• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A process is disclosed for performing encapsulation, en masse, by an in situ polymerization reaction to yield capsule wall material. The polymerization comprises a reaction between melamine and formaldehyde and/or polycondensation of monomeric methylol melamine or etherified methylol melamine, or a low molecular weight polymer thereof, in an aqueous vehicle and the reaction is conducted in the presence of negatively-charged, carboxyl-substituted, linear aliphatic hydrocarbon polyelectrolyte material dissolved in the vehicle. Liquid-liquid phase separation is accomplished and maintained by increase in the molecular weight of the resulting condensation polymer without further dilution of the manufacturing vehicle. The negatively-charged polyelectrolyte material is required and has an apparent effect of controlling or modifying the polymerization reaction. The disclosed encapsulation process permits manufacture of micro-capsules in concentrations of capsule to capsule manufacturing vehicle higher than previously possible.
    公开号:SU965341A3
    申请号:SU772559001
    申请日:1977-12-29
    公开日:1982-10-07
    发明作者:Лазло Фоуриз Питер；Вильям Браун Роберт；Спаргар Филлипс Пол (Младший)
    申请人:Эпплтон Пейперз,Инк. (Фирма)；
    IPC主号:
    专利说明:

    5) METHOD OF OBTAINING MICROCAPSULES
    1 .--. The invention relates to the production of microcapsules for use in copy paper.
    A known method of producing micro 6 capsules by dispersing a water-insoluble core material in an aqueous dispersion of the material forming the shell, which is the product of polymerization of urea and formaldehyde
    dG1
    The disadvantage of this method is the relatively low yield and concentration of the microcapsules obtained.
    The closest to the proposed 15 technical essence and the achieved result is the method of semi-, microcapsule cells by dispersing an insoluble core material in water in an aqueous dispersion of a shell-forming material, followed by separating the obtained C 2J microcapsules.
    However, the microcapsules obtained by this method release their contents when the casing is dried. 25
    This is not intended to preserve the contents of the core.
    The purpose of the invention is to obtain microcapsules with an impermeable during storage.
    The goal is achieved by the fact that in the method of producing microcapsules by dispersing the water-insoluble core material in an aqueous dispersion of the material forming the shell, followed by separating the resulting microcapsules, using a shell as the material forming its shell, selected from the group that includes the mixture melamine and formaldehyde, monomeric methylomelamine or its low molecular weight polymer, monomeric methylated methylolmelamine or its low grade, acrylic polymer or their mixtures and the process is carried out pH t, 3- (and a temperature of 20-100 ° C in the presence of a negatively charged, polymeric polyelectrolyte selected from the group consisting of a copolymer of ethylene and maleic anhydride with a molecular weight of 71,000 and maleic anhydride with a molecular weight of 250000, polyacrylic acid with a molecular mass of 5000 copolymer of propylene and maleic anhydride, copolymer of butadiene and maleic anhydride, copolymer of vinyl acetate and maleic anhydride, taken in quantity O, based on the weight of the aqueous dispersion. Once the formation of the system has been completed and the condensation reaction has begun, leading to the formation of walls, there is no need for a dissolution step. The presence of a system modifier makes it possible to form a high concentration polymer with relatively low viscosity, the resulting system with high concentration and low viscosity allows the separation of the liquid phase and the subsequent polymerization to a solid state in order to produce microcapsules in the whole volume, relatively short time , necessary to complete the process of microcapsule formation, the possibility of carrying out the reaction in a wide temperature range, almost full use similar materials in polymer formation - a product condensation, serving as the wall material. To obtain the walls of the microcapsules, methylolmelamines are used, containing from one to six methylol groups, where one or all methylol groups can be esterified. Compounds with a lower degree of methylation or esterification are preferred since they are more soluble in water and more reactive. The concentration of the shell material in the aqueous phase should preferably be in the range of 5 to 20%. Negatively charged polymer polyelectrolyte plays the role of a modifier of the reaction of polycondensation of raw materials. It is preferable to introduce it into the system before the start of the polycondensation reaction,. The amount of modifier in the system should be sufficient to provide the necessary rate of condensation reaction, as a result of which a polymer is formed. Of course, if the concentration of the modifier is very high, then the viscosity of the entire system will be unacceptably high. As a rule, the system must contain at least 0, and no more than S% modifier. In some cases, combinations of fractions of the same modifier with different molecular masses, as well as combinations of modifiers of different chemical nature can be successfully used. - In the microcapsule system, the materials present in the aquatic medium may vary widely within Wide Limits. Such systems can be successfully used in which the content of the aqueous phase is less than 60 or even less than +5 by volume of the volume of the entire system. Moreover, depending on the type of modifier system used (s, systems with a viscosity of less than 300 cP were obtained containing such a low volume of the aqueous phase. The material contained in the microcapsule, i.e. the material of the capsule core, is almost independent of the proposed method and it can be any kind of material: solid, liquid or gaseous, practically