WO1992008765A1 - Polyolefin pressure-sensitive adhesive compositions containing macromonomers - Google Patents
Polyolefin pressure-sensitive adhesive compositions containing macromonomers Download PDFInfo
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- WO1992008765A1 WO1992008765A1 PCT/US1991/007849 US9107849W WO9208765A1 WO 1992008765 A1 WO1992008765 A1 WO 1992008765A1 US 9107849 W US9107849 W US 9107849W WO 9208765 A1 WO9208765 A1 WO 9208765A1
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- carbon atoms
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- sensitive adhesive
- pressure
- adhesive composition
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- YXFVVABEGXRONW-UHFFFAOYSA-N Cc1ccccc1 Chemical compound Cc1ccccc1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J151/00—Adhesives based on graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Adhesives based on derivatives of such polymers
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J151/00—Adhesives based on graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Adhesives based on derivatives of such polymers
- C09J151/06—Adhesives based on graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Adhesives based on derivatives of such polymers grafted on to homopolymers or copolymers of aliphatic hydrocarbons containing only one carbon-to-carbon double bond
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J151/00—Adhesives based on graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Adhesives based on derivatives of such polymers
- C09J151/08—Adhesives based on graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Adhesives based on derivatives of such polymers grafted on to macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J7/00—Adhesives in the form of films or foils
- C09J7/30—Adhesives in the form of films or foils characterised by the adhesive composition
- C09J7/38—Pressure-sensitive adhesives [PSA]
- C09J7/381—Pressure-sensitive adhesives [PSA] based on macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2666/00—Composition of polymers characterized by a further compound in the blend, being organic macromolecular compounds, natural resins, waxes or and bituminous materials, non-macromolecular organic substances, inorganic substances or characterized by their function in the composition
- C08L2666/02—Organic macromolecular compounds, natural resins, waxes or and bituminous materials
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/14—Layer or component removable to expose adhesive
- Y10T428/1414—Ceramic, glass, glasslike, vitreous
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/14—Layer or component removable to expose adhesive
- Y10T428/1438—Metal containing
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31678—Of metal
- Y10T428/31692—Next to addition polymer from unsaturated monomers
- Y10T428/31696—Including polyene monomers [e.g., butadiene, etc.]
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31786—Of polyester [e.g., alkyd, etc.]
- Y10T428/31797—Next to addition polymer from unsaturated monomers
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31855—Of addition polymer from unsaturated monomers
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31855—Of addition polymer from unsaturated monomers
- Y10T428/3188—Next to cellulosic
Definitions
- This invention relates to pressure sensitive adhesive compositions comprising a copolymer with a saturated hydrocarbon backbone having one or more grafted pendant moieties preferably derived from polymerizable ethenylarene and conjugated diene monomers and to sheet materials coated therewith.
- PSA pressure sensitive adhesive
- Pressure sensitive adhesive compositions suitable, for example, for use in adhesive tape must have a requisite fourfold balance of adhesion, cohesion, stretchiness and elasticity as disclosed by U.S. Patent No. Re 24,906.
- the desire to maintain this balance of properties makes it extremely difficult to improve internal strength i.e., cohesiveness without sacrificing other desirable properties and destroying the overall pressure-sensitive nature of the adhesive system.
- PS block copolymers like the styrene-butadiene-styrene KRATONTM rubbers, can be used to improve the cohesive strength and hot-melt processability of PSAs.
- the PS block copolymers contain end-blocks which are capable of forming phase-separated/segregated "glassy" domains that act as thermally reversible crosslinks providing cohesive strength when such block copolymers are used in pressure-sensitive adhesives. At high temperatures the glassy domains effectively "dissolve” in the rubbery phase. When the polymer is cooled, the domains reform allowing recovery of the original physical and chemical properties.
- the reinforcing nature of phase-separation in polymers is described in more detail by D. Satas, "Handbook of Pressure-Sensitive Adhesive Technology",
- U.S. Patent No. 3,542,717 describes laminating adhesives made from tackified mixtures of ZN copolymers derived from ⁇ -olefin monomers of from 4 to 20 carbon atoms.
