WO2002087748A1 - Dispersions d'hydroxyapatite comprenant un agent stabilisant a fonction phosphoryle, sulfinyle ou carboxyle, et leur procede de preparation - Google Patents
Dispersions d'hydroxyapatite comprenant un agent stabilisant a fonction phosphoryle, sulfinyle ou carboxyle, et leur procede de preparation Download PDFInfo
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- WO2002087748A1 WO2002087748A1 PCT/FR2002/001442 FR0201442W WO02087748A1 WO 2002087748 A1 WO2002087748 A1 WO 2002087748A1 FR 0201442 W FR0201442 W FR 0201442W WO 02087748 A1 WO02087748 A1 WO 02087748A1
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B25/00—Phosphorus; Compounds thereof
- C01B25/16—Oxyacids of phosphorus; Salts thereof
- C01B25/26—Phosphates
- C01B25/32—Phosphates of magnesium, calcium, strontium, or barium
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K6/00—Preparations for dentistry
- A61K6/80—Preparations for artificial teeth, for filling teeth or for capping teeth
- A61K6/831—Preparations for artificial teeth, for filling teeth or for capping teeth comprising non-metallic elements or compounds thereof, e.g. carbon
- A61K6/838—Phosphorus compounds, e.g. apatite
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/0004—Preparation of sols
- B01J13/0008—Sols of inorganic materials in water
Definitions
- Hydroxyapatite dispersions comprising a stabilizing agent with phosphoryl, sulfinyl or carboxyl function, and process for their preparation
- the present invention relates to stable aqueous colloidal dispersions of colloids with apatite structure in which the colloids, of oblong shape, have nanometric dimensions.
- colloids in more or less aggregated form, form oblong objects of an average length (or greater dimension) (in number) between 20 and 200 nm and an equivalent aspect ratio between 5 and 500 .
- colloidal aqueous dispersion is generally meant a system consisting of a continuous aqueous phase in which are dispersed fine solid particles of colloidal dimension, said fine particles defining colloids on the surface of which molecules of an agent can be bonded or adsorbed. stabilizer or various ionic species present in the continuous aqueous phase.
- colloids with apatitic structure is meant according to the invention colloids of general formula:
- J is chosen from OH “ , CO 3 2" , F ' and / or CI " and in which certain phosphate ions (PO4 3" ) or hydrogen phosphate (HPO4 2 " ) can be replaced by carbonate ions (CO 3 2" ) ; and in which certain Ca 2+ cations can be replaced by metallic cations M n + of alkali, alkaline earth metals or of lanthanide where n represents 1, 2 or 3, it being understood that the molar ratio of the cation M n + to Ca 2+ , when M n + is present, varies between 0.01: 0.99 and 0.25: 0.75, and the substitution of HPO 4 2 ' ions or PO4 3 " ions with CO 3 2' ions , the incorporation of CO 3 2 " ions as J and the substitution of Ca 2+ cations by metal cations is carried out so as to satisfy the electronic balance, in particular with the creation of vacancies. Particularly preferably, when Ca 2+ is replaced by an al
- the latter is preferably Eu 3+ , Eu 2+ , Dy 3+ or Tb 3+ .
- lanthanide is understood to mean the elements of the group constituted by Tyrtrium and by the elements of the periodic classification with atomic number included inclusively between 57 and 71.
- the colloids are colloids of hydroxyapatite.
- colloids with an apatite structure also includes the colloids obtained by hydrolysis of the colloids of formula I above.
- Colloids with an apatite structure are generally obtained by contacting, in aqueous solution, a source of Ca 2+ and a source of PO 4 3 " in an appropriate pH range.
- colloids with an apatite structure are obtained, the growth of which is difficult to control and limit.
- the invention provides, according to a first of its aspects, a method for controlling the growth of colloids with apatitic structure and leading to stable colloidal dispersions consisting of colloids of nanometric dimensions.
- the invention relates to stable, aqueous colloidal dispersions of colloids with apatitic structure, formed of relatively fine colloids, of oblong shape, of an average length (in number) between 20 and 200 nm and an equivalent aspect ratio (ratio of the average length (in number) to the equivalent diameter) of between 5 and 500.