insoluble In water and not interacting with the material of the Capsule of the capsules or other components of the encapsulating system. As materials of the core of the capsule, Water-insoluble or poorly soluble in water, liquids such as olive oil, fish oil, vegetable oils, spermacetious oil, mineral oil, xylene, toluene, kerosene, chlorinated diphenyl and methyl saline, practically water-insoluble solid materials such as naphthalenes and oil can be used. cocoa; water-insoluble metal oxides and salts; fibrous materials such as cellulose or asbestos; water-insoluble synthetic polymeric materials; minerals, pigments; glass; fragrant and aromatic substances; reactants; biocidal compositions; physiologically active compositions and fertilizer compositions. After the process of obtaining the microcapsules is completed, they are separated from the reaction medium by filtration, followed by washing with water. The drying of the capsules takes place in a dryer with forced air supply. However, drying or separating the capsules from the medium before using them is optional. If desired, the encapsulated may be supplied as a suspension in solution emulsified with 520.7 g of the standard material of the core of capsules, as in Example t. 318, 5 g of the emulsion obtained above are placed in a water thermostat at 55 and with stirring, 32, k g of a 350 ml molecular weight melamine amine solution is added to it, then asz is stirred in a water bath overnight. After 2 hours the thermostat is disconnected. The densitometer reading on the SF sheet after 3 hours is 78. Example 7. A solution of 50 g of a 10% aqueous solution of a copolymer of methyl vinyl ether and maleic anhydride with a molecular weight of 350 and emulsified therein is 150 cm of standard, core material capsules. The emulsion was thermostatic in a water bath with stirring. Good quality microcapsules are formed after 90 minutes, as evidenced by a densitometer reading for an imprint on the SF sheet, which was 71. Example 8. The pH of the mixture is 100 g of a 10% solution of a copolymer of ethylene and maleic anhydride with a molecular weight of 75,000-90000 and 200 g of water is made up to A, O with sodium hydroxide. 200 ml of the core material is emulsified in this solution, as in example t. This emulsion is thermostatted in a water bath with stirring, adding to it 6.6 g of methylated methylol melamine with a molecular weight of 2bO. After 2 hours, the thermoregulation of the water bath is stopped, but the mixture is kept stirring overnight in a water-cooled bath. During the microencapsulation, the pH of the mixture rises to about. to 8 The course of the microencapsulation reaction is assessed by applying the samples of the mixture at various times after the introduction of the esterified methylol melamine onto the acid SF coating and by measuring the color intensity using a densitometer. Below are typical results of measuring the intensity of prints obtained in the presence of microencapsulated materials in accordance with the proposed method. For (Comparison, the results obtained in the presence of a urea-formaldehyde hydrolyzing capsules forming the known method are given., 10 Table 2 shows the densitometer readings on the imprints on the CB sheet. Table2 In the case when the densitometer reading is about 60 or above, this indicates that the oil per droplet is in the shell, and the process of microencapsulation is successfully completed. From the data presented above it can be seen that the proposed method, carried out with, ensures the formation of a protective shell of the material The capsule core is significantly more p-rich than the urea-formaldehyde system. This process can be modified in such a way that the protective coating is obtained at the same time, but at a lower temperature. The densitometer readings for the SF prints are 33 and 80, respectively. 1 and 2 hours after the components have been introduced. If desired, the proposed method can be carried out without any heating at all. In this case, a longer time is required to obtain a protective cover. Densitometer readings for SF-from seals at 9 CO, 5 hours, "7 (1 hour; 36 (1.5 hours), 67: 08 hours). As shown by the results of aging experiments with (in the heat chamber /, the proposed method makes it possible to obtain good capsules at room temperature, a dose for a reasonable period of time, whereas the microvalent-formaldehyde microcapsule system does not give equivalent capsules of good quality in the same conditions. (see Table 3). Example 9. Solution pH: 100 g of a 10% aqueous solution of a copolymer of methyl vinyl ether and maleic anhydride with a molecular weight of 250000, 100 g of water and B 5 g of a 60% solution of methylated methylol melamine with pH molecules A mass of 250 is adjusted to a value of approximately 4.8 with a saturated aqueous solution of sodium hydroxide. 180 g of standard capsule material is emulated in this solution. The emulsion is thermostated by stirring in a water bath, resulting in approximately 30 minutes satisfactory capsules. Example: pH of a solution of 40 g of a 25% aqueous solution of polyacrylic acid with a molecular weight of 150,000 and 1 gO of water is adjusted to about 0 with a 20% aqueous solution. sodium hydroxide. 