oxydant peroxydé, susceptible d'être utilisé comme un système à libération contrôlée de fonctions peroxyde oxydantes.Another essential objective of the invention is to provide an oxidizing system peroxidized, capable of being used as a controlled release system of oxidizing peroxide functions.

Un autre objectif essentiel de l'invention est de fournir un procédé d'obtention du système oxydant peroxydé sus-évoqué, qui soit simple à mettre en oeuvre et économique. Another essential objective of the invention is to provide a process for obtaining of the aforementioned peroxidized oxidizing system, which is simple to implement and economic.

Un autre objectif essentiel de l'invention est de prescrire l'utilisation du système oxydant peroxydé sus-visé, à titre d'agent de blanchiment des dents.,Another essential objective of the invention is to prescribe the use of the system peroxidized oxidant mentioned above, as a teeth whitening agent.,

Un autre objectif essentiel de l'invention est de fournir une composition dentaire dotée d'un agent de blanchiment efficace, stable et sélectif.Another essential objective of the invention is to provide a composition dental with an effective, stable and selective bleaching agent.

Ces objectifs, parmi d'autres, sont atteints par la présente invention qui concerne de nouveaux polyorganosiloxanes (POS) comprenant des motifs siloxaniques de formule (I) suivante : RaEbGcSiO 4 - (a+b+c)2

  • dans laquelle :
  • a+b+c=0 à 3
  • a, b, c = 0 à 3
  • R correspond à un ou plusieurs radicaux identiques ou différents, R étant choisi parmi les groupements monovalents hydrocarbonés, de préférence parmi les alkyles linéaires, ramifiés et/ou cycliques et/ou les aryles, et plus préférentiellement encore parmi les alkyles linéaires ou ramifiés en C1-C4 et les groupes phényle, xylyle et tolyle ;
  • E correspond à un ou plusieurs substituants fonctionnels identiques ou différents entre eux, monovalents, choisis parmi les groupements hydrocarbonés (cyclo)aliphatiques et/ou aromatiques et/ou hétérocycliques et porteurs d'une ou plusieurs fonctions peroxyde d'acyle Fpo de formule
    Figure 00040001
    avec X correspondant à H, à un halogène de préférence le chlore ou à un cation permettant de former un sel avec l'anion peroxyde d'acyle et choisi de préférence parmi les éléments des colonnes Ia et IIA de la classification périodique, et comportant éventuellement chacun une ou plusieurs fonctions Fstab stabilisantes de Fpo, identiques ou différentes entre elles et choisies parmi les fonctions susceptibles de se lier par l'intermédiaire de liaisons faibles avec les fonctions Fpo ;
  • G correspond à un ou plusieurs substituants fonctionnels identiques ou différents entre eux et comportant chacun une ou plusieurs fonctions Fstab stabilisantes de Fpo, identiques ou différentes entre elles et choisies parmi les fonctions susceptibles de se lier par l'intermédiaire de liaisons faibles avec les fonctions Fpo ;
  • avec les conditions selon lesquelles :
    • (i) . la concentration en fonctions [Fpo] exprimée par le ratio nombreFpo nombre total d'atomes de silicium dans le POS est définie comme suit :
    • Δ   0 < [Fpo]
    • Δ de préférence   0,01 ≤ [Fpo] ≤ 1,0
    • Δ et plus préférentiellement encore   0,1 ≤ [Fpo] ≤ 0,6.
    • (ii) . la concentration en % molaire en motifs siloxaniques T (a + b + c = 1) et/ou Q (a + b + c = 0) est définie comme suit :
    • Δ   0 ≤ [T et/ou Q] ≤ 20
    • Δ de préférence   0 ≤ [T et/ou Q] ≤10
    • Δ et plus préférentiellement encore,   0≤ [T et/ou Q] ≤ 8.
These objectives, among others, are achieved by the present invention which relates to new polyorganosiloxanes (POS) comprising siloxane units of formula (I) below: R at E b G vs SiO 4 - (a + b + c) 2
  • in which :
  • a + b + c = 0 to 3
  • a, b, c = 0 to 3
  • R corresponds to one or more identical or different radicals, R being chosen from monovalent hydrocarbon groups, preferably from linear, branched and / or cyclic alkyls and / or aryls, and more preferably still from linear or branched C alkyls 1 -C 4 and the phenyl, xylyl and tolyl groups;
  • E corresponds to one or more functional substituents which are identical or different from each other, monovalent, chosen from (cyclo) aliphatic and / or aromatic and / or heterocyclic hydrocarbon groups and carrying one or more acyl peroxide functions Fpo of formula
    Figure 00040001
    with X corresponding to H, preferably a halogen, chlorine or a cation making it possible to form a salt with the anion of acyl peroxide and preferably chosen from the elements of columns Ia and IIA of the periodic table, and optionally comprising each one or more Fstab stabilizing functions of Fpo, identical or different from each other and chosen from functions capable of binding via weak bonds with the Fpo functions;
  • G corresponds to one or more identical or different functional substituents with one another and each comprising one or more Fstab stabilizing functions of Fpo, identical or different between themselves and chosen from the functions capable of binding via weak bonds with the Fpo functions ;
  • with the conditions under which:
    • (i). the concentration of functions [Fpo] expressed by the ratio nombreFpo total number of silicon atoms in the POS is defined as follows:
    • Δ 0 <[Fpo]
    • Δ preferably 0.01 ≤ [Fpo] ≤ 1.0
    • Δ and more preferably still 0.1 ≤ [Fpo] ≤ 0.6.
    • (ii). the concentration in molar% of siloxane units T (a + b + c = 1) and / or Q (a + b + c = 0) is defined as follows:
    • Δ 0 ≤ [T and / or Q] ≤ 20
    • Δ preferably 0 ≤ [T and / or Q] ≤10
    • Δ and more preferably still, 0≤ [T and / or Q] ≤ 8.

Ces nouveaux POS peroxydés permettent de stabiliser la fonction peroxyde d'acyle et de contrôler son activité oxydante en réfrénant son activité de production de radicaux libres. En outre, leurs propriétés de blanchiment et de sélectivité vis-à-vis des dents font d'eux des systèmes de blanchiment particulièrement appropriés et efficaces pour des compositions orales dentaires telles que des dentifrices.These new peroxidized POSs stabilize the function acyl peroxide and to control its oxidative activity by restraining its activity production of free radicals. In addition, their bleaching and selectivity towards teeth makes them whitening systems particularly suitable and effective for dental oral compositions such only toothpaste.

En effet, ces silicones fonctionnalisés par des Fpo peroxyde d'acyle sont doués d'une affinité spécifique vis-à-vis des matériaux constitutifs des dents (en particulier de l'hydroxyapatite) de sorte que ce sont des vecteurs sélectifs propres à acheminer les fonctions de blanchiment chimique sur les dents. Il va de soi que cela optimise l'efficacité desdites fonctions. Il s'ensuit qu'il est possible de réduire les doses, ce qui va tout à fait dans le sens de la diminution de l'agressivité de l'agent de blanchiment.Indeed, these silicones functionalized with Fpo acyl peroxide are endowed with a specific affinity for the constituent materials of teeth (in hydroxyapatite) so these are selective vectors specific to route the chemical whitening functions to the teeth. It goes without saying that optimizes the efficiency of said functions. It follows that it is possible to reduce the doses, which is entirely in line with the decrease in the aggressiveness of the agent laundering.

De surcroít, ces silicones fonctionnalisés peroxydes sont hydrophobes et ont donc pour avantage de préserver les fonctions Fpo de l'eau, qui est un élément d'instabilité majeur pour celles-ci. In addition, these peroxide functional silicones are hydrophobic and have so the advantage of preserving the Fpo functions of water, which is an element major instability for them.

Les nouveaux polyorganosiloxanes peroxydés à fonctions Fpo peuvent être des polymères linéaires et/ou ramifiés et/ou réticulés selon le pourcentage en poids de motifs siloxyles DTQ qu'ils comprennent. De préférence, les POS peroxydés selon l'invention comprennent majoritairement des motifs D (a + b + c = 2) et plus préférentiellement encore sont linéaires.The new peroxidized polyorganosiloxanes with Fpo functions can be linear and / or branched and / or crosslinked polymers according to the percentage by weight of DTQ siloxyl patterns which they include. Preferably, the peroxidized POSs according to the invention mainly comprise units D (a + b + c = 2) and more still preferentially are linear.

Chaque fonction peroxyde d'acyle Fpo appartient à un reste peroxycarboxylique acide, halogénure - chlorure - ou sels. Each Fpo acyl peroxide function belongs to a peroxycarboxylic acid, halide - chloride - or salt residue.

A titre d'exemples de groupements X = cations, ont peut citer : Na+, K+, Ca++, Mg++...As examples of groups X = cations, we can cite: Na + , K + , Ca ++ , Mg ++ ...

Ces restes peroxycarboxyliques sont reliés au silicium de la chaíne du POS par une rotule hydrocarbonée (c'est-à-dire comprenant notamment des atomes de carbone et d'hydrogène), aliphatique et/ou alicyclique et/ou aromatique et/ou héterocyclique comportant éventuellement un ou plusieurs hétéroatomes : N, O, S..., éventuellement.These peroxycarboxylic residues are linked to the silicon of the POS chain by a hydrocarbon ball joint (that is to say comprising in particular carbon and hydrogen atoms), aliphatic and / or alicyclic and / or aromatic and / or heterocyclic optionally comprising one or more heteroatoms: N, O, S ..., possibly.

L'ensemble comprenant :

  • d'une part, le reste peroxycarboxylique,
  • et d'autre part, la rotule,
forme le substituant fonctionnel E.
En pratique, la rotule est, par exemple, du type -alkyl-O-aryle (benzyle), -alkyl anhydride, -alkylimide-aryle (benzyle), entre autres.The set including:
  • on the one hand, the peroxycarboxylic residue,
  • and on the other hand, the patella,
forms the functional substituent E.
In practice, the ball joint is, for example, of the -alkyl-O-aryl (benzyl), -alkyl anhydride, -alkylimide-aryl (benzyl) type, among others.

L'action stabilisante avantageuse des Fstab sur les Fpo est une caractéristique préférée des POS fonctionnalisés selon l'invention. Conformément à cette dernière, les Fstab sont localisées sur les substituants fonctionnels (pendants) E et/ou G. Sans que cela ne soit limitatif, il est préférable que les Fstab soient portées au moins par le
   ou les E, de façon à être proches des Fpo à stabiliser. Il n'est pas interdit de penser que l'effet stabilisant des Fstab est ainsi amélioré.
The advantageous stabilizing action of Fstab on Fpo is a preferred characteristic of the functionalized POSs according to the invention. In accordance with the latter, the Fstabs are located on the functional substituents (pendant) E and / or G. Without this being limiting, it is preferable that the Fstabs are carried at least by the
or the E, so as to be close to the Fpo to be stabilized. It is not forbidden to think that the stabilizing effect of Fstab is thus improved.

Suivant une caractéristique préférée de l'invention, les éventuelles fonctions de stabilisation Fstab des susbstituants E et/ou G de la formule (I) correspondent à des fonctions pouvant générer des liaisons faibles (liaisons hydrogène, e.g.) avec Fpo, et sélectionnées dans le groupe comprenant :

  • les motifs fonctionnels comportant de l'azote et/ou de l'oxygène et/ou du fluor, et/ou du soufre et/ou du phosphore ; les motifs carboxyliques, carboxylates, amides, imides, sulfonamides, hydroxyles, alcoxyles, amines ou organo-fluorés, étant préférés ;
  • les motifs cationiques, de préférence ceux comprenant un ou plusieurs ammoniums quaternaires ;
  • les motifs chélatants comportant une ou plusieurs fonctions éther et/ou une ou plusieurs fonctions amines, et/ou les motifs chélatants phosphonates et/ou sulfonates.
According to a preferred characteristic of the invention, the possible stabilization functions Fstab of the substituents E and / or G of formula (I) correspond to functions which can generate weak bonds (hydrogen bonds, eg) with Fpo, and selected in the group including:
  • functional units comprising nitrogen and / or oxygen and / or fluorine, and / or sulfur and / or phosphorus; the carboxylic, carboxylate, amide, imide, sulfonamide, hydroxyl, alkoxyl, amine or organofluoric units being preferred;
  • cationic units, preferably those comprising one or more quaternary ammoniums;
  • chelating units comprising one or more ether functions and / or one or more amine functions, and / or phosphonate and / or sulfonate chelating units.