- the invention relates to a stable aqueous colloidal dispersion of colloids with apatitic structure, having a pH between 3.5 and 9.5, of oblong shape with an average length (in number) between 20 and 200 nm and an equivalent aspect ratio (ratio of the average length (in number) to the equivalent diameter) of between 5 and 500; and comprising as stabilizing agent a compound of formula I, a compound of formula II or a compound of formula III, as defined below, optionally in ionized form or a mixture of these compounds, said colloids having an apatite structure having for formula:
- J is chosen from OH “ , F “ , CO 3 2 “ or CI " ; and in which certain phosphate ions (PO 4 3 “ ) or hydrogen phosphate (HPO4 2” ) can be replaced by carbonate ions (CO 3 2 " ); and in which certain Ca 2+ can be replaced by metal cations M n + of alkali, alkaline earth or lanthanide metals where n represents 1, 2 or 3, it being understood that the molar ratio of the cation M n + to Ca 2+ , when M n + is present, varies between 0.01: 0.99 and 0 , 25: 0.75, and that the substitution of HPO 4 2- ions "or ions PO 4 3" by CO 3 2- ions, incorporation of the CO3 2- ions "as J and substituting Ca + cations by metal cations is carried out in such a way as to satisfy the electronic balance; • the stabilizing agents of formula I being compounds of formula: in which :
- - n is an integer between 0 and 15 advantageously between 1 and 12, preferably between 2 and 6;
- - Gi represents a (C 2 -C 3 ) alkylene radical, preferably an ethylene radical
- - X represents -O-; a relationship ; the divalent group -OP (O) (OH) -X'- in which X 'is an oxygen atom or a bond; or the divalent group -O-R ⁇ o-P (O) -X "- in which Rio represents - (G 2 -O) rr where G 2 is as defined for Gi above and n 'is as defined for n above, preferably n 'is between 2 and 6, and X "represents an oxygen atom or a single bond;
- - R represents a (CrC 20 ) alkyl radical, preferably (CrCi 8 ) alkyl, or a (C 6 -C 3 o) aryl radical, said radical being optionally substituted; it being understood that when m represents 2, the two groups X- (GrO) n -R are not necessarily identical and if in one of these groups Gi represents -O-R ⁇ o-P (O) -X "- or - OP (O) (OH) -X'-, the other group X- (G ⁇ -O) n -R does not contain a group -OR 10 -P (O) -X "- nor a group -OP (O ) (OH) -X'-; • the stabilizing agents of formula (II) being compounds of formula:
- - A represents a sulfonyl or sulfinyl group
- - n ' is an integer between 0 and 15, advantageously between 1 and 12, preferably between 2 and 6;
- - K represents an (C 2 -C 3 ) alkylene radical, preferably an ethylene radical, • the stabilizing agents of formula (III) having the formula:
- colloids of oblong shape are understood to mean colloids of parallelepipedal shape (for example in the shape of a stick) or of acicular shape.
- the equivalent diameter is the diameter that would have the colloid of corresponding acicular shape with the same average volume (in number) and the same average length (in number).
- the equivalent diameter assigned to the cross section of the acicular colloid corresponds to the diameter of an average cross section.
- the oblong-shaped colloids are formed from colloids with a weakly aggregated apatitic structure.
- the oblong colloids have an average length (in number) between 20 and 200 nm and an equivalent diameter between 0.01 and 50 nm, preferably between 0.01 and 20 nm.
- J represents OH “ , or / and F " . Not all OH ions “need to be replaced by F “ ions, but only part of the OH ions " can be replaced by F “ ions. Likewise, when J is chosen from OH “ , F “ , CO 3 2 “ and CI " , it is not necessary for all the Js to be identical to each other.
- Stabilization of the colloidal dispersion is obtained by the action of a stabilizing agent.
- the stabilizing agent contributes not only to ensure the stabilization of the dispersion but also to control the growth of the colloids with apatitic structure during the preparation of the aqueous dispersion.
- the ionized forms of the compounds of formula I, of formula II or of formula III can be obtained by the action of a base, preferably an inorganic base.
- an inorganic base mention may be made of bases of the alkali metal or alkaline earth metal hydroxide and ammonium hydroxide type.
- alkylene is meant an aliphatic hydrocarbon chain, linear or branched at C1-C18, preferably at C1-C12.
