WO2001036501A1 - Ionomeric particulate composition - Google Patents
Ionomeric particulate composition Download PDFInfo
- Publication number
- WO2001036501A1 WO2001036501A1 PCT/US2000/012132 US0012132W WO0136501A1 WO 2001036501 A1 WO2001036501 A1 WO 2001036501A1 US 0012132 W US0012132 W US 0012132W WO 0136501 A1 WO0136501 A1 WO 0136501A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- composition
- monomer
- acid
- acrylate
- surfactant
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L51/00—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
- C08L51/003—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers grafted on to macromolecular compounds obtained by reactions only involving unsaturated carbon-to-carbon bonds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F265/00—Macromolecular compounds obtained by polymerising monomers on to polymers of unsaturated monocarboxylic acids or derivatives thereof as defined in group C08F20/00
- C08F265/08—Macromolecular compounds obtained by polymerising monomers on to polymers of unsaturated monocarboxylic acids or derivatives thereof as defined in group C08F20/00 on to polymers of nitriles
Definitions
- This invention relates to ionomeric particulate compositions useful for modifying the rheology and functionality of a polymer matrix so as to render the matrix more useful in applications that require adhesive properties.
- Polymerization occurs by mixing the premix phase with the water phase until the polymer beads are formed.
- the polymer beads may remain in the water prior to coating, during which time the beads are preferably storage-stable so as not to coalesce or agglomerate together. When coalescence is present, the beads tend to migrate towards one another and can form large masses. Coalescence of the beads hampers their handling and transportation and is undesirable.
- US Patent No. 5,952,420 discloses permeable, self-supporting, shaped structures that can be used in applications such as filters, masks, or respirators.
- the structure comprises a mass of active particulates (e.g., sorbents such as activated carbon, silica gel, or alumina granules) bonded together with pressure sensitive adhesive polymer particulates (also referred to as "PSA suspension beads") distributed in the mass of active particulate.
- PSA suspension beads from about 10 to 100 micrometers can be prepared using a combination of surfactants and using, as another co-monomer, a styrene sulfonate salt, such as sodium salt, to control particle size in the suspension polymerization.
- PSA suspension beads from about 1 to 10 micrometer can be achieved by homogenizing the polymerization reaction mixture comprising (1) the styrene sulfonate salt and (2) an amount of surfactant above the critical micelle concentration to the water phase before suspension polymerization. See Column 9. lines 39-44 and lines 57-61. Senkus also discloses that the PSA polymer is essentially any polymer, copolymer, or blend of copolymer that has pressure sensitive adhesive properties.
- a related patent is US Patent No. 5,696,199 (Senkus et al.) The polymeric particulate and beads discussed thus far typically use added chain transfer agents. Chain transfer refers to the termination of a growing polymer chain and the start of a new one thus controlling the molecular weight of the polymer.
- chain transfer agent which, in many cases, is some species that has been added to the polymerization process to effect chain transfer (referred to as an "added chain transfer agent").
- Chain transfer agents are used widely in polymerization processing to decrease the molecular weight of the polymer thereby imparting to the polymer one of the properties necessary for pressure sensitive tack.
- chain transfer agents are typically added to the oil phase, which contains the monomers.
- the monomers are acrylate esters of a non-tertiary alcohol having 1 to 14 carbon atoms
- common chain transfer agents include mercaptans, alcohols, and carbon tetrabromide, with isooctyl thioglycolate being a preferred one. See US Patent 4,833,179, Column 4, lines 37-42. The beads discussed thus far typically possess room temperature tackiness and thus are well suited as a pressure sensitive adhesive.
- homogenization which generally refers to reducing a material to particles and dispersing the particles throughout a liquid, can be achieved by using the appropriate agitation.
- a WaringTM blender is used for homogenization. It is well known in the suspension polymerization art that agitation can be important to achieving the desired particle-size distribution in the final product.
- This invention provides a novel ionomeric particulate composition where the particulate does not incorporate the use of an added chain transfer agent to control the molecular weight of the particulate.
- the resulting ionomeric particulates tend to have high molecular weight.
- the particulates can be formulated to have pressure sensitive tack or to have only minimal pressure sensitive tack, as desired.
- the particulates can act as a reinforcing agent when added to a polymer matrix.
- ionomeric particulates' size can be controlled through the use of surfactants and polyacrylamides.