Les éventuels substituants fonctionnels G comprennent chacun, outre la ou les Fstab, une rotule qui assure la liaison avec la chaíne silicone. Les rotules des substituants G sont identiques ou différentes entre elles, qui répondent à la même définition que celle donnée supra pour les rotules des substituants E.The optional functional substituents G each include, in addition to the one or more Fstab, a ball joint which ensures the connection with the silicone chain. The ball joints of the substituents G are identical or different from each other, which meet the same definition as that given above for the ball joints of substituents E.

Les POS peroxydés faisant l'objet de l'invention peuvent être obtenus :

  • soit à partir de chlorosilanes ou d'alcoxysilanes portant les substituants E , de chlorosilanes ou d'alcoxysilanes portant des substituants G et de chlorosilanes ou d'alcoxysilanes portant les substituants R et/ou l'hydrogène, par cohydrolyse, polycondensation et polymérisation des produits hydrolysés en présence de diorganosiloxanes cycliques ou redistribution en présence de polydiorganosiloxanes...
  • soit à partir de polydiorganosiloxanes fonctionnalisés par hydrosilylation de polydiorganosiloxanes hydrogénés à l'aide de précurseurs oléfiniques intégraux ou partiels des substituants fonctionnels E et G.
    Au sens du présent exposé, les termes "précurseurs oléfiniques intégraux ou partiels" correspondent respectivement :
    • au cas où le précurseur oléfinique est sous forme finale et n'a pas à subir d'autres greffages pour conduire à l'intégralité du substituant qui sera transformé en E ou G après peroxydation (rotule intégrale),
    • et au cas où la rotule des substituants E ou G est formée par plusieurs chaínons mis bout à bout et correspondant à des formes intermédiaires de synthèse, le précurseur oléfinique constituant le premier chaínon qui est lié, d'une part, à la chaíne silicone et, d'autre part, au chaínon suivant de la rotule.
The peroxidized POSs which are the subject of the invention can be obtained:
  • either from chlorosilanes or alkoxysilanes carrying the substituents E, from chlorosilanes or alkoxysilanes carrying the substituents G and from chlorosilanes or alkoxysilanes carrying the substituents R and / or hydrogen, by cohydrolysis, polycondensation and polymerization of the products hydrolyzed in the presence of cyclic diorganosiloxanes or redistribution in the presence of polydiorganosiloxanes ...
  • either from polydiorganosiloxanes functionalized by hydrosilylation of hydrogenated polydiorganosiloxanes using integral or partial olefin precursors of the functional substituents E and G.
    For the purposes of this description, the terms "integral or partial olefin precursors" correspond respectively:
    • in the case where the olefinic precursor is in final form and does not have to undergo other grafting to lead to the entirety of the substituent which will be transformed into E or G after peroxidation (integral ball joint),
    • and in the case where the ball joint of the substituents E or G is formed by several chains placed end to end and corresponding to intermediate forms of synthesis, the olefinic precursor constituting the first chain which is linked, on the one hand, to the silicone chain and , on the other hand, to the next link of the ball joint.

Sans que cela ne soit limitatif, on préfère conformément à l'invention les POS peroxydés obtenus par hydrosilylation de précurseurs oléfiniques de substituants E et G.
Ces réactions d'hydrosilylation peuvent être réalisées à une température de l'ordre de 15 à 200° C, de préférence de l'ordre de 20 à 100° C, en présence d'un catalyseur à base d'un métal du groupe du platine. On peut citer en particulier les dérivés complexes du platine décrits dans les brevets US N° 3 715 334, 3 775 452, 3 814 730, 3 159 601, 3 159 662.
Les quantités de catalyseurs platiniques mises en oeuvre sont de l'ordre de 1 à 300 parties par million, exprimées en métal par rapport au milieu réactionnel.
Les précurseurs oléfiniques mis en oeuvre dans ces hydrosilylations ne comportent pas les fonctions peroxyde d'acyle Fpo, mais leurs formes non péroxygénées F'po ou toutes formes intermédiaires de celles-ci. Il est préférable conformément à l'invention de prévoir une protection des fonctions précurseurs F'po avant l'hydrosilylation.
Les POS greffés par hydrosilylation et porteurs des fonctions précurseurs F'po, sont éventuellement purifiés puis soumis à une oxydation qui permet la transformation des fonctions F'po en fonctions Fpo.
Without this being limiting, peroxidized POSs obtained by hydrosilylation of olefinic precursors of substituents E and G are preferred in accordance with the invention.
These hydrosilylation reactions can be carried out at a temperature of the order of 15 to 200 ° C, preferably of the order of 20 to 100 ° C, in the presence of a catalyst based on a metal from the group of platinum. Mention may in particular be made of the complex platinum derivatives described in US Pat. Nos. 3,715,334, 3,775,452, 3,814,730, 3,159,601, 3,159,662.
The quantities of platinum catalysts used are of the order of 1 to 300 parts per million, expressed as metal relative to the reaction medium.
The olefinic precursors used in these hydrosilylations do not comprise the acyl peroxide functions Fpo, but their non-peroxygenated forms F'po or any intermediate forms thereof. It is preferable in accordance with the invention to provide protection for the precursor functions F'po before hydrosilylation.
The POS grafted by hydrosilylation and carrying the F'po precursor functions, are optionally purified and then subjected to an oxidation which allows the transformation of the F'po functions into Fpo functions.

Selon une forme préférée de réalisation de l'invention, les POS peroxydés répondent à la formule (II) donnée ci-après :

Figure 00090001
   dans laquelle :

  • R1 R3 représentant indépendamment un hydrogène, un hydroxyle ou un reste monovalent répondant à la même définition que celle donnée pour R supra ;
  • R2 représentent indépendamment l'hydrogène, un hydroxyle ou un reste monovalent répondant à la même définition que celle donnée pour R supra ;
  •    2 ≤ m + n + o ≤ 300
    de préférence   3 ≤ m + n + o ≤ 50
    et plus préférentiellement encore   5 ≤ m + n + o ≤ 20
  •    0 ≤ m ≤ 200
    de préférence   1≤ m ≤ 100
    et plus préférentiellement encore   1 ≤ m ≤ 10
  •    0 ≤ n ≤ 50
    de préférence   1 ≤ n ≤ 10
    et plus préférentiellement encore   2 ≤ n ≤ 4
  •    0 ≤ o ≤ 50
    de préférence   1 ≤ o ≤ 10
    et plus préférentiellement encore   2 ≤ o ≤ 4.
According to a preferred embodiment of the invention, the peroxidized POSs correspond to the formula ( II ) given below:
Figure 00090001
in which :
  • R 1 R 3 independently representing a hydrogen, a hydroxyl or a monovalent residue corresponding to the same definition as that given for R above;
  • R 2 independently represent hydrogen, a hydroxyl or a monovalent residue corresponding to the same definition as that given for R above;
  • 2 ≤ m + n + o ≤ 300
    preferably 3 ≤ m + n + o ≤ 50
    and more preferably still 5 ≤ m + n + o ≤ 20
  • 0 ≤ m ≤ 200
    preferably 1≤ m ≤ 100
    and more preferably still 1 ≤ m ≤ 10
  • 0 ≤ n ≤ 50
    preferably 1 ≤ n ≤ 10
    and more preferably still 2 ≤ n ≤ 4
  • 0 ≤ o ≤ 50
    preferably 1 ≤ o ≤ 10
    and more preferably still 2 ≤ o ≤ 4.

De manière plus préférée encore, les polyorganosiloxanes sont caractérisés en ce que :

  • Δ R1 R3 = alkyle en C1-C3, de préférence - CH3
  • Δ R2 = alkyle en C1-C3, de préférence - CH3
  • Δ le ou les substituants fonctionnels E, comprennent à la fois des fonctions Fpo et Fstab.
  • Even more preferably, the polyorganosiloxanes are characterized in that:
  • Δ R 1 R 3 = C 1 -C 3 alkyl, preferably - CH 3
  • Δ R 2 = C 1 -C 3 alkyl, preferably - CH 3
  • Δ the functional substituent (s) E, comprise both Fpo and Fstab functions.
  • En pratique, sans que cela ne soit limitatif, les substituants fonctionnels E des POS peroxydés comprennent chacun une rotule comprenant au moins un motif bicarboxylé et/ou benzoxylé et/ou imide.In practice, without this being limiting, the functional substituents E of Peroxidized POSs each include a ball joint comprising at least one pattern bicarboxylated and / or benzoxylated and / or imide.

    Le cas où la ou les rotules du ou des substituants fonctionnels E comprennent au moins un motif bicarboxylique, correspond à une forme préférée de l'invention dans laquelle la fonction Fpo est obtenue à partir d'un anhydride qui se transforme, d'une part, en une fonction peroxyde d'acyle Fpo et, d'autre part, en fonction acide carboxylique Fstab de stabilisation de la Fpo voisine.The case where the ball joint (s) of the functional substituent (s) E comprise at least one bicarboxylic motif, corresponds to a preferred form of the invention in which the Fpo function is obtained from an anhydride which is transformed, on the one hand, in an acyl peroxide function Fpo and, on the other hand, in an acid function Fstab carboxylic stabilization of neighboring Fpo.

    Les POS peroxydés selon l'invention sont stables et présentent un fort pouvoir blanchissant.The peroxidized POSs according to the invention are stable and have a high power whitening.

    Selon un autre de ses aspects, la présente invention concerne un procédé de préparation des POS tels que définis ci-dessus. Ce procédé est caractérisé en ce qu'il consiste essentiellement à oxyder les précurseurs polysiloxaniques des POS peroxydés visés. Cette oxydation est effectuée à l'aide d'au moins un oxydant de préférence choisi dans le groupe comprenant : H2O2, O2, O3 et leurs mélanges, Ces précurseurs POS de POS peroxydés se distinguent des POS peroxydés visés en ce qu'ils comportent une ou plusieurs fonctions F'po, précurseurs de Fpo et constituées :
    par des restes carboxyles :

    Figure 00100001
    avec X' répondant à la même définition que celle donnée pour X supra ;
    et/ou par des restes anhydrides d'acide
    Figure 00100002
    According to another of its aspects, the present invention relates to a process for the preparation of POSs as defined above. This process is characterized in that it essentially consists in oxidizing the polysiloxane precursors of the targeted peroxidized POSs. This oxidation is carried out using at least one oxidant preferably chosen from the group comprising: H 2 O 2 , O 2 , O 3 and their mixtures, These peroxidized POS precursors of POS are distinguished from the targeted peroxidized POS in that they comprise one or more F'po functions, Fpo precursors and consisting of:
    by carboxyl residues:
    Figure 00100001
    with X 'corresponding to the same definition as that given for X above;
    and / or by acid anhydride residues
    Figure 00100002

    Ces fonctions F'po peuvent être terminales ou incluses dans un cycle.These F'po functions can be final or included in a cycle.