- alkyl is meant an aliphatic group, linear or branched, in C- 1 -C1 8 , better still in C- ⁇ -C ⁇ 2 .
- alkyl radicals are methyl, ethyl, propyl, isopropyl, butyl, isobutyl, t-butyl, pentyl, isopentyl, neopentyl, 2-methylbutyl, 1-ethyl propyl, hexyl, isohexyl, neohexyl, 1-methylpentyl, 3 - methylpentyle, 1, 1-dimethylbutyl, 1, 3-dimethylbutyl, 2-ethylbutyl, 1-methyl-1- ethylpropyl, heptyle, 1-methylhexyl, 1-propylbutyl, 4,4-dimethylpentyl, octyl, 1-methylheptyle, 2 -ethylhexyl, 5,5-dimethylhexyl, nonyl, decyl, 1-methylnonyl, 3,7-dimethyloctyl and 7,
- alkyl represents methyl, ethyl, propyl, isopropyl, butyl, t-butyl, pentyl, isopentyl, neopentyl, 2-methylbutyl, 1- ethylpropyl, hexyl, isohexyl, neohexyl, 1-methylpentyl, 3-methylpentyl, 1, 1 -dimethylbutyl, 1, 3-dimethylbutyl, 2-ethylbutyl and 1-methyl-1-ethylpropyl.
- the alkyl radical comprises from 1 to 4 carbon atoms.
- Examples of (C 6 -C 3 o) aryl groups are in particular phenyl, naphthyl, anthryl and phenanthryl.
- R represents (CC 20 ) substituted alkyl or (CrC ⁇ 8 ) substituted alkyl, it is preferably substituted by (C 6 -C 3 o) aryl.
- R represents (C 6 - C 30 ) substituted aryl, it is preferably substituted by (CC 2 o) alkyl or (d- C ⁇ s) alkyl.
- n respectively n ', represents 3 or 5 and Gi, respectively K, represents ethylene.
- a particularly preferred subgroup of stabilizing agents consists of the compounds of formula (V):
- n represents an integer from 2 to 12.
- a preferred meaning of aryl is phenyl and when T 1 represents arylalkyl, T1 is preferably phenylalkyl or alternatively, when T 1 represents alkylaryl, T1 preferably represents alkylphenyl.
- T 1 represents hexyl, octyl, decyl, dodecyl, oleyl or nonylphenyl.
- a second preferred subgroup of stabilizing agents consists of the compounds of formula (VI):
- n 2 and n 3 are identical and between 2 and 12.
- T 2 and T 3 are identical.
- a preferred meaning of aryl is phenyl; a preferred meaning of arylalkyl is phenylalkyl; a preferred meaning of alkylaryl is alkylphenyl.
- T 2 and T 3 are chosen from hexyl, octyl, decyl, dodecyl, oleyl and nonylphenyl.
- a third preferred sub-group of stabilizing agents consists of a mixture in all proportions of compounds of formula V and compounds of formula VI.
- this type of amphiphilic compound mention may be made of those sold under the brands Lubrophos® and Rhodafac® by Rhodia, and in particular the products below:
- Rhodafac® RS 710 in which the polyoxyethylene part consists of 10 oxyethylene units, or RS 410 in which the polyoxyethylene part consists of 3 oxyethylene units;
- poly-oxy-ethylene oleocetyl ester phosphate for example Rhodafac® PA 35 in which the polyoxyethylene part consists of 5 oxyethylene units;
- poly-oxy-ethylene nonylphenyl phosphate ester for example Rhodafac® PA 17 in which the polyoxyethylene part consists of 6 oxyethylene units;
- non-branched poly (oxy-ethylene) phosphate ester for example Rhodafac® RE 610 in which the polyoxyethylene part consists of 6 oxyethylene units.
- the stabilizing agent is generally either present in free form in the continuous medium of the colloidal dispersion, or adsorbed or bound to the surface of the colloids, or in ionic interaction with the Ca 2+ ions present in the continuous phase of the dispersion.
- the stabilizing agent When the stabilizing agent is in free form in the dispersion, it is in acid form or in ionized form.