- the ionomeric particulate composition of the invention comprises or consists essentially: at least one vinyl monomer; an acid monomer; a metal oxide; at least a first and a second surfactant, the first surfactant being a monomer surfactant; and a polyacrylamide.
- the present invention provides ionomeric particulate compositions that can be dispersed into a polymer matrix to modify the rheology, functionality, and physical properties (e.g., cohesive strength, adhesion, toughness, elasticity, flexibility) of the polymer matrix so as to yield a useful organic particulate-filled adhesive.
- a key advantage of the present invention lies in the ability to tailor the ionomeric particulate so that when combined with a particular polymer matrix, the resulting organic particulate- filled adhesive exhibits the desired properties.
- the ionomeric particulates can be used to modify any polymer matrix that is compatible with it to yield an organic particulate-filled adhesive useful for a variety of diverse applications.
- the adhesive can be formulated to have pressure sensitive adhesive properties by choosing the appropriate ionomeric particulate composition, polymer matrix, and various other components, such as plasticizers and tackifiers.
- the inventive ionomeric particulates are useful as part of a repulpable adhesive. Repulpability requires that the adhesive components be water-soluble or water dispersible. When the components are water dispersible, they are preferably of a sufficiently small particle size to pass through repulping equipment.
- the inventive ionomeric particulates are also useful as a part of an adhesive that is applied to mammalian skin to remove undesirable materials (e.g., comedomes, unwanted hair follicles, dirt, oil, debris, dead skin).
- the present invention provides an advantage to controlling the particulates' size through the use of surfactants and polyacrylamide and not relying on the more conventional method of homogenization.
- surfactants and polyacrylamide Applicants have discovered a robust system to control the particulates' by minimizing the need for homogenization during processing.
- Another advantage of the present invention is the ability to make an ionomeric particulate that has little to no acid functional groups.
- the ionomeric particulate still has a surface that is rich in inorganic salt groups attached to a polymer chain. This type of tailoring can be achieved by using a sufficient amount of a metal oxide to nearly fully neutralize the acid monomer.
- Yet another advantage of the present invention involves the post addition of dimethylaminoethyl me hacrylate (DMAEMA) during a second stage of suspension polymerization as further described below.
- DMAEMA dimethylaminoethyl me hacrylate
- Organic particulate-filled adhesive refers to an adhesive system having ionomeric particulate dispersed in a polymer matrix so as to modify the properties of the matrix.
- “Ionomeric particulate” means a polymer particle (typically in spherical form), having an oleophilic rich core and a surface that is rich in inorganic salt groups (such as zinc salt) attached to a polymer chain.
- “Monomer surfactant” acts as a surfactant in that it aids in the initial formation of the polymer bead during suspension polymerization but it is believed that at least a portion of the surfactant polymerizes and becomes a part of the ionomeric particulate. Also, at least a portion of the surfactant polymerizes in the water phase.
- Pressure sensitive adhesive means the adhesive has properties that include sufficient inherent tack, sufficient loss modulus, and sufficiently low glass transition temperature, to enable it to form a firm bond with a substrate upon contact under light pressure, e.g. finger pressure, at the temperature of use, e.g. room temperature of about 23°C (73° F).
- the ionomeric particulates are made by suspension polymerizing an oil phase in a water phase.
- the oil phase typically contains the vinyl monomer and an initiator.
- the water phase typically contains deionized water, acid monomer, metal oxide, surfactants, polyacrylamide, and optionally suspending agents.
- the components are discussed in detail below.
- the vinyl monomers is preferably present in an amount of at least 80 parts, more preferably about 85 to 95 parts, based on 100 parts total monomer content. Vinyl monomers can be straight chain, branched, or cyclic.
- One class of vinyl monomers useful in the present invention include monofunctional unsaturated acrylate ester monomers, of which a preferred class includes acrylic acid ester of non-tertiary alcohol having 1 to 14 carbon atoms. Included within the preferred class of acrylate monomers are, e.g., isooctyl acrylate (IOA), isononyl acrylate, 2-ethylhexyl acrylate, decyl acrylate, dodecyl acrylate, n-butyl acrylate, hexyl acrylate, hydroxyethyl acrylate (HEA), hydroxyethyl methacrylate (HEMA), and combinations thereof.