50. g of an 80% solution of an esterified methylol melamine with a molecular weight of 350 is added to it. Then, 180 g of a standard capsule core material is emulsified in this solution. The emulsion is placed in a water bath, heated to a temperature of which is raised to 55 ° C for 15 minutes. Satisfactory capsules are formed after heating and stirring for 45 minutes. Example 11. The pH of a solution of 50 g of a 10-n solution of a copolymer of propylene and maleic anhydride, used as modifiers, 100 g of water is adjusted to 4.0 with a 20% aqueous solution of sodium hydroxide. This solution is emulsified with 100 cm of the standard material of the capsules, as in Example 1. Then, 25 g of an 80% solution of methylated methylol melamine with a molecular weight of 350 is added to the emulsion. The emulsion is heated in a 55 ° C water bath while stirring . Capsules of satisfactory quality are formed after 25 minutes, as evidenced by the reading of the densitometer 70 obtained for the imprint on the SF-sheet. Example 12.PH of a solution of 38 g of a TZ-th solution of a copolymer of butadiene and maleic anhydride and 77 g of water was adjusted to 4.0 with sodium hydroxide. To this solution, 25 g of 80% methylated methylomelamine with a molecular weight of 350 and 1bO cm of standard capsule core material are emulsified in the resulting solution. The emulsion is placed in a bath heated to. Capsules of satisfactory quality are formed in for kO min, as evidenced by the reading of the densitometer Jk obtained for the imprint on the SF sheet. Example 13. A 10% aqueous solution of copolymer of vinyl acetate and maleic anhydride (PVAMA) is prepared by dissolving the polymer in water by the action of injected vapor and partially neutralizing with approximately 0.5 cm of a 20% aqueous solution of sodium hydroxide per gram of polymer. whereby a solution is obtained, the pH of which is about 4.0. Then, a solution of 50 g of the PVAMA solution specified is prepared with 100 g of water and 25 g of methylated methylol melamine with a molecular weight of 350, in a slurry, emulsified with 100 cm MEO g) of a standard capsule core material. The emulsion was thermostatic at 5 ° C in a water bath. After 2 h, the sample of the coating on the SF sheet had a reflection coefficient of 74%. Example 14, a solution of 29 g of methylolmelamine, 9.5 g of a 37% aqueous formaldehyde solution and 5.5 g of water while stirring; ay at room temperature for 45 min-1 h until the solution becomes homogeneous, the pH of the resulting solution approximately 6.0. 20 g of a 25% aqueous solution of polyacrylic acid with a molecular weight of 150,000 and 130 g of water are mixed, the pH is adjusted to 4.5. To this solution is added a pre-prepared solution of methylol melamine and c. the resulting mixture is emulsified with 100 cm by 90 g of a standard capsule core material in a liquid carrier — a reaction medium or other, for example, for use in paper impregnation compositions, in dyeing or insecticidal compositions. . The individual capsules obtained according to the inventive method have a practically spherical shape and a diameter of from 1 micron to less than 100 microns, the preferred size of the capsules being 1-50 microns in diameter. By adjusting the intensity of mixing, you can get drops of liquid core material of capsules of any size. Depending on the amount of core material, the number of finished capsules may vary. Example 1. A solution is prepared of a mixture of 100 g of a 10% aqueous solution of a copolymer of ethylene and maleic anhydride containing approximately equimolar amounts of ethylene and maleic anhydride and having a molecular weight of about 75,000 to 90,000, and 200 g of water. Using a 20% aqueous solution of sodium iroxide, the pH of this solution is adjusted to 5. In this solution, 200 ml of a capsule core material consisting of a solution of 1.7 wt. D 3 3-bis-dimethylaminophenyl-6-dimethylamino-phthalmide, 0.55 wt.% 2-anilino-3-methyl-6 pyethylaminofluoride and 0, 55 wt. 3, 3-bis 1-methyl-2-methyl-3-yl-ft-l in a solvent mixture consisting of benzylated ethylbenzene and hydrocarbon oil, which is a fraction with a temperature of 204-2 bOs. With stirring, the emulsion is placed in a water bath at a temperature and a solution prepared by heating a mixture of 26.5 g of a 37% aqueous solution of formaldehyde and 20 g of melamine is added to it. After 2 h, the thermostat is turned off and the encapsulated mass is stirred in a bath with cooling water overnight. Since the size of the resulting capsules is very small, and the capsules themselves are intended to be used in carbon free. The reflection coefficient of hr prints;
    T &
    Refraction ratio
    A similar quality test of microcapsules consists in determining the degree of loss of the ability of the paper coated with microcapsules to imprint in a typewriter after storage 9
    X 100
    权利要求:
    Claims (3)
    [1]
    her in the chamber at a certain temperature for a certain period of time. A standard for assessing the quality of typewriter prints is carried out on a pair of sheets of CB / SF, pomeo / 4 copier papers, then they are tested using methods that evaluate their effectiveness in this area. Microcapsules are applied to a sheet called a GB sheet (a sheet with a covered back side) and tested in comparison with a standardized receiving sheet called a SF sheet (a sheet with a covered front side. The CB sheet coating consists of 75% capsules, 18. weight wheat starch and 7 wt.% of a binder, for example, hydroxyethyl ether starch or other water-soluble starch derivative. It is prepared by mixing 100 parts by weight of aqueous suspension of microcapsules containing tO in,% of the latter, 125 parts by weight of water , 10 wheat starch and Q parts by weight of 10% aqueous binder solution, the pH of the slurry was adjusted to 9 "The coating was applied using a rod wrapped with wire to apply a wet film coating in the amount of 9 kg per stack of paper (m 2). The coating of the comparative SF sheet consists of metal-modified phenolic resin, kaolin and other additives and bonding material. When the SHEET CB and the sheet of SF are combined from the side of the coatings applied on them and a certain pressure is applied to them, the microcapsules on the sheet CB are destroyed, the material contained in them is released and interacts with the acidic components of the sheet of SF, which results in staining. This is a test related to. the collapse of the capsules and the appearance of the okrhashi-. Vania is called an assessment of the intensity of a typewriter (TI), and the values of TI indicate the ratio of the reflection coefficient of prints obtained on the SF-sheet using a typewriter to the reflection coefficient of the back side of the paper. High values of this parameter are indicative of a slight color appearance, while low values indicate good color appearance. Heat a CB-sheet in a heating chamber at 18 h, and then repeating the whole experiment after thermostating. This sample shows that poor microcapsules practically completely abolish the ability to transfer images (prints) 8 to the process of such thermostating, and good microcapsules withstand such thermostating and do not lose their ability to produce prints. One of the significant advantages of the proposed method is the fact that high quality capsules are formed in a wide range of formaldehyde and melamine ratios. These results are presented in Table. 