- the stabilizing agent When the stabilizing agent is in interaction with the Ca 2+ ion present in the continuous phase, it can form aggregates of lamellar phase.
- the stabilizing agent When the stabilizing agent is interacting on the surface of the colloids, it is in strong, electrostatic and / or complexing interaction with the mineral ions present on the surface of the colloids. This strong bond can be demonstrated by showing the presence of the stabilizing agent on the colloids recovered by ultracentrifugation of the colloidal dispersions and dried at room temperature for a period greater than 7 days. By H NMR on these colloids, lines are observed corresponding to chemical shifts attributable to the stabilizing agent.
- the colloidal phase (consisting of colloids) is predominantly of apatitic structure as defined above.
- the apatite structure represents more than 50% by weight of the colloidal phase, preferably more than 75% by weight, better still more than 80%, for example more than 85% by weight.
- the colloidal phase can also comprise other structures, such as Ca (H 2 P0 4 ) 2 ; CaHPO; CaHPO, 2H 2 O or other amorphous phase based on calcium and PO 4 3 " , HPO 4 2" , H 2 PO 4 " or OH " .
- the molar ratio of total calcium present in the colloidal phase to total phosphorus present in the colloidal phase varies between 0.8 and 1.7, better still between 1.4 and 1.7 .
- the molar ratio of the stabilizing agent to calcium in the colloidal phase varies between 0.02 and 2, preferably between 0.02 and 1.0, more preferably between 0.05 and 0.8.
- the colloidal phase contains from 80 to 100% of the total calcium, preferably from 90 to 100%, better still from 95 to 100%.
- the calcium concentration of the dispersion is easily adjustable, according to the invention, by elimination of part of the continuous aqueous phase.
- the elimination of part of the aqueous phase can be carried out by ultrafiltration.
- the colloidal dispersion of the invention has a concentration greater than 0.25 M in calcium in the form of colloids with apatitic structure, preferably greater than 0.5 M, advantageously greater than 1M, this concentration possibly reaching 5M .
- the colloidal phase contains from 60 to 100% of total phosphorus (PO4 3 ' ions, HPO 4 2 " and H 2 PO 4 " total), preferably from 80 to 100%, preferably from 90 to 100%, better still from 95 to 100% by weight.
- the pH of the colloidal dispersion of the invention varies between 6 and 9.5, better still between 6.5 and 9.
- the invention relates to a process for preparing a stable aqueous colloidal dispersion, comprising the steps consisting in: a) bringing into contact, in aqueous solution, a source of Ca 2+ cations, and a source of PO 4 3 " anions and a stabilizing agent chosen from a compound of formula I, a compound of formula II and a compound of formula III, the formulas I, II and III being as defined above or representing a salt of one of these compounds with an acid or a base and one of their mixtures, at a pH of between 3.5 and 9.5, the respective amounts of the source of Ca 2+ and of the source of PO 3 anions " being such that the Ca 2+ / P molar ratio varies between 0.1 and 3, preferably between 0.2 and 2, the amount of stabilizing agent being such that the stabilizing agent / Ca
- source of Ca 2+ cations is meant a compound capable of releasing Ca 2+ ions in aqueous solution.
- source of PO 4 3 anions is meant a compound capable of releasing PO 4 3" ions in aqueous solution.
- Examples of a source of Ca 2+ cations are calcium hydroxide, calcium oxides, water-soluble calcium salts.
- Examples of calcium salts are the salts having for anion PF 6 “ , PCI 6 “ , BF 4 ' , BCI4 “ , SbF 6 “ , BPh 4 “ , CIO 4 “ , CF 3 SO3 " and more generally the carboxylates derived from C 2 -C 4 alkylcarboxylic acids and especially acetate
- Other salts are calcium halides, calcium hydrogen carbonate and calcium nitrate.
- those which can be used in the context of the invention are those with sufficient water solubility to ensure the desired concentration of Ca 2+ in the aqueous phase.
- the source of Ca 2+ cations is chosen from calcium hydroxide, calcium chloride, calcium fluoride, calcium nitrate, and calcium hydrogen carbonate.
- the source of PO 3 " anions is the salt of a PO 4 3" anion, the salt of an HPO4 2 " anion or the salt of an H2PO4 " anion such as a salt of ammonium, or an alkali metal salt.