- IOA isooctyl acrylate
- isononyl acrylate 2-ethylhexyl acrylate
- decyl acrylate dodecyl acrylate
- n-butyl acrylate hexyl acrylate
- HEMA hydroxy
- vinyl monomers include vinyl acetate, styrene, octylacrylamide, and N-vinyl lactams such as N-vinyl pyrrolidone and N- vinyl caprolactam. These latter vinyl monomers can be used in combination with the above described acrylate monomers.
- the initiator is preferably present in an amount of about 0.05 to 1 part based on 100 parts total monomer weight.
- Useful initiators for polymerizing the vinyl monomers include those suitable for free-radical polymerization of the vinyl monomers.
- the initiators are preferably oil-soluble and have low solubility in water.
- Illustrative examples of useful initiators include organic peroxides such as benzoyl peroxide, lauryl peroxide, and various thermal initiators such as 2,2'-azobisisobutyronitrile.
- a preferred thermal initiator is 2,2'-azobis(2-methylbutyronitrile), commercially available from E. I. Du Pont de Nemours and Company, Wilmington, DE, under the trade name VAZOTM 67.
- the acid monomer is present in an amount up to about 20 parts based on the total monomer content.
- Acid monomers useful in for this invention preferably contain a carboxylic acid group.
- Acid monomers useful for the practice of this invention include acrylic acid, methacrylic acid, itaconic acid, maleic acid, fumaric acid, and citraconic acid.
- Preferred acid monomers include acrylic acid and methacrylic acid.
- the metal oxide is present in an amount necessary to fully neutralize the acid functionality of the acid monomer.
- the metal oxide is zinc oxide and the acid monomer is methacrylic acid.
- To have a "fully neutralize" particulate requires up to one (1) mole of zinc oxide per two (2) moles of methacrylic acid.
- a fully neutralized ionomeric particulate can be used to tailor the interaction between the particulates and the polymer matrix.
- a fully neutralized ionomeric particulate is used as a component in an organic particulate-filled adhesive that desirably has little to no interaction with the substrate to which the adhesive is applied. This situation is particularly important if the substrate may contain acid sensitive groups on its surface. If, on the other hand, the organic particulate-filled adhesive contains ionomeric particulate that has acid functional groups, there may be some interaction between the adhesive and the substrate containing acid sensitive groups. This interaction could result in leaving residual adhesive on the substrate, an undesirable result when clean removal of the adhesive is a desired feature.
- the ionomeric particulate can have acid functionality, which arises when the acid monomer is not fully neutralized.
- the metal oxide can be used to tailor the functionality of the ionomeric particulate.
- One skilled in the art should take care in selecting a suitable polymer matrix when making the organic particulate-filled adhesive given the different functionality of the ionomeric particulate.
- a polymer matrix suitable for a fully neutralized ionomeric particulate may not be suitable for when the ionomeric particulate contains acid functionality.
- zinc oxide (ZnO) is preferred, other useful metal oxides include calcium oxide (CaO), and magnesium oxide (MgO). It is believed that the metal oxides react with the acid monomer to form metal ionic salts of acid monomer, which are located on the surface of the particulates.
- Surfactants are preferably present in an amount of about 3 to 10 parts based on the total monomer content.
- the first type can be referred to as a monomeric surfactant.
- the second type can be referred to as conventional surfactants, which include those selected from the group consisting of non-ionic surfactant, anionic surfactant, and mixtures thereof.
- monomer surfactant examples include sodium styrene sulfonate.
- Monomer surfactants not only function like conventional surfactants in suspension polymerization by aiding in the formation of suspension beads and minimizing coalescence of the beads, but it is believed that at least a portion of the surfactant polymerize and become a part of the ionomeric particulate. Because monomer surfactants can become part of the particulate, there may be little residue of these surfactants in the aqueous phase. In this respect, monomer surfactants differ from conventional surfactants.
- Useful conventional surfactants that are non-ionic have a HLB (Hydrophilic-
- Lipophilic Balance i'om about 1 to 15.
- the HLB number describes the balance of the size and strength of the hydrophilic (water-loving or polar) groups and lipophilic (oil- loving or non-polar) groups of the surfactant.
- Illustrative useful non-ionic surfactants include (1) polyethers, e.g., ethylene oxide and propylene oxide condensates, which include straight and branched C 2 to C ⁇ 8 alkyl, alkylaryl, and alkenyl alcohol based copolymers of ethylene oxide and propylene oxide, such as those from Union Carbide Company, Danbury, CT, under the trademarked TERGITOL series, (2) block copolymers of ethylene oxide and propylene oxide, such as those available from BASF Company, Mt.