- the copolymer mixture has PSA properties, while certain other compositions functioned as hot-melt adhesives, see column 4, lines 22-34. While the cohesive strength of the adhesive was acceptable for its intended laminating applications, nothing is mentioned about shear strength at elevated temperature.
- U.S. Patent No. 3,954,697 discloses that PSAs provided by copolymers of polypropylene and C 6 to C 10 ⁇ -olefins can have good cohesive strength when hot-melt coated at a melt temperature of at least 350°F (177°C), a temperature at which the copolymers exhibit no detectable crystallinity when examined using X-ray or DSC techniques.
- U.S. Patent No. 4,178,272 discloses that a hot-melt adhesive that provides strong T-peel and lap shear bonds can be made using ⁇ -olefin polymers.
- the hot-melt adhesive is a blend of poly(propylene-co-higher 1-olefin), tackifying resin, and crystalline polypropylene. The blend is not said to be naturally tacky or a PSA.
- adhesive bonds are formed at 200°C.
- U.S. Patent No. 4,007,311 shows that grafting methyl methacrylate to a styrene-isoprene-styrene block copolymer enhances adhesion without regard for elasticity or cohesiveness.
- compositions that are PSAs at about 20°C to 30°C or become PSAs at higher temperatures comprising:
- macromonomer comprising the polymerized product of at least one of an ethenylarene and a conjugated diene monomer and having a terminal ⁇ -alkenyl group of at least 4 carbon atoms and;
- the invention provides sheet materials coated with the PSA composition.
- sheet materials comprise a backing member and the
- the invention provides articles comprising the coated sheet material in the configuration of a roll of tape comprising a flexible backing sheet having at least one major surface coated with the PSA of the invention.
- Another article of the invention is a transfer tape comprising a film of PSA composition of the invention between two release liners.
- living polymer means a polymer prepared by anionic polymerization that has no effective termination reactions (Courie, “Polymers: Chemistry and Physics of Modern Materials”, Intex Ed. Pub., NY, 1973, p. 82-3);
- At least one of an ethenylenearene and conjugated diene polymer means a polymer prepared by anionic polymerization that contains either or both of ethenylarene and conjugated diene units;
- ZN catalyst means a two-component coordination initiator or catalyst having the properties described by Seymour and Carraher, "Polymer
- linear omega-alkenyl group means a group having the formula
- alpha ( ⁇ )olefin means any vinyl-containing aliphatic monomer, and in this application includes ethylene;
- number-average molecular weight weight average molecular weight and Z-average molecular weight are well known mathematical descriptions of the molecular weight distribution of a polymer sample
- polydispersity (pp) is a measure of the molecular weight distribution of a polymer and is defined as Further explanation of the derivation of these terms may be found in Experimental Methods in Polymer Chemistry, Wiley and Sons, 1981, Chapter 3 entitled “Molecular Weight Averages", pages 57-61.
- the adhesives of the present invention impart improved shear strength without crosslinking.
- the graft copolymer of the invention is preferably phase-separating into rubbery and glassy domains that provide a PSA having a shear strength of at least 30 minutes, preferably from 75 to 10,000 minutes. It is further preferred that: 1) the rubber regions of the phase separated copolymer have a T g in the range of from -70°C to -10°C, 2) the glassy macromonomer rich domains have a T g in the range of from 20°C to 300°C, and 3) the macromonomer has a number average molecular weight in the range of from 2,000 to 30,000. Peel adhesions of the PSA composition can be adjusted to pre-selected values by adding tackifying resins to the composition.
- the neat or tackified phase separating PSA compositions have excellent peel strength, shear strength, tack, creep resistance, and processability. Furthermore, the adhesives have excellent thermal and thermo-oxidative stability because there are no residual ethylenically-unsaturated groups in the polymer backbone.
- phase separated domains of high T g glassy macromonomer act as physical/reversible crosslinks interconnecting adjacent low T g inherently tacky ⁇ -olefin regions. This dramatically increases the cohesive strength of the adhesive and makes possible the formulation of high shear strength adhesives.
- the PSAs of the invention can be normally tacky at 20-30°C or they can become tacky upon application of heat.