    Comme cela est indiqué ci-avant, les précurseurs polysiloxaniques à fonctions F'po peuvent être obtenus par cohydrolyse de chlorosilanes et d'alcoxysilanes non fonctionnalisés et de chlorosilanes ou d'alcoxysilanes fonctionnalisés par des substituants E et G. L'étape qui suit la cohydrolyse peut être une polycondensation et une polymérisation des produits hydrolyse, en présence des diorganosiloxanes cycliques ou une étape de redistribution en présence de polydiorganosiloxanes. Ces synthèses classiques de POS par cohydrolyse / polycondensation / polymérisation ou par cohydrolyse / redistribution sont décrites notamment dans "W. NELL chemistry and technology of silicones. Edition Academic Press .1968."As indicated above, the polysiloxane precursors with functional F'po can be obtained by cohydrolysis of chlorosilanes and non-alkoxysilanes functionalized and chlorosilanes or alkoxysilanes functionalized with substituents E and G. The stage which follows the cohydrolysis can be a polycondensation and polymerization of hydrolysis products in the presence of diorganosiloxanes cyclic or a redistribution step in the presence of polydiorganosiloxanes. These classic POS syntheses by cohydrolysis / polycondensation / polymerization or by cohydrolysis / redistribution are described in particular in "W. NELL chemistry and technology of silicones. Academic Press Edition. 1968. "

    Selon une alternative préférée, les produits de départ utilisés peuvent être des polyorganosiloxanes hydrogénés qui peuvent être fonctionnalisés en les faisant réagir selon une réaction d'hydrosilylation (addition avec des précurseurs oléfiniques des substituants E et G.). On se reportera supra pour plus de détail sur cette hydrosilylation.According to a preferred alternative, the starting materials used can be hydrogenated polyorganosiloxanes which can be functionalized by reacting them according to a hydrosilylation reaction (addition with olefinic precursors of substituents E and G.). See above for more details on this hydrosilylation.

    Suivant une caractéristique préférée de l'invention, les précurseurs de POS peroxydés que l'on soumet à une oxydation pour obtenir des POS peroxydés visés sont sélectionnés parmi les précurseurs polyorganosiloxaniques

    • porteurs de fonctions F'po anhydrides, l'oxydation étant effectuée à l'aide d'H2O2 en présence d'un catalyseur de type base forte, de préférence la potasse ;
    • et/ou porteurs de fonctions F'po carboxyliques - de préférence benzoyles-, l'oxydation étant effectuée à l'aide d'H2O2 en présence d'un catalyseur de type acide fort.
    According to a preferred characteristic of the invention, the peroxidized POS precursors which are subjected to oxidation in order to obtain targeted peroxidized POS are selected from polyorganosiloxane precursors
    • carrying F'po anhydride functions, the oxidation being carried out using H 2 O 2 in the presence of a catalyst of the strong base type, preferably potassium hydroxide;
    • and / or carriers of F'po carboxylic functions - preferably benzoyl-, the oxidation being carried out using H 2 O 2 in the presence of a catalyst of strong acid type.

    D'une manière plus préférée encore, les précurseurs polyorganosiloxaniques sont porteurs de fonctions F'po anhydride succinique reliées aux atomes de silicium par une rotule -(CH2)3-.Even more preferably, the polyorganosiloxane precursors carry functions F'po succinic anhydride linked to the silicon atoms by a ball joint - (CH 2 ) 3 -.

    Conformément à l'invention, il est apparu particulièrement avantageux que les précurseurs - POS présentent avant l'étape d'oxydation permettant de transformer les F'po en Fpo, une pureté molaire ≥ 90 %, de préférence ≥ 95 %.In accordance with the invention, it appeared particularly advantageous that the precursors - POS present before the oxidation step to transform the F'po en Fpo, a molar purity ≥ 90%, preferably ≥ 95%.

    En pratique, cette étape de purification est effectuée par toute méthode connue et appropriée comme par exemple la dévolatilisation ou la précipitation fractionnée dans un solvant organique tel que le méthanol.
    S'agissant plus précisément de l'étape d'oxydation, on a vu que les agents oxydants pouvaient être l'eau oxygénée, l'oxygène, l'ozone et leurs mélanges.
    In practice, this purification step is carried out by any known and appropriate method such as, for example, devolatilization or fractional precipitation in an organic solvent such as methanol.
    As regards more specifically the oxidation step, it has been seen that the oxidizing agents could be hydrogen peroxide, oxygen, ozone and their mixtures.

    Dans le cas où l'agent oxydant est constitué par le peroxyde d'hydrogène, le catalyseur employé peut être une base forte, par exemple, une base minérale telle que KOH ou NaOH ou bien encore un acide fort, par exemple, un acide minéral tel que H2SO4 ou organique tel que MeSO3H. Les solvants mis en oeuvre dans ces cas de figure sont, par exemple, l'acétate d'éthyle ou Me SO3H.In the case where the oxidizing agent consists of hydrogen peroxide, the catalyst used can be a strong base, for example, a mineral base such as KOH or NaOH or even a strong acid, for example, a mineral acid such as H 2 SO 4 or organic such as MeSO 3 H. The solvents used in these cases are, for example, ethyl acetate or Me SO 3 H.

    Dès lors que l'agent oxydant est l'oxygène, il est envisageable d'employer un catalyseur comprenant du Co2+.As soon as the oxidizing agent is oxygen, it is possible to use a catalyst comprising Co 2+ .

    En pratique, cette étape d'oxydation peut se dérouler à température et à pression ambiante.In practice, this oxidation step can take place at temperature and pressure room.

    Les POS peroxydés selon l'invention sont particulièrement adaptés comme agent de blanchiment et plus particulièrement encore comme agent de blanchiment des dents, compte tenu de leurs propriétés de sélectivité vis-à-vis des dents de non-toxicité, de réactivité contrôlée des fonctions peroxydes Fpo (limitation de la production de radicaux libres), de non-toxicité et de haute efficacité à faible dose. The peroxidized POSs according to the invention are particularly suitable as bleaching agent and more particularly as a bleaching agent teeth, taking into account their properties of selectivity with respect to non-toxicity teeth, of controlled reactivity of the Fpo peroxide functions (limitation of the production of free radicals), non-toxicity and high efficiency at low doses.

    D'où il s'ensuit que la présente invention a également pour objet une composition dentaire (par exemple une composition orale) - en particulier dentifrice - caractérisée en ce qu'elle comprend des POS peroxygénés tels que définis ci-dessus à titre d'agent de blanchiment.From which it follows that the present invention also relates to a dental composition (for example an oral composition) - in particular toothpaste - characterized in that it comprises peroxygenated POSs as defined above at as a bleaching agent.

    Sans que cela ne soit limitatif, on peut donner quelques détails qui définissent qualitativement et quantitativement la composition dentaire selon l'invention en indiquant que celle-ci contient :

    • des POS peroxygénés
      à raison de 0,1 à 40 % en poids,
      de préférence de 0,1 à 10 % en poids,
      et plus préférentiellement encore de l'ordre de 1 à 5 % en poids ;
    • des abrasifs polissants à raison de 5 à 40 % en poids,
      de préférence de 5 à 35 % en poids, ces abrasifs pouvant être notamment la silice, le carbonate de calcium précipité, le carbonate de magnésium, les phosphates de calcium, les oxydes de titane de zinc ou d'étain, le talc, le kaolin, des particules abrasives comprenant un coeur de matériau calcique, de préférence en carbonate de calcium et une écorce de produit idrophobe, de préférence un sel d'acide gras et plus préférentiellement encore un stéarate de Na ;
    • un ou plusieurs composés fluorés correspondant à une concentration de l'ordre de 0,005 à 2 %, de préférence de 0,1 à 1 % en poids de fluor dans ladite composition, ces composés fluorés pouvant être en particulier les sels de l'acide monofluorophosphorique notamment ceux de sodium potassium, lithium, calcium, aluminium, et ammonium ou les fluorures de métaux alcalins, de sodium notamment ;
    • éventuellement des agents tensio-actifs anioniques, non-ioniques, amphotères ou zwitterioniques, à raison d'environ 0,1 à 10 %, de préférence d'environ 1 à 5 % du poids de ladite composition ; on peut citer, à titre d'exemple :
      • des tensio-actifs anioniques comme les sels de sodium, de magnésium, d'ammonium, d'éthanolamine, des
        • alkyl sulfates en C8-C18 pouvant éventuellement contenir jusqu'à 10 motifs oxyéthylène et ou oxypropylène (laurylsulfate de sodium notamment)
        • alkyl sulfoacétates en C8-C18 (laurylsulfoacétate de sodium notamment)
        • alkyl sulfoacétates en C8-C18 (dioctylsulfosuccinate de sodium notamment)
        • alkyl sarcosinates en C8-C18 (laurylsarcosinate de sodium notamment)
        • alkyl phosphates en C8-C18 pouvant éventuellement contenir jusqu'à 10 motifs oxyéthylène et ou oxypropylène
        • alkyl éther carboxylates en C8-C18 contenant jusqu'à 10 motifs oxyéthylène et ou oxypropylène
        • les monoglycérides sulfatés...
      • des agents tensio-actifs non-ioniques comme les esters gras de sorbitan éventuellement polyéthoxylés, les acides gras éthoxylés, les esters de polyéthylèneglycol, ou encore les alcools gras polyéther,
      • agents tensio-actifs amphotères comme les bétaines, sulfobétaines
    • éventuellement de l'eau à raison d'environ 0,1 à 50 %, de préférence environ 0,5 à 40 % du poids de ladite composition
    • éventuellement des agents humectants, à raison d'environ 10 à 85 %, de préférence de 10 à 70 % du poids de ladite composition, humectants comme le glycérol, le sorbitol, les polyéthylèneglycols, le lactilol, le xylitol ...
    • éventuellement des agents épaississants comme certaines silice utilisées à cet effet (TIXOSIL 43® commercialisée par RHONE-POULENC...) à raison de 5 à 15 % en poids et/ou des polymères utilisés seuls ou en association comme la gomme Xanthane, la gomme guar, les dérivés de la cellulose (Carboxyméthylcellulose, hydroxyéthylcellulose, hydroxypropylcellulose, hydroxypropylméthylcellulose....), des polyacrylates réticulés comme les CARBOPOL® distribués par GOODRICH, les alginates ou des carraghénannes, de la VISCARIN®, à raison de 0,1 à 5 % en poids.
    • éventuellement des agents thérapeutiques bactéricides, anti-microbiens, anti-plaque, comme le citrate de zinc, les polyphosphates, les guanidines, les bis-biguanides ou autre composé organique thérapeutique cationique,
    • éventuellement des agents arômatisants, (essence d'anis, de badiane, de menthe, de genièvre, cannelle, girofle, rose, ), des édulcorants, des colorants (chlorophylle), des conservateurs...
    Without being limiting, we can give some details which define qualitatively and quantitatively the dental composition according to the invention, indicating that it contains:
    • peroxygenated POS
      at a rate of 0.1 to 40% by weight,
      preferably from 0.1 to 10% by weight,
      and more preferably still on the order of 1 to 5% by weight;
    • polishing abrasives at a rate of 5 to 40% by weight,
      preferably from 5 to 35% by weight, these abrasives possibly being in particular silica, precipitated calcium carbonate, magnesium carbonate, calcium phosphates, oxides of zinc or tin titanium, talc, kaolin , abrasive particles comprising a core of calcium material, preferably calcium carbonate and a shell of an idrophobic product, preferably a fatty acid salt and more preferably still a Na stearate;
    • one or more fluorinated compounds corresponding to a concentration of the order of 0.005 to 2%, preferably 0.1 to 1% by weight of fluorine in said composition, these fluorinated compounds possibly being in particular the salts of monofluorophosphoric acid especially those of sodium potassium, lithium, calcium, aluminum, and ammonium or the fluorides of alkali metals, especially sodium;
    • optionally anionic, nonionic, amphoteric or zwitterionic surfactants, at a rate of about 0.1 to 10%, preferably about 1 to 5% of the weight of said composition; we can cite, by way of example:
      • anionic surfactants such as sodium, magnesium, ammonium, ethanolamine salts,
        • C 8 -C 18 alkyl sulphates which may optionally contain up to 10 oxyethylene and or oxypropylene units (especially sodium lauryl sulphate)
        • C 8 -C 18 alkyl sulfoacetates (especially sodium lauryl sulfoacetate)
        • C 8 -C 18 alkyl sulfoacetates (especially sodium dioctylsulfosuccinate)
        • C 8 -C 18 alkyl sarcosinates (especially sodium laurylsarcosinate)
        • C 8 -C 18 alkyl phosphates which may optionally contain up to 10 oxyethylene and or oxypropylene units
        • C 8 -C 18 alkyl ether carboxylates containing up to 10 oxyethylene and or oxypropylene units
        • sulfated monoglycerides ...
      • nonionic surfactants such as optionally polyethoxylated sorbitan fatty esters, ethoxylated fatty acids, polyethylene glycol esters, or alternatively polyether fatty alcohols,
      • amphoteric surfactants such as betaines, sulfobetaines
    • optionally water in an amount of about 0.1 to 50%, preferably about 0.5 to 40% of the weight of said composition
    • optionally humectants, at a rate of approximately 10 to 85%, preferably from 10 to 70% of the weight of said composition, humectants such as glycerol, sorbitol, polyethylene glycols, lactilol, xylitol, etc.
    • optionally thickening agents such as certain silica used for this purpose (TIXOSIL 43® marketed by RHONE-POULENC ...) at a rate of 5 to 15% by weight and / or polymers used alone or in combination such as Xanthan gum, gum guar, cellulose derivatives (Carboxymethylcellulose, hydroxyethylcellulose, hydroxypropylcellulose, hydroxypropylmethylcellulose ....), crosslinked polyacrylates such as CARBOPOL® distributed by GOODRICH, alginates or carrageenans, VISCARIN®, at a rate of 0.1 to 5% by weight.
    • optionally bactericidal, anti-microbial, anti-plaque therapeutic agents, such as zinc citrate, polyphosphates, guanidines, bis-biguanides or other organic cationic therapeutic compound,
    • possibly flavoring agents (essence of anise, star anise, mint, juniper, cinnamon, clove, rose,), sweeteners, colors (chlorophyll), preservatives ...