- polyethers e.g., ethylene oxide and propylene oxide condensates, which include straight and branched C 2 to C ⁇ 8 alkyl, alkylaryl, and alkenyl alcohol
- Non-ionic surfactants are the TWEEN and SPANS, trademarked compositions from ICI Inc., which are polyoxyalkylene derivatives of sorbitan and fatty acid esters.
- Useful conventional surfactants that are anionic include sulfates or sulfonates, such as sodium alkylaryl sulfonates and poly(alkyleneoxy) sulfates or sulfonates.
- a preferred sodium alkylaryl sulfonate is sodium dodecylbenzene sulfonate, which is commercially available from Rhone-Poulenc as RodacalTM DS-10.
- the poly(alkyleneoxy) compounds are ethylene oxide and propylene oxide or ethylene oxide and butylene oxide condensates, which include straight and branched C to C 18 alkyl, alkylaryl, and alkenyl alcohol based copolymers of ethylene oxide and propylene oxide or ethylene oxide and butylene oxide.
- This anionic surfactant is available from BASF under the tradename MAZON SAMTM 211, which is an alkylene polyalkoxy sulfate.
- Polyacrylamide is preferably present in an amount of about 0.01 to 2 parts based on the total monomer content and forms part of the water phase.
- the polyacrylamide functions as a stabilizer to produce ionomeric particulate of smaller size. It has been discovered that use of the polyacrylamide in combination with the anionic surfactants above can produce ionomeric particulate with less than about 10 micrometers in size. Thus it is not necessary to rely on the conventional homogenization process to make ionomeric particulate with less than 10 micrometer in volume average diameter.
- Preferred polyacrylamides are available from Cytec Industries, Inc., West Paterson, NJ under the trademarks CYANAMER N-300 and CYANAMER P-35. It is surprising that such a small amount of polyacrylamide can help to control the particulates' size.
- Suspending agents are preferably present in an amount of about 0.1 to 5 parts based on the total monomer content. In general, these agents are used in suspension polymerization to minimize coalescence of the particles. They can be minimally water- soluble inorganic salts, such as tribasic calcium phosphate, calcium carbonate, calcium sulfate, barium sulfate, barium phosphate, hydrophilic silicas, and magnesium carbonate.
- a preferred inorganic suspending agent is colloidal silica, such as Nalco 1042, available from NalcoTM Chemical Company.
- the inventive ionomeric particulate contains dimethyl aminoethy methacrylate (DMAEMA).
- DMAEMA dimethyl aminoethy methacrylate
- amino groups are basic in nature, ionomeric particulates containing them could be useful for certain substrates. The advantages discussed earlier for having a fully neutralized ionomeric particulate would apply here.
- the DMAEMA is preferably present in an amount of about 0.01 to 30 parts based on the total monomer content.
- the method of making an ionomeric particulate containing DMAEMA requires a two-step suspension polymerization process. In the first step, the oil phase and water phase are allowed to polymerize to form stable particles.
- the particles are about 70% polymerized before starting the second step, which is the addition of DMAEMA.
- the monomer insoluble in water and bulk polymerization can be carried out in suspended droplets.
- the water phase acts as a heat transfer medium.
- suspending agent and careful stirring among other techniques, can be used.
- One of the novel features of this invention combines the use of polyacrylamide and surfactants to minimize coalescence of the ionomeric particulates so as to control their size. Notably, this is done in the absence of careful stirring, such as use of homogenization.
- the methods of the invention require charging the water phase (often referred to as the "dispersion medium") into a heated vessel equipped with means for stirring the contents of the vessel. To the water phase is add a premixed oil phase that contains the vinyl monomers.
- the resulting ionomeric particulate compositions are storage stable in water (i.e., aqueous phase) and do not need to be collected and dried. However, if desired, the particulates can be collected, dried, and stored for later use.
- the ionomeric particulates of the invention have an average diameter of about 1 to 100 micrometers, more preferably about 1 to 50 micrometers, and most preferably from about 1 to 10 micrometers. It has been discovered that particle size of less than 10 micrometers can be produced with the inventive method using polyacrylamide and specific surfactants, as shown in the Examples.