1, where the F: M (formaldehyde: melamine) ratio is given, the initial intensity of the typewriter prints, ITI before thermostating, the intensity of the TI typewriter prints after thermostating for the capsules obtained according to the method described in this example. Table 1 Example
    [2]
    2. This example is similar to Example 1, except that 180 g of the material of the capsule core is added to the solution of the modifier, and then 27 g of a 37% formaldehyde solution and 12.6 g of dry melamine are added to the resulting emulsion. Good quality chili capsules. I Example 3. A pI solution of 100 g of water and 50 g of a 10% aqueous solution of a copolymer of methyl vinyl ether and maleic anhydride with a molecular weight of 250000 is brought to 73 with a 20% aqueous solution of sodium hydroxide. 100 ml of a standard capsule core material, as in Example 1, is emulsified in this solution and the resulting emulsion is placed in a water bath heated to 5 ° C. While stirring, 23.3 g of a solution consisting of 80 g of melamine in 19b is added to the emulsion. g of an aqueous solution of 9 1 formaldehyde. The stirring is stopped, the water bath thermoregulator is turned off after 1 h tO min. . Capsule formation is determined by the so-called SF copy method. An emulsion containing all the capsule-forming ingredients is applied on reactive SF paper. The color appears when the dye interacts with the SF coating. The formation of microcapsule walls is accompanied by a softening of the color when the emulsion is applied, and is measured using a densitometer, which allows the reflection coefficient of the coated surface to be determined. The value of the reflection coefficient of prints on the SF sheet after 22 hours is b5%. An example. The pH of the solution of 280 g of water and 20 g of a 50% aqueous solution of polyacrylic acid with a molecular weight of 5000 is adjusted to 5.12 with a 20% aqueous solution of sodium hydroxide. In this solution, emulsify 200 ml of the standard core material. The emulsion was thermostatic in a NOI water bath at 55 ° C, adding with stirring + 6.6 g of a solution of 80 g of melamine in 106 g of an aqueous solution of formaldehyde. Thermostating and stirring are carried out for 19 hours. After 19 hours, the reflectance on the SF sheet is 70. Example 5. The pH of a solution of 111.5 g of water and 38.5 g of a 13% aqueous solution of a copolymer of butadiene and maleic anhydride is adjusted to 5И2 with a 20% an aqueous solution of sodium hydroxide. In this solution, 100 ml of the standard core material is emulsified. The resulting emulsion is thermostatted in a water bath at 55c, adding to it with stirring 23.3 g of a solution of 100 g of Melamine in 132.5 g of a 37% aqueous solution of formaldehyde. After 4 hours, stirring stops, but temperature control | continue for a total of 21 hours. After 21 hours, the reflection coefficient of the print on the sheet is 60. Example bp of a solution of a 101% aqueous solution of a copolymer of ethylene and maleic anhydride, as in Example 1, and 309 g the water is adjusted to 5 with a 20% aqueous solution of sodium hydroxide. In this capsule. The emulsion was thermostatic in a water bath at. After 1 h 5 min, the emulsion sample deposited on the SF sheet had a reflectance of 53%. A sample deposited on a non-reactive paper showed a reflection coefficient of 5E1. Example 15 A solution of 20 g of methylol melamine and 15 g of a 37% aqueous solution of formaldehyde is stirred at room temperature for an hour until the solution becomes less viscous and homogeneous; The pH of the solution thus obtained | ea is about 6.0. 20 g of an aqueous solution of polyacrylic acid is mixed with a molecular weight of 150,000 and 130 g of water. The pH is adjusted to 5. The previously prepared solution of methylol melamine is added to it and in the resulting mixture, 100 cm (90 g) of the standard core material is emulsified. The emulsion was thermostatic at 55 ° C in a water bath. After 1 h kS min, the sample of the emulsion applied on the SF paper has a reflection coefficient. The comparative sample on non-reactive paper has a reflectance of 61%. Example 16. The solution pH is 0 g of a solution of butadiene-maleic anhydride copolymer in water and 65 g of water are brought to 5 with a 20% aqueous solution of sodium hydroxide. Then a solution of 1.5 g of methiolmelamine with a molecular weight of 350, dissolved with 17.5 g of water, is added to it. Then, in the resulting mixture, 100 cm (90 g) of the standard material of the core of the capsules is emulsified, as in Example 1. The emulsion is thermostatically controlled in a water bath. After 1 hour 25 minutes, a sample of the emulsion applied on the SF strip, having a reflection coefficient of 62,. Example 17. In the same manner as described in Example 8, the pH of the solution is 35 g of a 10% aqueous solution of a copolymer of ethylene and maleic anhydride with a molecular weight of 750,000, 90,000 and 65 g of 10% aqueous solution. Ethylene-maleic acid anhydride copolymer with a molecular weight of 5,000 to 7,000 and 157 g of water was adjusted to 4.0 with 20; S-HOro aqueous solution of sodium hydroxide. In this solution, 270 g of standard capsule core