    La composition dentifrice faisant l'objet de l'invention, peut se présenter :

  • Figure 00140001
    sous différentes formes (pâtes, gels, crèmes), préparées à l'aide des procédés conventionnels,
  • et sous divers conditionnements (e.g. mono ou bicompartiment).
  • The toothpaste composition which is the subject of the invention can be presented:
  • Figure 00140001
    in different forms (pasta, gels, creams), prepared using conventional methods,
  • and under various packaging (eg mono or bi-compartment).
  • La présente invention sera mieux comprise à l'aide des exemples non-limitatifs qui suivent et qui font également ressortir certains des avantages et les variantes d'exécution de l'invention. On présente dans ces exemples la préparation des POS précurseurs des POS peroxydés selon l'invention, la transformation par oxydation de ces précurseurs en POS peroxydés, et l'évaluation de ces derniers en terme de stabilité au stockage et de pouvoir blanchissant.The present invention will be better understood using non-limiting examples which also highlight some of the benefits and variations of the invention. We present in these examples the preparation of POS precursors of peroxidized POSs according to the invention, the transformation by oxidation of these peroxidized POS precursors, and the evaluation of these in terms of storage stability and bleaching power.

    EXEMPLESEXAMPLES Exemple 1 : préparation d'un précurseur - POS (B) d'un POS peroxyde selon l'invention, ce précurseur étant un polydiméthylsiloxane à extrémités trimethylsilyles et porteur de substituants fonctionnels de type -propyl-oxy-benzoïqueExample 1: preparation of a precursor - POS (B) of a peroxide POS according to the invention, this precursor being a polydimethylsiloxane with ends trimethylsilyles and carrying functional substituents of the -propyl-oxy-benzoic type

    Figure 00150001
    Figure 00150001

    1.1. Synthèse de l'acide allyloxybenzoïque1.1. Synthesis of allyloxybenzoic acid

    Dans un réacteur de 10 l muni d'un réfrigérant, d'une ampoule de coulée, d'une agitation mécanique, d'une sonde thermomètre et sous ciel d'argon, on charge 500 ml d'eau distillée, 51 d'éthanol absolu et progressivement 450,9 g de potasse (8,02 moles) sous forte agitation (240t/min). Une fois la potasse dissoute, on charge 558,3 g d'acide 4-hydroxy benzoïque (4,04 moles). La masse réactionnelle se trouble puis devient limpide. Le bromure d'allyle (489,0 g soit 4,04 moles) est alors coulé en 2h à température ambiante. Après la coulée, le milieu réactionnel est porté à 80°C pendant 17 heures.
    Après retour à la température ambiante, le milieu réactionnel est neutralisé par addition progressive en 1h30 de 1 l d'acide chlorhydrique à 36% (11 moles). Le milieu réactionnel devient laiteux et il est filtré sur fritte n°4 sous vide. On obtient un gâteau de filtration blanc qui est lavé à l'eau (250 ml).
    Pour effectuer la purification de l'acide allyloxybenzoïque se trouvant dans le gâteau de filtration, on procède par recristallisation. Dans le réacteur de 10 l, on charge le gâteau de filtration, 5 l d'éthanol absolu et 750 ml d'eau distillée. La masse réactionnelle est portée à reflux (80°C) et on ajoute progressivement de l'eau distillée jusqu'à obtenir une seule phase limpide soit 1,75 l d'eau distillée. La masse réactionnelle est alors transvasée dans un récipient de 10 l qui est refroidi par de la glace. On laisse le milieu se recristalliser pendant 16 h puis on filtre sur fritté n°4 sous vide. Le gâteau est lavé à l'eau distillée (2 l utilisé en trois fois). On obtient des cristaux qui sont séchés sous vide de 200 mmHg et à 70°C.
    Le rendement est de 35%.
    500 ml of distilled water, 51 of ethanol are charged into a 10 l reactor fitted with a condenser, a dropping funnel, a mechanical stirrer, a thermometer probe and under an argon sky. absolute and gradually 450.9 g of potash (8.02 moles) with vigorous stirring (240 rpm). Once the potassium has dissolved, 558.3 g of 4-hydroxy benzoic acid (4.04 moles) are charged. The reaction mass becomes cloudy and then becomes clear. The allyl bromide (489.0 g or 4.04 moles) is then poured in 2 hours at room temperature. After casting, the reaction medium is brought to 80 ° C for 17 hours.
    After returning to ambient temperature, the reaction medium is neutralized by gradual addition over 1 h 30 min of 1 l of 36% hydrochloric acid (11 moles). The reaction medium becomes milky and it is filtered on a No. 4 frit under vacuum. A white filter cake is obtained which is washed with water (250 ml).
    To carry out the purification of the allyloxybenzoic acid present in the filter cake, one proceeds by recrystallization. The filter cake, 5 l of absolute ethanol and 750 ml of distilled water are charged into the 10 l reactor. The reaction mass is brought to reflux (80 ° C.) and distilled water is gradually added until a single clear phase is obtained, namely 1.75 l of distilled water. The reaction mass is then transferred to a 10 l container which is cooled by ice. The medium is left to recrystallize for 16 h and then filtered through a No. 4 frit under vacuum. The cake is washed with distilled water (2 l used three times). Crystals are obtained which are dried under vacuum of 200 mmHg and at 70 ° C.
    The yield is 35%.

    1. 2. Protection de l'acide allyloxybenzoïque par un groupement triméthylsilyle: 1. 2. Protection of allyloxybenzoic acid by a trimethylsilyl group:

    Dans un tricol de 250 ml muni d'un réfrigérant, d'une agitation mécanique, d'une sonde thermomètre et sous ciel d'argon, on introduit 53,62 g d'acide allyloxybenzoïque préparé en 1.1. (0,3 mole) et on coule en 1 heure 120,58 g d'hexaméthyldisilazane (0,75 mole). Le milieu réactionnel est laissé en contact à 130°C pendant 24 heures. On obtient après retour à température ambiante une solution d'acide allyloxybenzoïque protégé en solution dans l'hexaméthyldisilazane. In a 250 ml three-necked flask fitted with a condenser, mechanical agitation, thermometer probe and under argon sky, 53.62 g of acid are introduced allyloxybenzoic acid prepared in 1.1. (0.3 mole) and poured in 1 hour 120.58 g hexamethyldisilazane (0.75 mole). The reaction medium is left in contact with 130 ° C for 24 hours. After returning to room temperature, protected allyloxybenzoic acid solution in solution in hexamethyldisilazane.

    Il est possible de purifier le produit protégé par distillation sous vide.The protected product can be purified by vacuum distillation.

    1.3. Hydrosilylation de l'acide allyloxybenzoïque protégé: 1.3. Hydrosilylation of protected allyloxybenzoic acid:

    Dans un tricol de 250 ml muni d'un réfrigérant, d'une ampoule de coulée, d'une agitation mécanique, d'une sonde thermomètre et sous ciel d'argon, on introduit 87,01 g de la solution d'acide protégé obtenue en 1.2 (0,15 mole d'acide protégé) et 31,0 mg de catalyseur platinique. Le milieu réactionnel est porté à 80°C et mis sous agitation. Puis, on coule en 45 minutes sur le milieu réactionnel 35,03 g d'huile de structure A (0,13 mole de fonction SiH). Le milieu réactionnel est ensuite laissé en contact 16 heures. Au cours de ce temps de contact on rajoute 7,5 mg de PtCl2(PhCN)2.
    A 85°C, on ajoute 2% massique de noir de carbone que l'on laisse en contact pendant 16 heures. Après retour à la température ambiante, on filtre le milieu réactionnel sur filtre carton sous pression puis on remet la masse réactionnelle dans un ballon monocol muni d'un barreau aimanté. On isole le produit par dévolatilisation à 120°C sous vide de 1 mmHg.
    Le produit ainsi isolé est déprotégé par hydrolyse à l'eau distillée (200 ml) que l'on coule sur le produit à déprotéger en 1h15 et chauffage à 90°C 16 heures. Le milieu devient blanchâtre. On élimine l'eau à 110°C sous vide de 2 mmHg pendant 4h15. On obtient alors 58,40 g d'huile hydrosilylée de structure B.
    87.01 g of the protected acid solution are introduced into a 250 ml three-necked flask fitted with a condenser, a dropping funnel, a mechanical stirrer, a thermometer probe and under an argon sky. obtained in 1.2 (0.15 mole of protected acid) and 31.0 mg of platinum catalyst. The reaction medium is brought to 80 ° C. and stirred. Then, poured in 45 minutes on the reaction medium 35.03 g of oil of structure A (0.13 mole of SiH function). The reaction medium is then left in contact for 16 hours. During this contact time, 7.5 mg of PtCl 2 (PhCN) 2 are added .
    At 85 ° C., 2% by mass of carbon black is added which is left in contact for 16 hours. After returning to ambient temperature, the reaction medium is filtered on a cardboard filter under pressure and then the reaction mass is returned to a single-color flask fitted with a magnetic bar. The product is isolated by devolatilization at 120 ° C under vacuum of 1 mmHg.
    The product thus isolated is deprotected by hydrolysis with distilled water (200 ml) which is poured onto the product to be deprotected in 1 hour 15 minutes and heating to 90 ° C. for 16 hours. The medium becomes whitish. The water is removed at 110 ° C. under a vacuum of 2 mmHg for 4 h 15 min. 58.40 g of hydrosilylated oil of structure B are then obtained.