- the graft copolymers of use in the tacky PSA compositions of the invention are copolymers of (1) macromonomer comprising an ethenylarene-conjugated diene polymer having a terminal omega-alkenyl group of at least 4 carbon atoms and (2) one or more alpha-olefin having 2 to 18 carbon atoms, preferably having the following formulae:
- L is a covalent bond or a divalent linking group selected from the group consisting of groups, in which each of R 1 and R 2 is independently hydrogen, an alkyl group having 1 to
- L is a covalent bond or a group
- L 1 is a covalent bond or a divalent linking group in which R 1 and R 2 are defined above;
- R° is a saturated or unsaturated linear hydrocarbyl group having 2 to 20 carbon atoms, a branched hydrocarbyl group having 3 to 20 carbon atoms or cyclic hydrocarbyl group having 5 to 20 carbon atoms;
- R 7 is hydrogen or one or more alkyl groups having 1 to 16 carbon atoms, at least 60% of R 7 being an alkyl group having 4 to 12 carbon atoms;
- n is an integer having a value from 0 to 16 preferably from 0 to 4;
- p is an integer having a value of 1, 2, or 3
- each R is independently a monovalent hydrocarbyl group which is selected from alkyl groups having from 1 to 18 carbon atoms, aryl groups having from 6 to 10 carbon atoms, and cyclic hydrocarbyl groups having from 5 to 10 carbon atoms, preferably, R is methyl or ethyl;
- Z is a divalent polymeric group having either or both of polymerized ethenylarene and conjugated diene repeat units and preferably a number average molecular weight of from about 2,000 to about 30,000;
- a and b are numbers providing a number average molecular weight of 50,000 to 10,000,000 to the graft copolymer, a having a value that is 0.1 to 25% of (a + b), preferably 0.1 to 10% of (a + b) of one or both of 1)
- Z is a divalent polymeric group obtained by the anionic polymerization of one or more of 1) at least one ethenylarene monomer having 8 to 20 carbon atoms, and 2) at least one conjugated diene monomer having 4 to 20 carbon atoms.
- the divalent polymeric group Z can be a homopolymeric group comprised solely of ethenylarene monomers, or solely of conjugated diene monomers.
- the polymer can also be a copolymer comprising both ethenylarene and conjugated diene monomers.
- the copolymer can be a random copolymer, a block copolymer, or a tapered block copolymer.
- Z When Z is a block polymeric group, it may be di-block or higher. More preferably, Z has a number average molecular weight in the range of 2,000 to 30,000 and a polydispersity in the range of 1.05 to 5.0, preferably in the range of 1.05 to 3.0.
- the divalent polymeric Z group has the general formula:
- each R 3 , R 4 and R 5 is independently, hydrogen, a phenyl group, an alkyl group or alkenyl group having 1 to 12 carbon atoms [there being no more than 16 carbon atoms total in (R 3 + R 4 )], or any two of R 3 , R 4 and R 5 together with the carbon atoms to which they are attached form one or two saturated or unsaturated 5 or 6 carbon atom rings, preferably each of R 3 , R 4 and R 5 is hydrogen or methyl;
- R 6 is an aryl group having 6 to 18 carbon atoms, optionally substituted by lower alkyl groups having from 1 to 4 carbon atoms, trialkylsilyl, 2,2-dialkylalkoxysilyl, N,N-bis(trimethylsilyl)amino, trimethylsiloxyethyl groups; and 1,1-dimethylethoxycarbonyl; and
- x, y, and z are numbers providing a number average molecular weight of 2,000 to 30,000 to the polymeric Z group and expressing the number of ethenylarene and conjugated diene groups that are present in random or block configuration in the polymeric Z group, in which numbers any of x,y, and z can be zero, but at least one of x, y, and z is not zero.
- the macromonomers are prepared by either of methods I and II.
- method la the macromonomer is made by anionically
- a terminating agent having multiple functionality, e.g. an omega-alkenyl group and one or more group(s) capable of undergoing nucleophilic displacement reactions.
- useful terminating agents include omega-alkenyl acid halides and omega-alkenyl halides which react to form macromonomers containing carbonyl or covalent bond linkages (as shown in Summary Reactions I below).
- omega-alkenyl mono-, di-, and tri-, halosilanes whose highly reactive silicon-halogen bond allows controlled preparation of linear, branched, and star macromonomers having narrow molecular weight distributions are used as terminating agents in the preparation of the macromonomer (as shown in Summary Reactions II below).