material is emulsified, 50 g of methylated methylmelamine with a molecular weight of 350 are added to it. The total dry matter content in the system is brought to about 55. The resulting emulsion is placed in a water bath heated to and mixed for 2 h, after which the thermostat is turned off. The emulsion is stirred for overnight. After adjusting the pH of the emulsion to 7-8 with ammonium hydroxide, the formed capsules can be used to coat the substrates using methods known in the art to obtain carbon-free CB sheets. Example 18. This example illustrates an Eovani microcapsule method, which can be successfully performed without mixing the system after the ingredients are introduced into it. . The pH of the solution is 35 g of a 10% aqueous solution of copolymers of ethylene and maleic anhydride with a molecular weight of 75,000-90000, b5 g of a 10% aqueous solution of a copolymer of ethylene and maleic anhydride with a molecular weight of 5000-7000 and 170 g of water is brought to 7 s using a 20% aqueous solution of sodium hydroxide. In this solution, 270 g of standard capsule core material is emulsified, after which 50 g of methylated methane LOL is added to it with a molecular weight of 350. The resulting emulsion is mixed without thermostating in a water bath at. Satisfactory quality capsules that can be used to produce carbon-free carbon paper are formed without mixing from the system. Prints on the SF test sheets show the formation of capsules, the densitometer reading after 1 hour is at least 70. Example 19. In this example, three system modifiers with different molecular weights of example 1 are used. The capsules contain a solution of the material with an oil core colorless color-forming initial dye PI example 1, and the reading of the reflection coefficient is carried out according to the example
    [3]
    3. The results of the experiments are given in table. C,, Table Poly (ethylene maleic anhydride / molecular weight: 75000-90000Bk 15000-2000072 5000-700075 1500-200075 Poly (methyl vinyl ether maleic anhydride) with a molecular mass: I2500069 750000. 620000 6k Poly (acrylic acid) with molecular weight: less meme 300,000 68 less than 150000 73 less than 50,000 Example 20. A solution of 3 10-percent aqueous solution of ethylene and maleic anhydrile molecular weight of 90000 and b5 of aqueous copolymer of ethyl anhydride with molecules of 5000-7000 v 170 g of water to pH k, 0 as a result of sodium hydroxide injected. In this re-emulsify .270 g of solution 50 g of vortex formaldehyde is added to the mixture and the mixture is poured into boiling water (i 10,) and mixed for 15 minutes, after which 116 are removed, mixed and applied as a coating. a sheet of CB product with respect to a metal modified sheet of phenol resin SF was 58. And the intensity for typewriters measured after storing the Material overnight at was equal to 60. Comparative example (in the absence of a modifier) ;. In a solution of 125 g of methylated methylol melamine with a molecular weight of 2 W and 75 g of water are emulsified with 225 ml of standard capsule core material, as in Example 1. The pH of the emulsion is reduced to k, Q with glacial acetic acid. The emulsion was thermostatic with stirring in a water bath at 5 °. After 1 h 10 min, the contents of the reactor were a single solid mass. The proposed method for producing microcapsules produces microcapsules that retain their contents during storage and are pressure-sensitive on them, which can be used to produce copy paper. Invention A method for producing microcapsules by dispersing a water-insoluble core material in an aqueous dispersion of material forming shell, followed by the separation of the resulting microcapsules, characterized in that, in order to obtain microcapsules with an impermeable during storage, as all shell materials use a compound selected from the group consisting of a mixture of melamine and formaldehyde, monomeric methylolmelamine or its low molecular weight polymer, monomeric methylated methylolmelamine or its low molecular weight polymer, or mixtures thereof, and the process is carried out at a pH of k-6 and a temperature of 20 -100 ° C in the presence of a negatively charged polymer polyelectrolyte selected from the group consisting of a copolymer of ethylene and maleic anhydride with a molecular weight of 1000, a copolymer of methyl vinyl ether and maleic anhydride with a molecular weight of V250000, poly17 9653 118
    acrylic acid with molecular mass -f sources of information,
    SOY 5000, copolymer of propylene and taken into account in the examination of maleic anhydride, copolymer of bu- 1. The USSR patent for the application of thiene and maleic anhydride, comp. W 2152 06/05, cl. On 01 J 13/02, 1979.; poly (amide) acetate and maleic $ 2. US patent No. SUAUB, anhydride, taken as number of cells. 260-2, 5 F, spublik. 1972 0.4-15% by weight of water; dispersion. (prototype),
    类似技术:
    公开号 | 公开日 | 专利标题
    SU965341A3|1982-10-07|Method for making microcapsules
    US4089802A|1978-05-16|Capsule manufacture
    US4898696A|1990-02-06|Continuous preparation of microcapsules with melamine-formaldehyde condensate walls in aqueous dispersion
    US4406816A|1983-09-27|Process for the preparation of microcapsules, and the microcapsules obtained thereby
    FI74218B|1987-09-30|FOERFARANDE FOER FRAMSTAELLNING AV MIKROKAPSLAR.
    US6224795B1|2001-05-01|Low-formaldehyde dispersion of microcapsules of melamine-formaldehyde resins
    US4328119A|1982-05-04|Method of making microcapsules
    AU642010B2|1993-10-07|Microcapsules
    US3875074A|1975-04-01|Formation of microcapsules by interfacial cross-linking of emulsifier, and microcapsules produced thereby
    US4162165A|1979-07-24|Process for the production of microcapsular coating compositions containing pigment particles and compositions produced thereby
    US4785048A|1988-11-15|Polyurea and polyurea-epoxy microcapsules
    US4089834A|1978-05-16|Water-resistant micro-capsular opacifier system and products