    1.4. Purification d'une huile silicone B à fonctions acide benzoïque:1.4. Purification of a silicone oil B with benzoic acid functions :

    On part d'une huile pure à 92% massique avec 8% massique constitué d'oligomères non greffés provenant de l'acide allyloxybenzoïque non greffé ou d'isomères de l'acide allyloxybenzoïque. Parmi les différentes techniques de purification plusieurs sont possibles. La méthode mise en oeuvre ici est la précipitation fractionnée. Il s'agit de solubiliser l'huile greffée obtenue en 1.3 dans un alcool à chaud. Cet alcool peut être plus particulièrement du méthanol. Puis on fait précipiter le polymère par addition d'eau de pH basique. L'opération est répétée une autre fois. La troisième opération consiste à solubiliser à chaud le polymère silicone dans le méthanol puis à ajouter de l'eau à pH acide. Le polymère ainsi purifié est chauffé à 115°C sous vide de 20 mmHg afin d'éliminer l'eau ou l'alcool résiduel. Le produit est enfin mis à l'étuve à 100°C sous pression atmosphérique. On obtient un polymère de pureté supérieure à 95% en poids.We start from a pure oil at 92% by mass with 8% by mass consisting of oligomers ungrafted from ungrafted allyloxybenzoic acid or acid isomers allyloxybenzoic. Among the different purification techniques several are possible. The method used here is fractional precipitation. It is dissolve the grafted oil obtained in 1.3 in a hot alcohol. This alcohol can be more particularly methanol. Then the polymer is precipitated by addition water of basic pH. The operation is repeated another time. The third operation consists in hot solubilizing the silicone polymer in methanol and then adding water at acidic pH. The polymer thus purified is heated to 115 ° C. under a vacuum of 20 mmHg to remove residual water or alcohol. The product is finally placed in the oven at 100 ° C. under atmospheric pressure. A polymer of purity greater than 95% is obtained in weight.

    Exemple 2 : préparation d'un précurseur - POS (C) d'un POS peroxyde selon l'invention, ce précurseur étant un polydiméthylsiloxane à extrémités triméthylsilyles et porteur de substituants fonctionnels de type -propylanhydride succiniqueExample 2: preparation of a precursor - POS (C) of a peroxide POS according to the invention, this precursor being a polydimethylsiloxane with ends trimethylsilyl and carrying functional substituents of the -propylanhydride type succinic

    Figure 00180001
    Figure 00180001

    Synthèse de l'huile de silicone C à motifs anhydride succinique : Synthesis of silicone oil C with succinic anhydride units :

    Dans un tricol de 500 ml muni d'une agitation mécanique, d'un réfrigérant, d'une ampoule de coulée, d'une sonde de température et sous balayage d'argon, on introduit 119,53 g d'allylanhydride succinique pur à plus de 99% molaire (0,85 mole) et 44,2 mg de platine de Karstedt à 10% en masse de platine. Le milieu réactionnel est porté à 90°C sous agitation puis on coule 175,53 g, d'huile de structure A (0,66 mole de fonction SiH) en 1h25. Le milieu réactionnel est laissé en contact à 90°C sous agitation pendant 4 heures. On traite ensuite le milieu réactionnel par 2% en poids de noir de carbone à 70°C pendant 4 heures. Après retour à température ambiante, on filtre sur carton sous pression d'azote le milieu réactionnel. Après avoir placé le milieu réactionnel dans un ballon monocol muni d'un barreau aimanté, on isole le polymère silicone greffé en dévolatilisant l'oligomère en excès par chauffage à 180°C sous vide de 2 mmHg. On obtient une huile silicone de structure C et de pureté égale à 94% en poids. In a 500 ml three-necked flask fitted with mechanical agitation, a condenser, a pouring funnel, temperature probe and under argon sweep, we introduce 119.53 g of pure succinic allylanhydride with more than 99 mol% (0.85 mol) and 44.2 mg of Karstedt platinum at 10% by mass of platinum. The reaction medium is brought to 90 ° C with stirring then 175.53 g of oil of structure A (0.66 mole of SiH function) in 1 hour 25 minutes. The reaction medium is left in contact at 90 ° C under stirring for 4 hours. The reaction medium is then treated with 2% by weight of carbon black at 70 ° C for 4 hours. After returning to room temperature, filters the reaction medium on cardboard under nitrogen pressure. After placing the middle reaction in a single-color flask fitted with a magnetic bar, the polymer is isolated silicone grafted by devolatilizing the excess oligomer by heating to 180 ° C. under vacuum 2 mmHg. A silicone oil of structure C and of purity equal to 94% is obtained in weight.

    Pour purifier ce produit jusqu'à plus de 99% en poids de pureté, on a dévolatilisé le produit à l'aide d'une pompe à diffusion sous vide de 10-3 mmHg en chauffant le polymère de 120 à 160°C pendant 6 heures. On obtient alors un polymère silicone greffé propylanhydride succinique de pureté supérieure à 99% en poids. L'analyse infrarouge montre que l'anhydride n'est pas ouvert lors des traitements décrits dans les exemples.To purify this product to more than 99% by weight of purity, the product was devolatilized using a vacuum diffusion pump of 10 -3 mmHg by heating the polymer from 120 to 160 ° C for 6 hours. This gives a grafted silicone propylanhydride succinic polymer of purity greater than 99% by weight. Infrared analysis shows that the anhydride is not opened during the treatments described in the examples.

    Exemple 3 : préparation d'un précurseur - POS (E) d'un POS peroxyde selon l'invention, ce précurseur étant un polydiméthylsiloxane à extrémités triméthylsilyles et porteur de substituants fonctionnels de type -propyl-succinimide- benzoïqueExample 3: preparation of a precursor - POS (E) of a peroxide POS according to the invention, this precursor being a polydimethylsiloxane with ends trimethylsilyl and carrying functional substituents of the -propyl-succinimide type benzoic

    Figure 00190001
    Figure 00190001

    3.1. Préparation de silicone à fonction amine par coéquilibration :3.1. Preparation of silicone with amine function by coequilibration :

    Dans un tricol muni d'un système de dévolatilisation, d'une agitation mécanique, d'une ampoule de coulée, d'une sonde de température et sous ciel d'argon, on introduit 50 g d'aminopropyldiméthoxyméthylsilane (0,3 mole) et on additionne en 1 heure une quantité de 27,6 g d'eau (1,5 mole). On porte à 110°C et on dévolatilise sous 11 mmHg afin de recueillir la quantité de méthanol de 19,2 g.
    Après retour à la température et en ayant remplacé le système de distillation par un réfrigérant, on introduit en plus de 35,1 g de silane hydrolysé précédemment obtenu, 30,5 g d'octaméthyltétrasiloxane (0,1 mole soit 10% en excès), 34,3 g d'une huile silicone courte avec 6 siliciums de formule M2D4 et 5,3 g de siliconate de potassium à 15% en poids de potasse (80 ppm). Après chauffage à 130°C pendant 6 heures sous stripping d'azote, on neutralise le mélange réactionnel par addition de 12,3 g d'une solution d'ester silicié d'acide phosphorique à 9 % massique d'acide phosphorique. Suite à la neutralisation, on laisse le milieu en contact pendant 30 minutes à 80°C puis on dévolatilise sous 2 mmHg à 170°C. On obtient 113,5 g d'huile silicone de structure D.
    50 g of aminopropyldimethoxymethylsilane (0.3 mole) are introduced into a three-necked flask provided with a devolatilization system, a mechanical stirrer, a dropping funnel, a temperature probe and under an argon sky and a quantity of 27.6 g of water (1.5 mole) is added over 1 hour. It is brought to 110 ° C. and devolatilized under 11 mmHg in order to collect the quantity of methanol of 19.2 g.
    After returning to temperature and having replaced the distillation system with a refrigerant, in addition to 35.1 g of hydrolyzed silane previously obtained, 30.5 g of octamethyltetrasiloxane (0.1 mol or 10% excess) are introduced. 34.3 g of a short silicone oil with 6 silicones of formula M 2 D 4 and 5.3 g of potassium siliconate at 15% by weight of potassium hydroxide (80 ppm). After heating at 130 ° C. for 6 hours under nitrogen stripping, the reaction mixture is neutralized by the addition of 12.3 g of a solution of silicon ester of phosphoric acid at 9% by mass of phosphoric acid. Following neutralization, the medium is left in contact for 30 minutes at 80 ° C. and then devolatilized under 2 mmHg at 170 ° C. 113.5 g of silicone oil of structure D are obtained.

    3.2. Formation d'un silicone E à fonctions acide et imide 3.2. Formation of a silicone E with acid and imide functions

    Dans un ballon tricol muni d'un réfrigérant, d'une agitation mécanique, d'une ampoule de coulée, d'une sonde thermomètre, d'un système Dien Stark et sous ciel d'argon, on charge 28,8 g d'anhydride triméllique (0,15 mole), et 75 g de toluène et on coule en 1 heure 50,0 g d'huile silicone à fonction amine de structure D (0,15 mole de fonction amine). Le mélange réactionnel est laissé en contact à température ambiante pendant 1 heure puis le mélange réactionnel est porté à reflux pendant 5 heures au cours du temps on suit l'élimination de l'eau. Après retour à la température ambiante, on filtre sur carton et sous pression le mélange réactionnel. Après avoir placé ce dernier dans un ballon monocol muni d'un barreau aimanté, on dévolatilise le solvant en chauffant à 110°C sous vide de 10 mmHg. On obtient un polymère de structure E pur à 95% en poids. In a three-necked flask fitted with a refrigerant, a mechanical stirrer, a light bulb, thermometer probe, Dien Stark system and under sky of argon, 28.8 g of trimellic anhydride (0.15 mol) are charged, and 75 g of toluene and 50.0 g of silicone oil with an amine function of structure D (0.15) are poured in over 1 hour mole of amine function). The reaction mixture is left in contact at temperature ambient for 1 hour then the reaction mixture is brought to reflux for 5 hours over time we follow the elimination of water. After return to temperature ambient, the reaction mixture is filtered on cardboard and under pressure. After having placed the latter in a single-colored balloon fitted with a magnetic bar, we devolatilize the solvent by heating to 110 ° C under vacuum of 10 mmHg. We obtain a polymer of structure E pure at 95% by weight.

    EXEMPLE 5 : OBTENTION D'UN POS PEROXYDE DANS LEQUEL LES FONCTIONS FPO (-O-O-) DES SUBSTITUANTS E SONT COMPRISES DANS DES RESTES PERACIDES CARBOXYLIQUES
    Figure 00210001
    A PARTIR DU PRECURSEUR POS SELON L'EXEMPLE 2 (RESTES ANHYDRIDES PENDANTS)
    EXAMPLE 5: OBTAINING A PEROXIDE POS IN WHICH THE FPO FUNCTIONS (-OO-) OF THE SUBSTITUTES E ARE INCLUDED IN PERACID CARBOXYL REMAINS
    Figure 00210001
    FROM THE PRECURSOR POS AS EXAMPLE 2 (REMAINING ANHYDRIDES REMAINING)
    5.1. Essai 5.1. Trial

    Dans un tube pèse-matière:

    • peser 250 mg d'huile silicone C de l'exemple 2 soit 0,615 mmole de fonctions anhydrides (4 fonctions par polymère)
    • ajouter 0,5 ml d'acétate d'éthyle (AcOEt),
    • peser 45 mg d'eau oxygénée à 70 % soit 0,926 mmole (excès 1,5 équivalent par rapport à la stochiométrie qui est de 1 H2O2 par anhydride).
    • introduire 1 goutte de KOH (1N)
    • ajouter un petit barreau magnétique
    • agiter à température ambiante pendant 1 heure.
    In a weighing tube:
    • weigh 250 mg of silicone oil C from Example 2, ie 0.615 mmol of anhydride functions (4 functions per polymer)
    • add 0.5 ml of ethyl acetate (AcOEt),
    • weigh 45 mg of hydrogen peroxide at 70% or 0.926 mmol (excess 1.5 equivalent relative to the stochiometry which is 1 H 2 O 2 per anhydride).
    • introduce 1 drop of KOH (1N)
    • add a small magnetic bar
    • stir at room temperature for 1 hour.