- the suspension polymerization reaction was carried out in a 1 -liter split-flask equipped with a condenser, thermometer, nitrogen inlet, motor-driven agitator, and a heating mantle with temperature control.
- the reaction flask was first charged with the ingredients of the water phase listed in Table 1 and heated to 58°C.
- the water phase was maintained at this temperature with agitation and nitrogen-purging for about 1 hour to remove oxygen from the flask.
- a premixed charge of the oil phase listed in
- Examples 1 to 7 showed that all the particulates had particles size less than about 4 micrometer, which was achieved by using polyacrylamide and vigorous agitation (about 700 rpm) but not resorting to homogenization.
- Examples 8 and 9 exemplified fully neutralized ionomeric particulate compositions. Examples 8 and 9 also show that a wide range of particle size (from 2.8 to 12.7) can be achieved by using different polyacrylamides. None of the examples used an added chain transfer agent, such as isooctyl thioglycolate, or used colloidal silica as a suspending agent.
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Adhesives Or Adhesive Processes (AREA)
- Polymerisation Methods In General (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001538988A JP2003514930A (en) | 1999-11-17 | 2000-05-04 | Ionomer fine particle composition |
EP00930350A EP1250364A1 (en) | 1999-11-17 | 2000-05-04 | Ionomeric particulate composition |
AU48186/00A AU4818600A (en) | 1999-11-17 | 2000-05-04 | Ionomeric particulate composition |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/441,566 | 1999-11-17 | ||
US09/441,566 US6509404B1 (en) | 1999-11-17 | 1999-11-17 | Ionomeric particulate composition |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2001036501A1 true WO2001036501A1 (en) | 2001-05-25 |
Family
ID=23753397
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2000/012132 WO2001036501A1 (en) | 1999-11-17 | 2000-05-04 | Ionomeric particulate composition |
Country Status (5)
Country | Link |
---|---|
US (1) | US6509404B1 (en) |
EP (1) | EP1250364A1 (en) |
JP (1) | JP2003514930A (en) |
AU (1) | AU4818600A (en) |
WO (1) | WO2001036501A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1352919A1 (en) * | 2002-04-09 | 2003-10-15 | Eastman Kodak Company | Polymer particle stabilized by dispersant and method of preparation |
US6866902B2 (en) | 2002-04-09 | 2005-03-15 | Eastman Kodak Company | Ink recording element containing stabilized polymeric particles |
US7059714B2 (en) | 2002-04-09 | 2006-06-13 | Eastman Kodak Company | Ink printing method utilizing stabilized polymeric particles |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6620874B1 (en) * | 1999-11-17 | 2003-09-16 | 3M Innovative Properties Co | Method of making ionomeric particulates by suspension polymerization |
JP4537870B2 (en) * | 2005-03-16 | 2010-09-08 | ガンツ化成株式会社 | A method for producing an alkyl (meth) acrylate copolymer emulsion. |
US7645827B2 (en) * | 2006-03-08 | 2010-01-12 | 3M Innovative Properties Company | High shear pressure-sensitive adhesive |
US7531595B2 (en) * | 2006-03-08 | 2009-05-12 | 3M Innovative Properties Company | Pressure-sensitive adhesive containing silica nanoparticles |
US20080200587A1 (en) * | 2007-02-16 | 2008-08-21 | 3M Innovative Properties Company | Pressure-sensitive adhesive containing acicular silica particles crosslinked with polyfunctional aziridines |
US7393901B1 (en) | 2007-02-16 | 2008-07-01 | 3M Innovative Properties Company | Acrylate adhesives containing silica nanoparticles crosslinked with polyfunctional aziridines |
US20090149591A1 (en) * | 2007-12-07 | 2009-06-11 | Yong Yang | Paint Compositions With Low- or Zero-VOC Coalescence Aids and Nano-Particle Pigments |
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US5061757A (en) * | 1986-02-14 | 1991-10-29 | Bemis Company, Inc. | High impact strength polyamide blends and method for preparation thereof |
WO1995022955A1 (en) * | 1994-02-28 | 1995-08-31 | Minnesota Mining And Manufacturing Company | Improved color stability of dental compositions containing metal complexed ascorbic acid |