    US4753968A|1988-06-28|Process for preparing microcapsules
    US4562116A|1985-12-31|Microcapsule for pressure-sensitive recording paper and process for producing the same
    US4308165A|1981-12-29|Formation of microcapsules by interfacial cross-linking of emulsifier, and resulting microcapsules
    KR840001591B1|1984-10-11|Process of preparing microcapsule for pressure-sensitive recording paper
    FI86036C|1992-07-10|FOERFARANDE FOER FRAMSTAELLNING AV MIKROKAPSLAR.
    US4209188A|1980-06-24|Microcapsules, method of making same, and carbonless copying system including said microcapsules
    GB2089312A|1982-06-23|Method of making microcapsules
    EP0149557B1|1990-09-19|Partially pressure-sensitive recording paper
    CA1108942A|1981-09-15|Capsule manufacture
    US5196149A|1993-03-23|Preparation of high solids, low viscosity carbonless paper gelatin base microcapsules
    CA1108944A|1981-09-15|Capsule manufacture
    US4000345A|1976-12-28|Substrate having coating thereon comprising microcapsular opacifying agents, and method of preparing same
    US5064470A|1991-11-12|High solids, low viscosity carbonless paper gelatin base microcapsule system
    同族专利:
    公开号 | 公开日
    SE414583B|1980-08-11|
    NO774457L|1978-07-03|
    NL172750B|1983-05-16|
    NL7714610A|1978-07-04|
    NO147980C|1983-07-20|
    DE2757528C2|1993-05-13|
    GB1542058A|1979-03-14|
    SE7714554L|1978-07-01|
    ATA931377A|1980-09-15|
    BR7708690A|1978-08-15|
    NO147980B|1983-04-11|
    NZ185773A|1979-06-19|
    US4100103A|1978-07-11|
    AU513160B2|1980-11-20|
    JPS5935258B2|1984-08-28|
    AR218281A1|1980-05-30|
    CH630269A5|1982-06-15|
    NL172750C|1983-10-17|
    DE2757528A1|1978-07-06|
    FR2375903B1|1981-12-24|
    FR2375903A1|1978-07-28|
    AT361895B|1981-04-10|
    JPS5384881A|1978-07-26|
    ES465482A1|1978-09-16|
    CA1108943A|1981-09-15|
    IT1114947B|1986-02-03|
    AU3175977A|1979-06-28|
    ZA777103B|1978-09-27|
    BE862371A|1978-04-14|
    DK584177A|1978-07-01|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    RU2474417C2|2007-06-18|2013-02-10|Дольхаи Клиника Эгесшегюдьи Кфт.|Biocidal capsules containing their preparation and tampon containing preparation|
    RU2756655C1|2020-11-27|2021-10-04|Федеральное государственное автономное образовательное учреждение высшего образования «Северныйфедеральный университет имени М. В. Ломоносова»|Method for producing hybrid organomineral microcapsules for concrete mixes and building mortars|US2838468A|1953-05-25|1958-06-10|Monsanto Chemicals|Process for preparing aminoplasts in bead form comprising reacting aminealdehyde resins with anionic polyelectrolytes|
    US3074845A|1959-10-14|1963-01-22|Plant Products Corp|Particulate pesticidal composition coated with an amido-aldehyde resin polymerized in situ|
    NL275857A|1961-03-13|1900-01-01|
    CH453305A|1963-10-21|1968-06-14|Pilot Pen Co Ltd|Process for encapsulating fine droplets of dispersed liquids|
    US3418656A|1965-10-23|1968-12-24|Us Plywood Champ Papers Inc|Microcapsules, process for their formation and transfer sheet record material coated therewith|
    US3607775A|1968-01-29|1971-09-21|Ncr Co|Process for encapsulating minute particles by use of autogenously polymerizable capsule wall material|
    BE717133A|1968-08-05|1968-12-27|
    US3726803A|1970-02-16|1973-04-10|Ncr|Capsule wall treating process utilizing condensation polymerization and capsule product|
    US4001140A|1974-07-10|1977-01-04|Ncr Corporation|Capsule manufacture|
    DE2940786A1|1979-10-08|1981-04-16|Basf Ag, 6700 Ludwigshafen|METHOD FOR PRODUCING MICROCAPSULES|US4369173A|1974-11-27|1983-01-18|Wickhen Products, Inc.|Antiperspirant compositions|
    US4189171A|1977-03-01|1980-02-19|Sterling Drug Inc.|Marking systems containing 3-aryl-3-heterylphthalides and 3,3-bisphthalides|
    JPS602100B2|1977-09-28|1985-01-19|Mitsubishi Paper Mills Ltd|
    US4197346A|1978-10-10|1980-04-08|Appleton Papers Inc.|Self-contained pressure-sensitive record material and process of preparation|
    JPS6023859B2|1978-11-14|1985-06-10|Kanzaki Paper Mfg Co Ltd|
    JPS5592135A|1978-12-29|1980-07-12|Kanzaki Paper Mfg Co Ltd|Production of microcapsule|
    JPS5833116B2|1979-03-28|1983-07-18|Mitsubishi Paper Mills Ltd|
    US4433637A|1979-06-04|1984-02-28|Vectra International Corporation|Microencapsulated cholesteric liquid crystal temperature measuring device for determining the temperature of non-planar or planar surfaces|
    JPS6244970B2|1979-10-02|1987-09-24|Fuji Photo Film Co Ltd|
    DE2940786A1|1979-10-08|1981-04-16|Basf Ag, 6700 Ludwigshafen|METHOD FOR PRODUCING MICROCAPSULES|
    AU539624B2|1980-04-08|1984-10-11|Wiggins Teape Group Limited, The|Production of microcapsules|
    DE3022453A1|1980-06-14|1982-01-07|Bayer Ag, 5090 Leverkusen|METHOD FOR PRODUCING MICROCAPSULES|
    JPS6352595B2|1980-12-19|1988-10-19|Fuji Photo Film Co Ltd|
    US4407231A|1981-09-28|1983-10-04|The Clorox Company|Movement activated odor control animal litter|
    US4454083A|1981-12-21|1984-06-12|Appleton Papers Inc.|Continuous microencapsulation|
    JPH0257985B2|1982-02-13|1990-12-06|Mitsubishi Paper Mills Ltd|
    US4444699A|1982-04-20|1984-04-24|Appleton Papers Inc.|Capsule manufacture|
    US4490313A|1983-01-24|1984-12-25|Appleton Papers Inc.|Capsule manufacture|
    JPH0627425Y2|1983-01-26|1994-07-27|三菱製紙株式会社|No-carbon paper for kanji printer|
    US4525520A|1983-03-28|1985-06-25|Kanzaki Paper Manufacturing Company, Ltd.|Method of preparing microcapsules|
    JPS6256778B2|1983-06-14|1987-11-27|Kanzaki Paper Mfg Co Ltd|
    US4493869A|1983-10-11|1985-01-15|Minnesota Mining And Manufacturing Company|Fragrance-releasing microcapsules on a see-through substrate|
    US4528226A|1983-10-11|1985-07-09|Minnesota Mining And Manufacturing Co.|Stretchable microfragrance delivery article|
    JPH0346315B2|1984-05-15|1991-07-15|Mitsubishi Paper Mills Ltd|