    5.2. Traitement 5.2. Treatment

    • ajouter 3 ml AcOETadd 3 ml AcOET
    • transférer dans une petite ampoule à décanter de 50 mltransfer to a small 50 ml separating funnel
    • ajouter 3 ml d'eau permutée à 100 g/l de sulfate d'ammoniumadd 3 ml of deionized water to 100 g / l of ammonium sulphate
    • agiter, laisser décanter, éliminer la phase aqueuse inférieurestir, allow to settle, remove the lower aqueous phase
    • recommencer l'opération encore 2 foisrepeat the operation 2 more times
    • récupérer la phase organique dans un bécher de 50 ml,recover the organic phase in a 50 ml beaker,
    • ajouter 1 g de MgSO4 anhydreadd 1 g of anhydrous MgSO 4
    • transférer dans un ballon taré de 50 ml, rincer 2 fois l'ampoule et MgSO4 par 1 ml d'ACOEttransfer to a tared 50 ml flask, rinse the ampoule 2 times and MgSO4 with 1 ml of ACOEt
    • tirer à sec au Rotavapor, bain à 35° maxidry draw with Rotavapor, bath at 35 ° maximum
    • tirer quelques minutes sous vide pompe, à froid (température ambiante)draw a few minutes under vacuum pump, cold (room temperature)
    • peser le produit obtenuweigh the product obtained
    5.3. Dosage peroxydes dans l'huile silicone peroxydée 5.3. Peroxide determination in peroxidized silicone oil

    Appareil : METROHM Dosimat 665

  • 5.3.1. Mode opératoire
    En erlen de 50 ml :
    • peser environ 250 mg d'huile peroxydée
    • ajouter :
      • 20 ml de mélange ACIDE ACETIQUE / H2O 80/20 et dissoudre
      • ou mieux 20 ml d'acide acétique pur, dissoudre, puis ajouter un peu d'eau
    • ajouter 1 spatule (1g) de NaHCO3 (inertage par CO2)
    • ajouter 1 spatule (1g) d'iodure de potassium
    • boucher et mettre à l'obscurité 20 minutes minimum.
    Transférer dans un bécher de 150 ml (forme haute) :
    • rincer avec 50 ml d'eau distillée
    • ajouter de l'acétone (maintient de la solubilité et antimousse)
    • ajouter un barreau magnétique et mettre en place, dosage de l'iode libérée par une solution de THIOSULFATE DE SODIUM 0,1 N
  • 5.3.2. Calculs
    Nbre mmoles H2O2 = Vml x CO3 x CO2 / COO x CO1
    % poids H2O2 = Nbre millimoles dosées x 34 / 1000
    1 équivalent H2O2 = 1 équivalent R-CO-O-OH
  • 5.3.3. Expression des résultats : % poids en équivalent H2O2
    Etant donné que le précurseur -POS (huile - C -) préparé dans l'exemple 2 comprend les substituants E porteurs chacun d'un anhydride, et que l'on suppose que la réaction est totale (rendement d'oxydation = 100 %), alors pour une mole d'huile (- C -), on fait réagir 4 moles d'H2O2, soit en % en poids : 1 mole huile (- C -) = 1628 g, pour 4 moles H2O2 = 136 g, soit 8,35 % poids d'H2O2.
  • 5.3.4. Résultat La teneur en peracide de l'huile C oxydée est de 6,2 %, soit une oxydation de 6,2 / 8,35 x 100 = 74 %.
  • Device: METROHM Dosimat 665
  • 5.3.1. Procedure
    In 50 ml Erlenmeyer flask:
    • weigh approximately 250 mg of peroxidized oil
    • add :
      • 20 ml of ACETIC ACID / H 2 O 80/20 mixture and dissolve
      • or better 20 ml of pure acetic acid, dissolve, then add a little water
    • add 1 spatula (1g) of NaHCO 3 (inerting with CO 2 )
    • add 1 spatula (1g) of potassium iodide
    • stopper and put in the dark for at least 20 minutes.
    Transfer to a 150 ml beaker (tall form):
    • rinse with 50 ml of distilled water
    • add acetone (maintains solubility and defoamer)
    • add a magnetic bar and put in place, assay of the iodine released by a solution of THIOSULFATE OF SODIUM 0.1 N
  • 5.3.2. calculations
    No. mmoles H 2 O 2 = Vml x CO3 x CO2 / COO x CO1
    % weight H 2 O 2 = No. of millimoles dosed x 34/1000
    1 equivalent H 2 O 2 = 1 equivalent R-CO-O-OH
  • 5.3.3. Expression of results:% weight in H 2 O 2 equivalent
    Since the precursor -POS (oil - C -) prepared in Example 2 comprises the substituents E each carrying an anhydride, and it is assumed that the reaction is complete (oxidation yield = 100%) , then for one mole of oil (- C -), 4 moles of H 2 O 2 are reacted, that is in% by weight: 1 mole oil (- C -) = 1628 g, for 4 moles H 2 O 2 = 136 g, or 8.35% by weight of H 2 O 2 .
  • 5.3.4. Result The peracid content of oxidized oil C is 6.2%, i.e. an oxidation of 6.2 / 8.35 x 100 = 74%.
  • EXEMPLE 6 OBTENTION D'UN POS PEROXYDE DANS LEQUEL LES FONCTIONS FPO (-O-O-) DES SUBSTITUANTS E SONT COMPRISES DANS DES RESTES PERACIDES CARBOXYLIQUES
    Figure 00220001
    A PARTIR DU PRECURSEUR POS SELON L'EXEMPLE 2 (RESTES ANHYDRIDES PENDANTS)
    EXAMPLE 6 OBTAINING A PEROXIDE POS IN WHICH THE FPO FUNCTIONS (-OO-) OF THE SUBSTITUTES ARE INCLUDED IN PERACID CARBOXYLIC RESIDUES
    Figure 00220001
    FROM THE PRECURSOR POS AS EXAMPLE 2 (REMAINING ANHYDRIDES REMAINING)

    En ballon de 100 ml, charger :

    • 15 g d'huile C de l'exemple 2 (36,9 mmoles anhydride)
    • 30 g d'acétate d'éthyle
    • 2,7 g d'eau oxygénée 0 70 % (55,6 mmoles (x 1,5))
    • 0,6 ml de KOH N (0,6 mmole)
    Mettre un barreau magnétique et agiter. L'exothermie est immédiate, la température atteint 31°C.
    Placer un cristallisoir d'eau froide pour ramener à température ambiante
    Maintenir 1 heure
    Transvaser en ampoule à décanter de 100 ml, rincer 2 fois le ballon par 10 ml d'AcOEt
    Procéder à 8 lavages par 20 ml d'eau permutée à 100 g/l de sulfate d'ammo : la disparition de l'eau oxygénée dans les phases aqueuses est suivie par papier indicateur des peroxydes.
    Sécher sur MgSO4 anhydre
    Filtrer sur verre fritté
    Transvaser dans un ballon de 100 ml, rincer l'ampoule et le fritté
    Tirer à sec au rotovapor, bain à 35° maxi.
    Sécher sous vide pompe pendant 3 heures à température ambiante.
    Poids obtenu : 15,4 g
    Teneur en peracides : 5,46 % (exprimé en H2O2)
    Oxydation : 65 %In 100 ml flask, load:
    • 15 g of oil C from Example 2 (36.9 mmol anhydride)
    • 30 g ethyl acetate
    • 2.7 g of hydrogen peroxide 0 70% (55.6 mmol (x 1.5))
    • 0.6 ml KOH N (0.6 mmol)
    Put on a magnetic bar and shake. The exotherm is immediate, the temperature reaches 31 ° C.
    Place a crystallizer of cold water to bring it to room temperature
    Maintain 1 hour
    Transfer to 100 ml separating funnel, rinse the flask twice with 10 ml of AcOEt
    Proceed to 8 washes with 20 ml of water permuted to 100 g / l of ammonium sulphate: the disappearance of hydrogen peroxide in the aqueous phases is followed by indicator paper for peroxides.
    Dry over anhydrous MgSO 4
    Filter on sintered glass
    Transfer to a 100 ml flask, rinse the vial and the frit
    Draw dry on rotovapor, bath at 35 ° max.
    Dry under vacuum pump for 3 hours at room temperature.
    Weight obtained: 15.4 g
    Peracid content: 5.46% (expressed as H 2 O 2 )
    Oxidation: 65%

    EXEMPLE 7 : ETUDE DE LA STABILITE AU STOCKAGE DE POS PEROXYDES SELON L'INVENTIONEXAMPLE 7 STUDY OF THE STABILITY OF STORAGE OF POS PEROXIDES ACCORDING TO THE INVENTION

    Le POS utilisé est préparé selon la méthodologie donné à l'exemple 6.
    Le produit est stocké seché à 5° C et 25° C.
    On prélève des échantillons au cours du temps et en dose les peroxydes comme décrit supra en 5.3.

  • 7.1. Stockage à 5° C de 0 à 30 jours
    Les résultats sont donnés par le tableau 1 ci-dessous. Durée (j) % Peracides % oxydation 0 5,72 100,0 2 5,48 95,8 6 5,08 88,8 13 3,82 66,8 22 2,90 50,7 30 1,70 30,0
  • 7.2. Stockage à 5 °C, 0, 11 et 22 jours
    Les résultats sont donnés par le tableau 2 ci-dessous Durée jours % peracides 5° C % oxydation 5°C 0 5,46 100,0 11 4,24 74,1 22 2,85 49,8
  • The POS used is prepared according to the methodology given in Example 6.
    The product is stored dried at 5 ° C and 25 ° C.
    Samples are taken over time and dose the peroxides as described above in 5.3.
  • 7.1. Storage at 5 ° C from 0 to 30 days
    The results are given in Table 1 below. Duration (d) % Peracids % oxidation 0 5.72 100.0 2 5.48 95.8 6 5.08 88.8 13 3.82 66.8 22 2.90 50.7 30 1.70 30.0
  • 7.2. Storage at 5 ° C, 0, 11 and 22 days
    The results are given in Table 2 below Duration days % peracids 5 ° C % oxidation 5 ° C 0 5.46 100.0 11 4.24 74.1 22 2.85 49.8
  • EXEMPLE 8 : OBTENTION D'UN POS PEROXYDE DANS LEQUEL LES FONCTIONS FPO (-O-O-) DES SUBSTITUANTS E SONT COMPRISES DANS DES RESTES PERACIDES CARBOXYLIQUES
    Figure 00240001
    A PARTIR DU PRECURSEUR POS SELON L'EXEMPLE 2 (RESTES ANHYDRIDES PENDANTS)
    EXAMPLE 8 OBTAINING A PEROXIDE POS IN WHICH THE FPO FUNCTIONS (-OO-) OF THE SUBSTITUTES ARE INCLUDED IN PERACID CARBOXYLIC RESIDUES
    Figure 00240001
    FROM THE PRECURSOR POS AS EXAMPLE 2 (REMAINING ANHYDRIDES REMAINING)

    On reproduit l'exemple 5 à la différence près que l'on n'utilise pas de KOH.Example 5 is reproduced with the difference that no KOH is used.