- PO4 3 is the salts of oligomeric phosphate-type anions such as the salts of polyphosphates (or catena-polyphosphate) of general formula:
- n varies from 2 to 10 (and in particular the salts of the tripolyphosphate type) or else the salts of the trimetaphosphate anion (PO 3 ) 3 3" , or the salts of the pyrophosphate anion (P 2 ⁇ ) 4 ' .
- the next step consists in mixing the two aqueous solutions, this mixture being used in a conventional manner with stirring.
- the pH of the two dispersions is adjusted beforehand before mixing.
- the bases and acids which can be used are those generally used in the art.
- bases which can be used mention may be made of NH 4 OH, KOH, NaOH, NaHCO 3 , Na 2 CO 3 , KHCO3 and K 2 CO 3 .
- NH 4 OH or NaOH will be used.
- acids which can be used are in particular HCI, H 2 SO, H 3 PO or HNO 3 .
- HNO 3 will be used .
- a buffer operating in the desired range can be used.
- a buffer ensuring a pH of 6.5 to 9 is used.
- a buffer consisting of an aqueous solution of potassium dihydrogen phosphate (0.025M) and sodium hydrogen phosphate (0.025M), which ensures a pH of 6.86 at 25 ° C.
- the contacting of the sources with an aqueous medium can be carried out in any way.
- the relative proportions of the compounds used respectively as a source of Ca 2+ and of PO 4 3 " are calculated so that the Ca / P molar ratio is between 0.1 and 3, preferably between 0.2 and 2.
- the Ca / P molar ratio takes into account all of the Ca 2+ cations introduced and all of the phosphorus introduced into the solution, whether the phosphorus is in the form H3PO4, H 2 PO 4 3 " , HPO 4 2" or PO 4 3 " .
- the stabilizing agent is added either to the aqueous solution of Ca 2+ , or to the aqueous solution of PO 4 3 " , or to the two aqueous solutions, in which case the respective proportion of stabilizing agent added to each solution is arbitrary.
- the amount of stabilizing agent to be added to the total is defined so that the stabilizing agent / Ca molar ratio varies between 0.05 and 0.5, preferably between 0.08 and 0.4.
- the amount of stabilizing agent used affects the dimensions of the colloids ultimately obtained.
- the concentration of Ca 2+ cations in the solution is between 0.1 M and 1M, preferably between 0.1 M and 0.5M; and the concentration of ions PO 4 3 " , HPO4 2" and H 2 PO 4 " total varies between 0.05M and 2M, preferably between 0.15M and 1M.
- the contacting of the source of Ca 2+ with the source of PO 4 3 " generally takes place at ambient temperature, for example between 15 and 30 ° C.
- Suitable sources are the hydroxides of these metals or salts of these metals, such as halides or nitrates.
- the metal cation is the cation of a lanthanide
- a salt of said lanthanide such as a chloride or a nitrate.
- Step b) of the process of the invention is a maturing step during which the mixture of the two solutions is left to stand or stirred, the time necessary to observe the formation of colloids.
- This ripening stage can be carried out at ambient temperature (15-30 ° C) or at a higher temperature, namely up to 150 ° C. Thus, generally, the temperature is fixed at this stage between 15 and 150 ° C, better still between 40 and 100 ° C.
- the ripening stage is preferably carried out in a closed enclosure.
- the dispersion, conditioned in a closed enclosure, can be placed directly in an oven previously brought to the set temperature or undergo a temperature ramp up to the set temperature, the rate of temperature rise preferably varying between 0.1 ° C. / min and 10 ° C / min.
- the ripening is carried out at various temperatures.
- a first phase of ripening is carried out at a first temperature between 20 and 95 ° C.
- a second phase of ripening is carried out at a second temperature, said second temperature also being between 20 and 95 ° C.
- said second temperature is lower than said first temperature.
- the ripening time varies depending on the operating conditions and more particularly on the temperature. Usually the time to ripening varies between 10 min and 24 hours, for example between 30 min and 18 hours.
- the continuous phase of the colloidal dispersion can contain different species such as NH + , Na ⁇ K + , CI “ , NO 3 " and SO 4 2 " .
- These ions come either from sources of calcium and PO 4 3" , or from acids and mineral bases used for pH adjustments.