    EP0188807B2|1984-12-24|1993-05-26|Papierfabrik August Koehler AG|Process for encapsulating oils containing products which produce a colour by reaction, microcapsules produced by said process and their use in carbon papers|
    JPS61174941A|1985-01-28|1986-08-06|Kanzaki Paper Mfg Co Ltd|Preparation of microcapsule|
    US4594370A|1985-03-29|1986-06-10|The Mead Corporation|Amine-formaldehyde microencapsulation process|
    JPH0586250B2|1986-05-26|1993-12-10|Fuji Photo Film Co Ltd|
    DE3771446D1|1986-10-23|1991-08-22|Ciba Geigy Ag|FIGHTING EKTOPARASITES.|
    US4935172A|1987-05-15|1990-06-19|Mitsubishi Paper Mills, Ltd.|Method for producing microcapsules|
    US4978483A|1987-09-28|1990-12-18|Redding Bruce K|Apparatus and method for making microcapsules|
    US4963461A|1987-10-02|1990-10-16|Fuji Photo Film Co., Ltd.|Light-sensitive micropcapsule and light-sensitive material employing the same|
    JP2634836B2|1988-01-29|1997-07-30|大王製紙株式会社|Manufacturing method of microcapsules|
    JP2502146B2|1989-04-12|1996-05-29|日本製紙株式会社|Microcapsule manufacturing method|
    JPH0813901B2|1990-02-19|1996-02-14|株式会社ホーネンコーポレーション|Method for producing hollow melamine resin crosslinked particles having uniform particle diameter and crosslinked particles|
    JP2539690B2|1990-02-19|1996-10-02|株式会社ホーネンコーポレーション|Method for producing melamine resin crosslinked particles having a uniform particle size|
    US5084433A|1990-11-21|1992-01-28|Minnesota Mining And Manufacturing Company|Carbonless paper printable in electrophotographic copiers|
    US5353820A|1992-02-06|1994-10-11|Gillette Canada Inc.|Flavored dental cleaning article and method|
    EP0573210B2|1992-06-04|2005-11-23|Arjo Wiggins Limited|Pressure-sensitive record material|
    US5334094A|1992-09-21|1994-08-02|Minnesota Mining And Manufacturing Company|Carbonless pad assembly|
    GB9221621D0|1992-10-15|1992-11-25|Wiggins Teape Group Ltd|Solvents for use in pressure-sensitive record material|
    JPH06269657A|1993-03-17|1994-09-27|Sakura Color Prod Corp|Production of microcapsule|
    GB9313790D0|1993-07-03|1993-08-18|Wiggins Teape Group The Ltd|Pressure-sensitive copying material|
    IT1276525B1|1994-04-13|1997-10-31|Webcraft Technologies Inc|DEVICE AND PROCEDURE FOR THE SELECTIVE EXPOSURE OF MICRO-ENCAPSULATED LIQUIDS.|
    GB9414637D0|1994-07-20|1994-09-07|Wiggins Teape Group The Limite|Presure-sensitive copying material|
    US5680876A|1995-06-01|1997-10-28|Gillette Canada Inc.|Floss brush manufacture and product|
    US5866269A|1995-08-10|1999-02-02|Appleton Papers Inc.|Agricultural mulch with extended longevity|
    AU700493B2|1995-08-10|1999-01-07|Appleton Papers Inc.|Mulching composite|
    GB9522233D0|1995-10-31|1996-01-03|Wiggins Teape Group The Limite|Pressure-sensitive copying paper|
    US6203723B1|1998-03-12|2001-03-20|Ying Yen Hsu|Microencapsulated liquid crystal having multidomains induced by the polymer network and method|
    US6310002B1|2000-03-07|2001-10-30|Appleton Papers Inc.|Record material|
    US6592990B2|2000-09-06|2003-07-15|Appleton Papers Inc.|In situ microencapsulated adhesive|
    US6841515B2|2001-01-22|2005-01-11|Unified Enviromental Services Group, L.L.C.|Production and use of biosolid granules|
    GB0106560D0|2001-03-16|2001-05-02|Quest Int|Perfume encapsulates|
    US20050193692A1|2001-05-02|2005-09-08|Playtex Products, Inc.|Waste disposal device including rotating cartridge coupled to hinged lid|
    US7694493B2|2001-05-02|2010-04-13|Playtex Products, Inc.|Waste disposal device including a geared rotating cartridge|
    US7712285B2|2001-05-02|2010-05-11|Playtex Products, Inc.|Waste disposal device including a sensing mechanism for delaying the rotation of a cartridge|
    US7708188B2|2001-05-02|2010-05-04|Playtex Products, Inc.|Waste disposal device including a hamper accessible through a movable door|
    US8091325B2|2001-05-02|2012-01-10|Playtex Products, Inc.|Waste disposal device including a diaphragm for twisting a flexible tubing dispensed from a cartridge|
    US7617659B2|2001-05-02|2009-11-17|Playtex Products, Inc.|Waste disposal device including a cartridge movable by rollers|
    US7503159B2|2001-05-02|2009-03-17|Playtex Products, Inc.|Waste disposal device including an external actuation mechanism to operate a cartridge|
    US7316100B2|2001-05-02|2008-01-08|Playtex Products, Inc.|Waste disposal device including a film cutting and sealing device|
    US7434377B2|2001-05-02|2008-10-14|Playtex Products, Inc.|Waste disposal device including a rotatable geared rim to operate a cartridge|
    US7503152B2|2001-05-02|2009-03-17|Playtex Products, Inc.|Waste disposal device including rotating cartridge coupled to lid|
    US7958704B2|2001-05-02|2011-06-14|Playtex Products, Inc.|Waste disposal device including a mechanism for scoring a flexible tubing dispensed from a cartridge|
    US6544926B1|2001-10-11|2003-04-08|Appleton Papers Inc.|Microcapsules having improved printing and efficiency|
    US20030216488A1|2002-04-18|2003-11-20|The Procter & Gamble Company|Compositions comprising a dispersant and microcapsules containing an active material|
    AR040093A1|2002-05-21|2005-03-16|Procter & Gamble|CLEANING COMPOSITION THAT INCLUDES SUSPENDED PEARLS|
    US20030224030A1|2002-05-23|2003-12-04|Hirotaka Uchiyama|Methods and articles for reducing airborne particulates|
    US6939826B2|2002-06-25|2005-09-06|Appleton Papers, Inc.|Product authentication|
    US7108190B2|2003-02-28|2006-09-19|Appleton Papers Inc.|Token array and method employing authentication tokens bearing scent formulation information|
    US6932602B2|2003-04-22|2005-08-23|Appleton Papers Inc.|Dental articulation kit and method|
    US20060063125A1|2003-04-22|2006-03-23|Hamilton Timothy F|Method and device for enhanced dental articulation|
    US20040251309A1|2003-06-10|2004-12-16|Appleton Papers Inc.|Token bearing magnetc image information in registration with visible image information|
    US20050044819A1|2003-09-02|2005-03-03|Chomik Richard S.|Waste storage device|