    Résultats :Results:

    • Teneur en équivalent H2O2 = 0,59 %H 2 O 2 equivalent content = 0.59%
    • oxydation : 7 %oxidation: 7%
    EXEMPLE 9 OBTENTION D'UN POS PEROXYDE DANS LEQUEL LES FONCTIONS FPO (-O-O-) DES SUBSTITUANTS E SONT COMPRISES DANS DES RESTES PERACIDES CARBOXYLIQUES
    Figure 00240002
    A PARTIR DU PRECURSEUR POS SELON L'EXEMPLE 2 (RESTES ANHYDRIDES PENDANTS)
    EXAMPLE 9 OBTAINING A PEROXIDE POS IN WHICH THE FPO FUNCTIONS (-OO-) OF THE SUBSTITUTES E ARE INCLUDED IN PERACID CARBOXYL REMAINS
    Figure 00240002
    FROM THE PRECURSOR POS AS EXAMPLE 2 (REMAINING ANHYDRIDES REMAINING)

    On reproduit l'exemple 6 à la différence près que l'on remplace la goutte de KOH par une goutte d'H3PO4 (85 % dans l'eau).Example 6 is reproduced with the difference that the drop of KOH is replaced by a drop of H 3 PO 4 (85% in water).

    Résultats : Results :

    • Teneur en équivalent H2O2 = 1,03 %H 2 O 2 equivalent content = 1.03%
    • oxydation : 12 %oxidation: 12%
    EXEMPLE 10 : OBTENTION D'UN POS PEROXYDE DANS LEQUEL LES FONCTIONS FPO (-O-O-) DES SUBSTITUANTS E SONT COMPRISES DANS DES RESTES PERACIDES CARBOXYLIQUES
    Figure 00250001
    A PARTIR DU PRECURSEUR POS SELON L'EXEMPLE 1 (RESTES BENZOÏQUES PENDANTS)
    EXAMPLE 10: OBTAINING A PEROXIDE POS IN WHICH THE FPO FUNCTIONS (-OO-) OF THE SUBSTITUTES E ARE INCLUDED IN PERACID CARBOXYLIC RESIDUES
    Figure 00250001
    FROM THE POS PRECURSOR AS IN EXAMPLE 1 (PENDANT BENZOIC REMAINS)

  • 10.1 Essai En tube pèse-matière :
    • peser 250 mg d'huile silicone B de l'exemple 1, soit 0,578 mmoles de fonctions acides (4 fonctions par polymère)
    • ajouter 0,5 ml d'acétate d'éthyle (AcOEt),
    • peser 84 mg d'eau oxygénée à 70 % soit 1,729 mmoles (excès 3 équivalents par rapport à la stochiométrie qui est de 1 H2O2 par acide).
    • 1 goutte H2SO4 (95 % dans l'eau)
    • ajouter un petit barreau magnétique
    • agiter à température ambiante pendant 2 heures, en présence d'un excès MgSO4 anhydre (> 100 mg).
    10.1 Test In weighing tube:
    • weigh 250 mg of silicone oil B from Example 1, i.e. 0.578 mmol of acid functions (4 functions per polymer)
    • add 0.5 ml of ethyl acetate (AcOEt),
    • weigh 84 mg of 70% hydrogen peroxide, ie 1.729 mmol (excess 3 equivalents compared to the stochiometry which is 1 H 2 O 2 per acid).
    • 1 drop H 2 SO 4 (95% in water)
    • add a small magnetic bar
    • stir at room temperature for 2 hours, in the presence of an excess anhydrous MgSO4 (> 100 mg).
  • 10.2. Traitement
    • ajouter 3 ml AcOET
    • transférer dans une petite ampoule à décanter de 50 ml
    • ajouter 3 ml d'eau permutée à 100 g/l de sulfate d'ammonium
    • agiter, laisser décanter, éliminer la phase aqueuse inférieure
    • recommencer l'opération encore 2 fois
    • récupérer la phase organique dans un bêcher de 50 ml,
    • ajouter 1 g de MgSO4 anhydre
    • transférer dans un ballon taré de 50 ml, rincer 2 fois l'ampoule et MgSO4 par 1 ml d'ACOEt
    • tirer à sec au Rotavapor, bain à 35° maxi
    • tirer quelques minutes sous vide pompe, à froid (température ambiante)
    • peser le produit obtenu
    10.2. Treatment
    • add 3 ml AcOET
    • transfer to a small 50 ml separating funnel
    • add 3 ml of deionized water to 100 g / l of ammonium sulphate
    • stir, allow to settle, remove the lower aqueous phase
    • repeat the operation 2 more times
    • recover the organic phase in a 50 ml beaker,
    • add 1 g of anhydrous MgSO 4
    • transfer to a tared 50 ml flask, rinse the ampoule 2 times and MgSO4 with 1 ml of ACOEt
    • dry draw with Rotavapor, bath at 35 ° maximum
    • draw a few minutes under vacuum pump, cold (room temperature)
    • weigh the product obtained
  • 10.3 Résultat
    • Teneur en peracide : 0,66 %
    • oxydation : 9 %
    10.3 Result
    • Peracid content: 0.66%
    • oxidation: 9%
  • EXEMPLE 11 : EVALUATION DU POUVOIR BLANCHISSANT DU POS PEROXYDE DE L'EXEMPLE 6EXAMPLE 11: EVALUATION OF THE WHITENING POWER OF THE POS PEROXIDE OF EXAMPLE 6 11. 1 Méthode en développement de détermination du pouvoir blanchissant sur de la poudre d'hydroxyapatite HAP 11. 1 Method under development for determining the whitening power on hydroxyapatite PAH powder

  • 11. 1. 1. Principe
    • Mesure du pouvoir blanchissant de composés oxydants, sur une poudre d'hydroxyapatite HAP, préalablement encrassée par une solution chaude de thé.
    • Pouvoir blanchissant quantifié par mesures colorimétriques effectuées sur l'appareil Minolta CR-241.
    11. 1. 1. Principle
    • Measurement of the whitening power of oxidizing compounds, on a hydroxyapatite PAH powder, previously fouled with a hot tea solution.
    • Whitening power quantified by colorimetric measurements performed on the Minolta CR-241 device.
  • 11.1.2.Appareillage
  • A - Petits ustensiles
    • Papier filtre, « filtration rapide » n°41 de Whatman pour la filtration de la solution de thé et pour la récupération de la poudre encrassée
    • Papier filtre.GF/C diamètre de 47 mm de Whatman utilisé pour la récupération de la poudre blanchie
    • Büchner (diamètre de 100 ou 160 mm), fiole à vide de 2 L, pompe à vide ou trompe à eau avec manomètre différentiel, joints en caoutchouc
    • Pots en polystyrène cristal (transparent), capacité de - 40 ml
  • B - Appareils
    • Colorimètre Minolta CR-241
    • Agitateur va-et-vient Promax 2020
    • Etuve (50 à 100 ° C)
  • C - Produits
    • Eau désionisée
    • Thé Lipton Yellow, qualité n°1
    • Poudre d'hydroxyapatite HAP BIO-RAD
    • Solution ou oxydante
  • 11.1.2.Appareillage
  • A - Small utensils
    • Filter paper, “rapid filtration” n ° 41 from Whatman for the filtration of the tea solution and for the recovery of dirty powder
    • Filter paper.GF/C diameter 47 mm from Whatman used for the recovery of bleached powder
    • Büchner (diameter 100 or 160 mm), 2 L vacuum flask, vacuum pump or water pump with differential pressure gauge, rubber seals
    • Crystal polystyrene jars (transparent), capacity of - 40 ml
  • B - Devices
    • Minolta CR-241 colorimeter
    • Promax 2020 back and forth shaker
    • Oven (50 to 100 ° C)
  • C - Products
    • Deionized water
    • Lipton Yellow tea, quality n ° 1
    • BIO-RAD HAP hydroxyapatite powder
    • Solution or oxidant
  • 11.1.3. Mode opératoire
  • A - Encrassement de la poudre HAP
  • a - Mesure de la blancheur initiale de la poudre
    Une mesure de la blancheur initiale de la poudre HAP est effectuée. Elle s'effectue sur l'appareil Minolta CR-241. Trois mesures sont faites pour obtenir une valeur moyenne de Lo, ao, bo.
  • b -Décoction du thé, filtration
    Dans un bêcher de 1 000 ml, 500 ml d'eau désionisée et 10 sachets de thé découpés sont introduits (C= ∼ 40g/l) et portés à ∼ 80°C sous agitation mécanique (200 tr/min) pendant 90 minutes.
    L'agitation et la puissance de chauffe sont arrêtés. Une fois le milieu refroidi à ∼ 40°C (durée nécessaire = ∼ 90 min), il est filtré sous vide.
    Le filtrat (= solution encrassante de thé) est récupéré. Son volume est réajusté à 500 ml avec de l'eau désionisée.
  • c - L'encrassement
    7,5 g de poudre HAP sont introduits dans la solution de thé.
    L'ensemble est à nouveau porté à ∼ 80°C, sous agitation pendant 45 minutes.
    Le chauffage et l'agitation sont arrêtés, le milieu refroidit à l'air ambiant (jusqu'à ~ 40°C) avant d'être filtré sous vide.
    La poudre est lavée avec trois fois 20 ml d'eau désionisée chaude jusqu'à ce que le filtrat soit incolore.
    Le filtre et la poudre sont placés à l'étuve [T= 50-100°C] jusqu'à évaporation complète de l'eau.
    La poudre récupérée sous forme d'agglomérats est broyée à l'aide d'un mortier et d'un pilon.
    Sa nouvelle blancheur est mesurée (Ls, as, bs) au Minolta CR-241.
  • B - Blanchiment de la poudre HA P encrassée
    6.5 g de solution oxydante (contenant l'équivalent de 0.3 % en H2O2) et 50 mg de poudre HAP encrassée sont transvasés dans un flacon en polystyrène cristal de contenance - 40 ml.
    Le tout est placé sur l'agitateur va-et-vient PROMAX 2020 pendant le temps souhaité (15 min, 30 min, 1h, 2h, ...) à raison de 250 allers-retours.
    Le milieu est ensuite dilué par addition de 20 ml d'éthanol avant d'être filtré.
    La poudre est lavée avec trois fois 30 ml d'éthanol.
    L'ensemble filtre + poudre blanchie est séché à l'air libre sous hotte.
    La nouvelle blancheur de la poudre blanchie peut être mesurée (Lc), et le pouvoir blanchissant de la solution oxydante peut être calculé.
  • 11.1.3. Procedure
  • A - Contamination of the PAH powder
  • a - Measurement of the initial whiteness of the powder
    A measurement of the initial whiteness of the PAH powder is carried out. It is performed on the Minolta CR-241 device. Three measurements are made to obtain an average value of Lo, ao, bo.
  • b - Tea decoction, filtration
    In a 1000 ml beaker, 500 ml of deionized water and 10 cut tea bags are introduced (C = ∼ 40g / l) and brought to ∼ 80 ° C with mechanical stirring (200 rpm) for 90 minutes.
    Stirring and heating power are stopped. Once the medium has cooled down to ∼ 40 ° C (required time = ∼ 90 min), it is filtered under vacuum.
    The filtrate (= fouling tea solution) is collected. Its volume is readjusted to 500 ml with deionized water.
  • c - Fouling
    7.5 g of PAH powder are introduced into the tea solution.
    The whole is again brought to ∼ 80 ° C., with stirring for 45 minutes.
    Heating and stirring are stopped, the medium cools with ambient air (up to ~ 40 ° C) before being filtered under vacuum.
    The powder is washed with three times 20 ml of hot deionized water until the filtrate is colorless.
    The filter and the powder are placed in an oven [T = 50-100 ° C] until the water has completely evaporated.
    The powder recovered in the form of agglomerates is ground using a mortar and pestle.
    Its new whiteness is measured (Ls, as, bs) with the Minolta CR-241.
  • B - Bleaching of dirty HA P powder
    6.5 g of oxidizing solution (containing the equivalent of 0.3% of H 2 O 2 ) and 50 mg of contaminated PAH powder are transferred to a crystal polystyrene bottle of capacity - 40 ml.
    The whole is placed on the PROMAX 2020 back-and-forth agitator for the desired time (15 min, 30 min, 1 hour, 2 hours, etc.) at the rate of 250 round trips.
    The medium is then diluted by adding 20 ml of ethanol before being filtered.
    The powder is washed with three times 30 ml of ethanol.
    The whole filter + bleached powder is dried in the open air in a hood.
    The new whiteness of the bleached powder can be measured (Lc), and the whitening power of the oxidizing solution can be calculated.
  • 11.1.4 Calculs
    Le calcul du pouvoir blanchissant du composé oxydant s'effectue à partir de la valeur L donnée par le colorimètre, et obtenue après les différents traitements de la poudre HAP.
    L* représente la clarté de l'échantillon, ses valeurs s'étendent entre 0 et 100.
    On définit ainsi les différentes valeurs :
    • Lo, clarté initiale avant encrassement.
    • Ls, clarté après encrassement.
    • Lc, clarté après blanchiment.
    Le pouvoir blanchissant est calculé comme suit :
  • ¤ Pouvoir blanchissant : Pb = Lc - Ls Lo - Ls x 100
  • 11.1.4 Calculations
    The bleaching power of the oxidizing compound is calculated from the value L given by the colorimeter, and obtained after the various treatments of the PAH powder.
    L * represents the clarity of the sample, its values range between 0 and 100.
    We thus define the different values:
    • Lo, initial clarity before fouling.
    • Ls, clarity after fouling.
    • Lc, clarity after bleaching.
    The whitening power is calculated as follows:
  • ¤ Whitening power: Pb = Lc - Ls Lo - Ls x 100
  • 11.2 Mesure de la blancheur Lc obtenue dans le test décrit en 11.1 supra, avec le POS peroxydé de l'exemple 6 11.2 Measurement of the whiteness Lc obtained in the test described in 11.1 above, with the peroxidized POS of Example 6