- the continuous phase of the colloidal dispersion can also contain stabilizers in neutral form or in ionized form, not in interaction with the surface of the colloids, that is to say completely free, or else in interaction with Ca 2 ions + present in the continuous phase.
- This washing can be carried out in a conventional manner per se, by ultrafiltration or dialysis.
- Ultrafiltration can be carried out in particular in air or in an atmosphere of air and nitrogen or even under nitrogen. It preferably takes place with water whose pH is adjusted to the pH of the dispersion.
- the pH can also be post-adjusted after washing and concentration by ultrafiltration. This final pH can advantageously be between 6 and 8.5.
- the size of the colloids can be determined by photometric counting from an analysis by METHR (High Resolution Transmission Electron Microscopy).
- the structure of the colloids and in particular their more or less significant degree of aggregation can be determined by cryo-transmission electron microscopy by following the Dubochet method.
- the average length (in number) of the oblong colloids varies between 20 and 200 nm and their equivalent aspect ratio (ratio of the average length (in number) to the equivalent diameter) varies between 5 and 500.
- One of the advantages of the invention is the low aggregation of the colloidal particles between them.
- colloidal dispersions of the invention can be used in multiple applications, as such, or after isolation and stacking and cohesion of the colloids with apatitic structure to form, for example, porous materials.
- colloidal dispersions of the invention can also be used after preparation of an emulsion by addition of an oily phase.
- colloids and porous materials are the separation and purification of proteins, use in prostheses and use in sustained release systems.
- the hydroxyapatite colloids obtained can be used in the treatment of osteoporosis, cramps, colitis, bone fractures, insomnia, as well as in dental hygiene.
- Hydroxyapatite colloids can also be used in the preparation of hydroxyapatite films, absorbent materials with high specific surface and high pore volume, encapsulation materials and catalytic materials, but also in the field of luminescence.
- the colloids of the aqueous dispersions of the invention can be isolated simply by ultracentrifugation. These colloids can present, bound or adsorbed, on their surface, a certain amount of stabilizing agent. The amount of stabilizing agent present can be determined by chemical determination. The molar ratio of the stabilizing agent to the calcium of the colloid generally varies between 0.02 and 2, preferably between 0.05 and 0.8.
- the determination of the mass percentage of Ca of the colloids is carried out from the colloids isolated by centrifugation and dried at room temperature for 7 days, in the following manner.
- the dried colloids are dissolved by microwave attack with HN ⁇ 3 / HF / H 2 O 2 .
- the determination of Ca is then carried out by atomic emission spectroscopy by induced plasma (ICP / AES Inductive Coupled Plasma) on a Jobin Yvon Ultima device.
- the principle is an excitation of atoms in a plasma argon, with emission of photons of different wavelengths.
- a grating spectrometer allows the separation of wavelengths and the detection is carried out by a photo multiplier.
- the mass percentage of carbon present in the colloids recovered by ultracentrifugation and dried at room temperature for 7 days is determined in a conventional manner by elementary microanalysis using a LECO CS-044 device. Oxidation is carried out in the presence of the product catalyst in an induction furnace under oxygen scavenging.
- the detection and integration of CO 2 peaks is carried out by infrared.
- the invention relates to colloids of apatitic structure redispersible in water which can be obtained by implementing the steps consisting in: a - preparing an aqueous colloidal dispersion by implementing the method of the invention as described above; b - isolate the colloids from the aqueous colloidal dispersion obtained in the previous step.
- the isolation of the colloids from the colloidal dispersion can be carried out in a manner known per se, and for example by simple evaporation at room temperature of the continuous phase or by ultracentrifugation.
- the colloids isolated after ultracentrifugation or evaporation of the continuous phase are in the form of a paste or possibly powdered solid.
- the continuous phase can be evaporated using conventional techniques known to those skilled in the art, for example at room temperature or at temperatures above 100 ° C.
- the colloids thus obtained are redispersible in water.
- the resulting dispersion has a concentration greater than 0.25M of calcium in the form of colloids with apatitic structure, preferably greater than 0.5M, advantageously greater than 1M.
- the molar ratio of calcium to phosphorus also varies in the colloids between 0.8 and 1.7.