    US20050074484A1|2003-10-07|2005-04-07|Estanislao Roderico B.|Product for administration of active agents to different areas of the skin|
    US7531365B2|2004-01-08|2009-05-12|International Flavors & Fragrances Inc.|Analysis of the headspace proximate a substrate surface containing fragrance-containing microcapsules|
    US6925781B1|2004-02-03|2005-08-09|Playtex Products, Inc.|Integrated cutting tool for waste disposal method and apparatus|
    US20070196502A1|2004-02-13|2007-08-23|The Procter & Gamble Company|Flowable particulates|
    DE602004008209T2|2004-02-17|2008-05-29|Sensient Imaging Technologies S.A.|Copy sheet and method for creating or enhancing copy quality of a copy sheet|
    US7452547B2|2004-03-31|2008-11-18|Johnson&Johnson Consumer Co., Inc.|Product for treating the skin comprising a polyamine microcapsule wall and a skin lightening agent|
    WO2006048412A1|2004-11-08|2006-05-11|Freshpoint Holdings Sa|Time-temperature indicating device|
    US9695092B2|2006-02-23|2017-07-04|Anuvia Plant Nutrients Corporation|Process for treating sludge and manufacturing bioorganically-augmented high nitrogen-containing inorganic fertilizer|
    US8105413B2|2005-02-23|2012-01-31|Vitag Corporation|Manufacturing of bioorganic-augmented high nitrogen-containing inorganic fertilizer|
    US8192519B2|2005-03-09|2012-06-05|Vitag Corporation|Beneficiated, heat-dried biosolid pellets|
    JP5090335B2|2005-03-25|2012-12-05|アップルトンペーパーズインコーポレイテッド|Materials that can be bonded and fixed|
    US7717261B2|2005-06-10|2010-05-18|Philip Morris Usa Inc.|Hinge lid aroma pack|
    AU2006292505B2|2005-09-15|2011-09-22|Anuvia Plant Nutrients Holdings, Inc.|Organic containing sludge to fertilizer alkaline conversion process|
    US20070098148A1|2005-10-14|2007-05-03|Sherman Kenneth N|Aroma releasing patch on mobile telephones|
    CN103446963B|2006-04-20|2016-03-09|宝洁公司|Flowable particulates|
    DE602006008432D1|2006-05-09|2009-09-24|Cognis Ip Man Gmbh|Use of microcapsules for the production of paints and varnishes|
    US20080090942A1|2006-05-31|2008-04-17|George Hovorka|Tamper evident paint having microcapsules containing signal indicators|
    US7935201B2|2006-11-29|2011-05-03|Wausau Paper Mills, Llc|Non-slip masking product, and methods|
    CN101687720B|2007-02-16|2014-02-12|维塔格控股有限责任公司|Process for treating sludge and manufacturing bioorganically-augmented high nitrogen-containing inorganic fertilizer|
    WO2008153882A1|2007-06-11|2008-12-18|Appleton Papers Inc.|Benefit agent containing delivery particle|
    WO2009080695A1|2007-12-21|2009-07-02|Akzo Nobel N.V.|Compositions for protection and release of active materials|
    US20090274906A1|2008-05-01|2009-11-05|Appleton Papers Inc.|Particle with low permeance wall|
    US8071214B2|2008-05-01|2011-12-06|Appleton Papers Inc.|Particle with selected permeance wall|
    US8067089B2|2008-05-01|2011-11-29|Appleton Papers Inc.|Cationic microcapsule particles|
    CA3115327A1|2008-06-04|2009-12-10|Jp Laboratories Inc.|A monitoring system based on etching of metals|
    US7915215B2|2008-10-17|2011-03-29|Appleton Papers Inc.|Fragrance-delivery composition comprising boron and persulfate ion-crosslinked polyvinyl alcohol microcapsules and method of use thereof|
    US8455098B2|2009-04-07|2013-06-04|Appleton Papers Inc.|Encapsulated solid hydrophilic particles|
    WO2011036174A1|2009-09-25|2011-03-31|B.R.A.I.N. Biotechnology Research And Information Network Ag|A novel method for the production of a antimicrobial peptide|
    WO2011084141A2|2009-12-21|2011-07-14|Appleton Papers Inc.|Hydrophilic liquid encapsulates|
    ES2741133T3|2009-12-30|2020-02-10|Anuvia Plant Nutrients Holdings Llc|High value fertilizer bioorganically increased|
    US20110269657A1|2010-04-28|2011-11-03|Jiten Odhavji Dihora|Delivery particles|
    US9993793B2|2010-04-28|2018-06-12|The Procter & Gamble Company|Delivery particles|
    US9186642B2|2010-04-28|2015-11-17|The Procter & Gamble Company|Delivery particle|
    BR112013025243B1|2011-03-28|2021-07-06|Anuvia Plant Nutrients Holdings, Inc.|High value organically intensified inorganic fertilizers|
    CN103458859A|2011-04-07|2013-12-18|宝洁公司|Personal cleansing compositions with increased deposition of polyacrylate microcapsules|
    WO2012138696A2|2011-04-07|2012-10-11|The Procter & Gamble Company|Shampoo compositions with increased deposition of polyacrylate microcapsules|
    MX2013010981A|2011-04-07|2013-10-30|Procter & Gamble|Conditioner compositions with increased deposition of polyacrylate microcapsules.|
    US20120095605A1|2011-09-17|2012-04-19|Tran Bao Q|Smart building systems and methods|
    US8359750B2|2011-12-28|2013-01-29|Tran Bao Q|Smart building systems and methods|
    US8951708B2|2013-06-05|2015-02-10|Xerox Corporation|Method of making toners|
    JP2015086249A|2013-10-28|2015-05-07|スリーボンドファインケミカル株式会社|Microcapsule type thermosetting resin composition|
    US10485739B2|2014-10-16|2019-11-26|Encapsys Llc|High strength microcapsules|
    US9714397B2|2014-10-16|2017-07-25|Encapsys Llc|Controlled release microcapsules|
    US9714396B2|2014-10-16|2017-07-25|Encapsys Llc|Controlled release dual walled microcapsules|
    WO2016149148A1|2015-03-17|2016-09-22|3M Innovative Properties Company|Solventless anti-corrosion composition and methods of using the same|
    EP3302782A4|2015-06-05|2019-01-09|Anuvia Plant Nutrients Holdings, LLC|High value organic containing fertilizers and methods of manufacture|
    WO2017074995A1|2015-10-27|2017-05-04|Encapsys, Llc|Encapsulation|
    EP3541355A4|2016-11-21|2020-06-17|Bell Flavors And Fragrances, Inc.|Malodor counteractant composition and methods|
    EP3574061B1|2017-01-27|2021-11-10|Encapsys, LLC|Encapsulates|
    WO2020037242A1|2018-08-16|2020-02-20|Anuvia Plant Nutrients Holdings, Llc|Reactive inorganic coatings for agricultural fertilizers|
    WO2022002846A1|2020-07-01|2022-01-06|Laboratorios Miret, S.A.|Microencapsulated tcmtb|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US05/755,830|US4100103A|1976-12-30|1976-12-30|Capsule manufacture|
    [返回顶部]