  • 11.2.1. Le blanchiment de la poudre HAP selon le point 11.1.3 B supra est effectué comme suit :
    6,5 g de préparation oxydante contenant 300 mg de POS peroxydé selon l'exemple 6 dispersés dans 6,2 g d'eau inversée par agitation manuelle.
    et 50 mg de poudre HAP encrassée sont transvasés dans un flacon en polystyrène cristal de contenance 40 mg.
    On procède ensuite comme indiqué au point 11.1.3. B.
    11.2.1. The bleaching of the PAH powder according to point 11.1.3 B above is carried out as follows:
    6.5 g of oxidizing preparation containing 300 mg of peroxidized POS according to Example 6 dispersed in 6.2 g of inverted water by manual stirring.
    and 50 mg of dirty PAH powder are transferred to a 40 mg crystal polystyrene bottle.
    Then proceed as indicated in point 11.1.3. B.
  • 11.2.2 Résultats Temps (min) Lc avec témoin eau Pb Lc avec POS peroxydé Pb 0 50 0 50 0 15 49 0 69 45 60 49 0 69 45 120 49 0 70 48 11.2.2 Results Time (min) LC with water indicator Pb Lc with peroxidized POS Pb 0 50 0 50 0 15 49 0 69 45 60 49 0 69 45 120 49 0 70 48
  • Claims (12)

    1. Polyorganosiloxanes (POSs) comprising siloxane units of following formula (I): RaEbGcSiO 4 - (a+b+c)2
      in which
      a + b + c = 0 to 3
      a, b, c = 0 to 3
      R corresponds to one or more identical or different radicals, R being chosen from monovalent hydrocarbonaceous groups, preferably from linear, branched and/or cyclic alkyls and/or aryls, and more preferably still from linear or branched C1-C4 alkyls and phenyl, xylyl and tolyl groups;
      E corresponds to one or more monovalent functional substituents, which are identical to or different from one another, chosen from (cyclo)aliphatic and/or aromatic hydrocarbonaceous groups and/or heterocyclic groups and carrying one or more acyl peroxide functional groups Fpo of formula
      Figure 00410001
      with X corresponding to H, a halogen, preferably chlorine, or to a cation which makes it possible to form a salt with the acyl peroxide anion and which is preferably chosen from the elements from columns Ia and IIa of the Periodic Table, and each optionally comprising one or more Fpo-stabilizing functional groups Fstab which are identical to or different from one another and are chosen from functional groups capable of bonding via weak bonds with the Fpo functional groups;
      G corresponds to one or more functional substituents, identical to or different from one another, each comprising one or more Fpo-stabilizing functional groups Fstab which are identical to or different from one another and are chosen from functional groups capable of bonding via weak bonds with the Fpo functional groups;
      with the conditions according to which:
      (i). the concentration of [Fpo] functional groups, expressed by the ratio Fpo number Total number of silicon atoms in the POS is defined as follows:
      Δ 0 < [Fpo]
      Δ preferably   0.01 ≤ [Fpo] ≤ 1.0
      Δ and more preferably still   0.1 ≤ [Fpo] ≤ 0.6,
      (ii). the concentration as mol% of T siloxane units (a + b + c = 1) and/or Q siloxane units (a + b + c = 0) is defined as follows:
      Δ 0 ≤ [T and/or Q] ≤ 20
      Δ preferably   0 ≤ [T and/or Q] ≤ 10
      Δ and more preferably still   0 ≤ [T and/or Q] ≤ 8.
    2. Polyorganosiloxanes according to claim 1, characterized in that, in the G substituent or substituents of the formula (I), the Fstabs correspond to functional groups which can generate weak bonds (hydrogen bonds) with Fpo and which are selected from the group consisting of:
      functional units comprising nitrogen and/or oxygen and/or fluorine and/or sulphur and/or phosphorus; carboxylic, carboxylate, amide, imide, sulphonamide, hydroxyl, alkoxy, amine or organofluorinated units being preferred;
      cationic units, preferably those comprising one or more quaternary ammoniums;
      chelating units comprising one or more ether functional groups and/or one or more amine functional groups, and/or phosphonate and/or sulphonate chelating units.
    3. Polyorganosiloxanes according to either one of claims 1 and 2, characterized in that they correspond to the formula (II) given below:
      Figure 00420001
      in which:
      R1 and R3 independently represent a hydrogen, a hydroxyl or a monovalent residue corresponding to the same definition as that given for R above;
      R2 independently represents hydrogen, a hydroxyl or a monovalent residue corresponding to the same definition as that given for R above;
         2 ≤ m + n + o ≤ 300
      preferably   3 ≤ m + n + o ≤ 50
      and more preferably still   5 ≤ m + n + o ≤ 20
         0 ≤ m ≤ 200
      preferably   1 ≤ m ≤ 100
      and more preferably still   1 ≤ m ≤ 10
         0 ≤ n ≤ 50
      preferably   1 ≤ n ≤ 10
      and more preferably still   2 ≤ n ≤ 4
         0 ≤ o ≤ 50
      preferably   1 ≤ o ≤ 10
      and more preferably still   2 ≤ o ≤ 4.
    4. Polyorganosiloxanes according to claim 4,
      characterized in that:
      Δ R1 and R3 = C1-C3 alkyl, preferably -CH3
      Δ R2 = C1-C3 alkyl, preferably -CH3
      Δ the functional substituent or substituents E simultaneously comprise Fpo and Fstab functional groups.
    5. Polyorganosiloxanes according to any one of the preceding claims, characterized in that E comprises, an Fpo percarboxylic acid functional group and an Fstab carboxylic acid functional group.
    6. Process for the preparation of the POSs according to any one of claims 1 to 5, characterized in that it consists essentially in oxidizing polysiloxane precursors of the said POSs using at least one oxidizing agent preferably chosen from the group consisting of:
      H2O2, O2, O3 and their mixtures,
         these polysiloxane precursors being distinguished from the polyorganosiloxanes (POSs) in that they comprise one or more F' po functional groups which are Fpo precursors and are composed:
      of carboxyl residues:
      Figure 00430001
      with X' corresponding to the same definition as that given for X in claim 1; and/or of acid anhydride residues:
      Figure 00440001
    7. Process according to claim 6, characterized in that the polyorganosiloxane precursors selected:
      carry F'po anhydride functional groups, the oxidation being carried out using H2O2 in the presence of a catalyst of strong base type, preferably potassium hydroxide,
      and/or carry F'po carboxylic functional groups, preferably benzoyl groups, the oxidation being carried out using H2O2 in the presence of a catalyst of strong acid type.
    8. Process according to claim 7, characterized in that the polyorganosiloxane precursors carry F'po succinic anhydride functional groups connected to the silicon atoms via a -(CH2)3- linking unit.
    9. Process according to any one of claims 6 to 8, characterized in that use is made of POS precursors with a molar purity ≥ 90%, preferably ≥ 95%.
    10. Use of the polyorganosiloxanes (POSs) forming the subject-matter of any one of claims 1 to 8 or obtained according to the process forming the subject-matter of any one of claims 9 to 12 in a dental composition, as agent for bleaching the teeth.
    11. Dental composition, in particular a dentifrice, characterized in that it comprises at least one polyorganosiloxane (POS) forming the subject-matter of any one of claims 1 to 5 or obtained according to the process forming the subject-matter of any one of claims 6 to 9 as bleaching agent.
    12. Dental composition according to claim 11, characterized in that it comprises:
      from 0.1 to 40% by weight of at least one polyorganosiloxane (POS)
      from 5 to 40% by weight of at least one polishing agent
      and from 0.005 to 2% by weight of at least one fluorinated compound.
    EP99973300A 1998-12-09 1999-12-01 Peroxidised polyorganosiloxanes (pos), one of the methods for preparing them and their use as bleaching agent in dental compositions Expired - Lifetime EP1149123B1 (en)

    Applications Claiming Priority (3)

    Application Number Priority Date Filing Date Title
    FR9815715 1998-12-09
    FR9815715A FR2787114B1 (en) 1998-12-09 1998-12-09 POLYORGANOSILOXANES (POS) PEROXIDES, ONE OF THEIR PREPARATION METHODS AND THEIR USES IN PARTICULAR AS A WHITENING AGENT IN DENTAL COMPOSITIONS
    PCT/FR1999/002984 WO2000034360A1 (en) 1998-12-09 1999-12-01 Peroxidised polyorganosiloxanes (pos), one of the methods for preparing them and their uses as bleaching agent in dental compositions

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    FR2787114B1 (en) * 1998-12-09 2001-02-16 Rhodia Chimie Sa POLYORGANOSILOXANES (POS) PEROXIDES, ONE OF THEIR PREPARATION METHODS AND THEIR USES IN PARTICULAR AS A WHITENING AGENT IN DENTAL COMPOSITIONS
    DE19860364C2 (en) * 1998-12-24 2001-12-13 3M Espe Ag Polymerizable dental materials based on siloxane compounds capable of curing, their use and manufacture
    EP3502257B1 (en) * 2016-08-22 2023-02-15 Suzhou SJ Biomaterials, Ltd. Co. Solid-phase carrier capable of improving detection sensitivity, and detection component

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    US2963501A (en) * 1959-04-06 1960-12-06 Dow Corning Organosilyl peroxides
    US3726943A (en) * 1971-08-12 1973-04-10 Union Carbide Corp Ethylenically unsaturated monomer polymerization with silyl acyl peroxides and acyl peroxy polysiloxanes
    JPH0617479B2 (en) * 1986-08-28 1994-03-09 日本油脂株式会社 Method for producing dimethylsiloxane block copolymer
    FR2787114B1 (en) * 1998-12-09 2001-02-16 Rhodia Chimie Sa POLYORGANOSILOXANES (POS) PEROXIDES, ONE OF THEIR PREPARATION METHODS AND THEIR USES IN PARTICULAR AS A WHITENING AGENT IN DENTAL COMPOSITIONS

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    EP1149123A1 (en) 2001-10-31
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    FR2787114B1 (en) 2001-02-16
    ES2223196T3 (en) 2005-02-16

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