- M denotes the molecular mass
- the phosphate solution is added to the calcium solution with stirring at room temperature. It is readjusted to pH 7 with a 1 M aqueous NH 4 OH solution.
- the mixture has a Ca / P molar ratio of 0.5 and a PA 35 / Ca molar ratio of 0.25.
- the mixture is stirred for one hour, transferred to an airtight bottle, then undergoes heat treatment by keeping in an oven previously warmed up to 50 ° C.
- the heat treatment lasts 16 hours.
- a colloidal dispersion is obtained.
- the colloidal dispersion is washed by ultrafiltration by passage over a 3 KD membrane. Washing is carried out with a volume of demineralized water equal to 4 times the volume of dispersion.
- the phosphate solution is added to the calcium solution with stirring at room temperature. A decrease in pH is observed. It is readjusted to pH 8.5 with a 1 M aqueous NH 4 OH solution.
- the mixture is stirred for one hour, transferred to an airtight bottle, then undergoes heat treatment by keeping in an oven previously brought to temperature at 95 ° C.
- the heat treatment lasts 16 hours.
- a colloidal dispersion is obtained.
- the colloidal dispersion is washed by ultra-filtration by passage over a 3 KD membrane. Washing is carried out with a volume of demineralized water equal to 4 times the volume of dispersion.
- the objects are rod-shaped with an average length of around 50 nm and an equivalent diameter of around 10 nm.
- the phosphate solution is added to the calcium solution with stirring at room temperature. A decrease in pH is observed. It is readjusted to pH 8.5 with a 1 M aqueous NH 4 OH solution.
- the mixture is stirred for one hour, transferred to an airtight bottle, then undergoes heat treatment by keeping in an oven previously warmed up to 50 ° C.
- the heat treatment lasts 16 hours.
- a colloidal dispersion is obtained.
- the colloidal dispersion is washed by ultrafiltration by passage over a 3 KD membrane. Washing is carried out with a volume of demineralized water equal to 4 times the volume of dispersion.
- the phosphate solution is added to the calcium solution with stirring at room temperature. A decrease in pH is observed. It is readjusted to pH 8.0 with a 1 M aqueous solution of NH4OH.
- the mixture is stirred for one hour, transferred to an airtight bottle, then undergoes heat treatment by keeping in an oven previously warmed up to 50 ° C.
- the heat treatment lasts 16 hours.
- a colloidal dispersion is obtained.
- the colloidal dispersion is washed by ultrafiltration by passage over a 3 KD membrane. Washing is carried out with a volume of demineralized water equal to 4 times the volume of dispersion.
- the average length of the rods is approximately 60 nm and the equivalent diameter is approximately 5 nm.
- the dispersion On an aliquot of the dispersion, it is dried at room temperature for several days. The dried product is then taken up in a volume of water to a volume corresponding to the volume of the initial dispersion before drying. The product is redispersible and a colloidal dispersion is again obtained.
- the phosphate solution is added to the calcium solution with stirring at room temperature. A decrease in pH is observed. It is readjusted to pH 8.5 with a 1 M aqueous NH 4 OH solution.
- the mixture is stirred for one hour, transferred to an airtight bottle, then undergoes heat treatment by keeping in an oven previously brought to temperature at 95 ° C.
- the heat treatment lasts 16 hours.
- a colloidal dispersion is obtained.
- the colloidal dispersion is washed by ultrafiltration by passage over a 3 KD membrane. Washing is carried out with a volume of demineralized water equal to 4 times the volume of dispersion. After ultracentrifugation at 50,000 M min for 4 hours, a pellet is collected which is dried at room temperature.
- the 60 cm 3 of the phosphate solution B thus prepared are added to an aliquot of 90 cm 3 of the calcium solution A with stirring at room temperature. A decrease in pH is observed. It is readjusted to pH 8.5 with a 1 M aqueous NH 4 OH solution.
- a solution A is prepared by adding 0.44 g of CaCl 2 , 2H 2 O (ie 3 millimoles) in 30 cm 3 of water. 0.780 g of Rhodafac PA 35 (ie 1 millimole) is added. The pH is equal to 2. It is adjusted to pH 7 with a 1 M aqueous solution of NH 4 OH.