WO1996007677A1 (en) * | 1994-09-09 | 1996-03-14 | Chevron Chemical Company | Water dispersible ethylene ionomers |
WO1997030764A1 (en) * | 1996-02-21 | 1997-08-28 | E.I. Du Pont De Nemours And Company | Ionomeric composition for golf balls |
EP0921154A1 (en) * | 1997-06-20 | 1999-06-09 | Mitsui Chemicals, Inc. | Aqueous dispersion composition process for preparing the same, rust preventive, rust prevention method, and rust-proofed metallic products |
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US4952650A (en) | 1987-07-27 | 1990-08-28 | Minnesota Mining And Manufacturing Company | Suspension polymerization |
US4833179A (en) * | 1987-07-27 | 1989-05-23 | Minnesota Mining And Manufacturing Company | Suspension polymerization |
ATE145735T1 (en) * | 1988-12-28 | 1996-12-15 | Mita Industrial Co Ltd | CHARGE CONTROL RESIN, TONER CONTAINING THE RESIN AND METHOD FOR PRODUCING SUCH TONER |
US5292844A (en) * | 1991-05-22 | 1994-03-08 | Minnesota Mining And Manufacturing Company | Vinyl acetate modified suspension polymer beads, adhesives made therefrom and a method of making |
JP3423354B2 (en) * | 1992-05-27 | 2003-07-07 | 三井化学株式会社 | Emulsion polymer containing (meth) acrylate unit, emulsion thereof, method for producing them, and adhesive composition containing them |
JP3256583B2 (en) * | 1992-12-10 | 2002-02-12 | 株式会社リコー | Electrophotographic toner and method for producing the same |
US5696199A (en) | 1995-12-07 | 1997-12-09 | Minnesota Mining And Manufacturing Company | Pressure-sensitive adhesive polyacrylate polymer and method of making |
JPH1179926A (en) * | 1997-09-03 | 1999-03-23 | Shiyoufuu:Kk | Medical and dental curable composition |
JPH11209410A (en) * | 1998-01-23 | 1999-08-03 | Mitsui Chem Inc | Suspension polymerization method |
-
1999
- 1999-11-17 US US09/441,566 patent/US6509404B1/en not_active Expired - Lifetime
-
2000
- 2000-05-04 EP EP00930350A patent/EP1250364A1/en not_active Withdrawn
- 2000-05-04 JP JP2001538988A patent/JP2003514930A/en active Pending
- 2000-05-04 WO PCT/US2000/012132 patent/WO2001036501A1/en active Application Filing
- 2000-05-04 AU AU48186/00A patent/AU4818600A/en not_active Abandoned
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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US5061757A (en) * | 1986-02-14 | 1991-10-29 | Bemis Company, Inc. | High impact strength polyamide blends and method for preparation thereof |
WO1995022955A1 (en) * | 1994-02-28 | 1995-08-31 | Minnesota Mining And Manufacturing Company | Improved color stability of dental compositions containing metal complexed ascorbic acid |
WO1996007677A1 (en) * | 1994-09-09 | 1996-03-14 | Chevron Chemical Company | Water dispersible ethylene ionomers |
WO1997030764A1 (en) * | 1996-02-21 | 1997-08-28 | E.I. Du Pont De Nemours And Company | Ionomeric composition for golf balls |
EP0921154A1 (en) * | 1997-06-20 | 1999-06-09 | Mitsui Chemicals, Inc. | Aqueous dispersion composition process for preparing the same, rust preventive, rust prevention method, and rust-proofed metallic products |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1352919A1 (en) * | 2002-04-09 | 2003-10-15 | Eastman Kodak Company | Polymer particle stabilized by dispersant and method of preparation |
US6866902B2 (en) | 2002-04-09 | 2005-03-15 | Eastman Kodak Company | Ink recording element containing stabilized polymeric particles |
US6906157B2 (en) | 2002-04-09 | 2005-06-14 | Eastman Kodak Company | Polymer particle stabilized by dispersant and method of preparation |
US7059714B2 (en) | 2002-04-09 | 2006-06-13 | Eastman Kodak Company | Ink printing method utilizing stabilized polymeric particles |
US7390844B2 (en) | 2002-04-09 | 2008-06-24 | Eastman Kodak Company | Polymer particle stabilized by dispersant and method of preparation |
Also Published As
Publication number | Publication date |
---|---|
US6509404B1 (en) | 2003-01-21 |
AU4818600A (en) | 2001-05-30 |
JP2003514930A (en) | 2003-04-22 |
EP1250364A1 (en) | 2002-10-23 |
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