- a solution B is prepared with 20 cm 3 of a 0.25M aqueous solution of (NH 4 ) 2 HPO 4 (i.e. 5 millimoles) pre-adjusted to pH 7.
- cryo-MET acicular colloids with an average length of 150 nm and a diameter of 5 nm are perfectly individualized.
- the colloidal dispersion is prepared by the two-step process of the invention in which, during the first step, bringing the source of Ca 2+ and the source of PO into contact 4 3 " is produced by mixing an aqueous solution of a source of PO 4 3" having a pH between 6.5 and 9, with an aqueous solution of a source of Ca 2+ containing the stabilizing agent and having a pH between 6.5 and 9
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EP02726282A EP1381456A1 (fr) | 2001-04-27 | 2002-04-25 | Dispersions d'hydroxyapatite comprenant un agent stabilisant a fonction phosphoryle, sulfinyle ou carboxyle, et leur procede de preparation |
US10/475,294 US20040116543A1 (en) | 2001-04-27 | 2002-04-25 | Hydroxypatite dispersions comprising a stabilising agent with a phosphoryl, sulphinyl or carboxyl functional , and method for preparing same |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR01/05746 | 2001-04-27 | ||
FR0105746A FR2823991B1 (fr) | 2001-04-27 | 2001-04-27 | Dispersions d'hydroxyapatite comprenant un agent stabilisant a fonction phosphoryle, sulfinyle ou carboxyle, et leur procede de preparation |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2002087748A1 true WO2002087748A1 (fr) | 2002-11-07 |
Family
ID=8862804
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/FR2002/001442 WO2002087748A1 (fr) | 2001-04-27 | 2002-04-25 | Dispersions d'hydroxyapatite comprenant un agent stabilisant a fonction phosphoryle, sulfinyle ou carboxyle, et leur procede de preparation |
Country Status (4)
Country | Link |
---|---|
US (1) | US20040116543A1 (fr) |
EP (1) | EP1381456A1 (fr) |
FR (1) | FR2823991B1 (fr) |
WO (1) | WO2002087748A1 (fr) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2855768B1 (fr) * | 2003-05-21 | 2006-06-16 | Rhodia Chimie Sa | Compositions a base d'isocyanate, leur procede d'utilisation pour realiser des vetements et revetements ainsi obtenus |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2605229A (en) * | 1949-04-23 | 1952-07-29 | Joseph K Marcus | Calcium phosphate gels |
US3027229A (en) * | 1957-12-02 | 1962-03-27 | Diamond Lab | Method of preparing hydrated calcium phosphate gels |
EP0322250A1 (fr) * | 1987-12-23 | 1989-06-28 | Sumitomo Chemical Company, Limited | Solution de revêtement contenant de l'hydroxyapatite et procédé pour effectuer un revêtement d'hydroxyapatite utilisant ladite solution |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1248634A (en) * | 1969-03-21 | 1971-10-06 | British Petroleum Co | Polymerisation process |
-
2001
- 2001-04-27 FR FR0105746A patent/FR2823991B1/fr not_active Expired - Fee Related
-
2002
- 2002-04-25 EP EP02726282A patent/EP1381456A1/fr not_active Withdrawn
- 2002-04-25 US US10/475,294 patent/US20040116543A1/en not_active Abandoned
- 2002-04-25 WO PCT/FR2002/001442 patent/WO2002087748A1/fr not_active Application Discontinuation
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2605229A (en) * | 1949-04-23 | 1952-07-29 | Joseph K Marcus | Calcium phosphate gels |
US3027229A (en) * | 1957-12-02 | 1962-03-27 | Diamond Lab | Method of preparing hydrated calcium phosphate gels |
EP0322250A1 (fr) * | 1987-12-23 | 1989-06-28 | Sumitomo Chemical Company, Limited | Solution de revêtement contenant de l'hydroxyapatite et procédé pour effectuer un revêtement d'hydroxyapatite utilisant ladite solution |
Also Published As
Publication number | Publication date |
---|---|
EP1381456A1 (fr) | 2004-01-21 |
FR2823991A1 (fr) | 2002-10-31 |
US20040116543A1 (en) | 2004-06-17 |
FR2823991B1 (fr) | 2003-06-20 |
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