- the macromonomer is prepared directly by reacting an initiator containing omega-alkenyl groups with anionically polymerizable ethenylarene and/or conjugated diene based monomers to form a living polymer and terminating the living anion by reaction with alcohol as is well known in the art.
- the polymerization and termination reactions are summarized in Summary Reactions III, below.
- the macromonomers of use in the adhesive compositions of the invention have a glass transition temperature in the range of -70° to above
- the living polymer anion can be converted to an alkoxy anion by the addition of ethylene oxide or substituted ethylene oxide prior to reaction with the terminating agent (Termination Types C(a), C(b), and E).
- the Z groups can be conveniently prepared by reacting at least one of ethenylarene and conjugated diene monomers with an alkali metal hydrocarbon or alkoxide salt in the presence of an inert hydrocarbon or ether organic solvent that does not participate in, or interfere with, the polymerization process.
- Anionic polymerization methods are also described by Milkovich et al., (U.S. Patent Nos. 3,786,116 and 3,842,059), the disclosures of which are incorporated herein by reference.
- the divalent polymeric group, Z can be a homopolymeric group made from only ethenylarene monomers, or only from conjugated diene monomer. It also can be random or block polymeric group formed from both ethenylarene and conjugated diene monomers. When Z is a block polymeric group it may be di- block or higher.
- the macromonomer has a number average molecular weight in the range of 2,000 to 30,000.
- U.S. Patent No. 3,786,116 teaches that the molecular weight distribution of the polymer chains of a
- macromonomer should be narrow, i.e., a polydispersity of less than 1.1 for preparation of polymer having improved physical characteristics useful as tough, flexible self-supporting films, it has been found that useful PSA compositions according to the present invention can be made with macromonomer having a polydispersity of up to about 5 without deleterious effects on adhesive properties.
- the polydispersity of the macromonomer of the invention preferably can be from about 1.05 to 5.0, preferably 1.05 to 3.0.
- Any ethenylarene having 8 to about 20 carbon atoms that can be polymerized by anionic polymerization methods can be used in the preparation of the divalent Z group.
- Examples include: styrene(ethenyl benzene),
- ⁇ -methylstyrene (propenylbenzene), 1-ethenyl-2-methylbenzene, 1-ethenyl-3-methylbenzene, 1-ethenyl-4-methylbenzene, 1-ethenyl-4-(1,1-dimethylethyl)benzene, 4-dodecyl-1-ethenylbenzene, 1-ethenylnaphthalene, 2-ethenylanthracene,
- ethenylarenes substituted by groups that provide elevated glass temperatures to the macromonomers of use in the invention and are unreactive under anionic polymerization conditions are:
- Any conjugated diene having 4 to about 20 carbon atoms capable of polymerization by anionic methods can be used in the preparation of the
- linear and branched conjugated dienes examples include: 1,3-butadiene, 1,3-pentadiene, 1,3-hexadiene, 1,3-heptadiene,
- 2-methyl-1,3-butadiene isoprene
- 2,3-dimethyl-1,3-butadiene 2,3-diethyl-1,3-butadiene, 2,5-dimethyl-1,3-hexadiene
- 2-phenyl-1,3-butadiene 2,3-diphenyl-1,3- butadiene
- 2-methyl-6-methylene-2,7-octadiene myrcene
- Examples of cyclic conjugated dienes include: 1,2-bis(methylene)cyclopentane,
- Initiators for anionic polymerization may be any of the alkali metal hydrocarbyl salts which produce a monofunctional living polymer, i.e., only one end of the polymer contains a reactive ion.
- Such initiators include organometallic hydrocarbon salts of lithium, sodium, or potassium, for example, having an alkyl or alkenyl radical containing up to 20 carbon atoms or more, and preferably up to 8 carbon atoms.
- Illustrative alkali metal organometallic initiators include
- the preferred initiators are n-butyllithium, sec-butyllithium, and 3-butenyllithium.
- Terminating agents for use in Method I, Terminating Types A, B and C may be chosen from co-alkenyl halides containing 4 to 18 carbon atoms, preferably 4 to 10 carbon atoms, there being at least two carbon atoms between the halogen and the omega double bond and ⁇ -alkenoyl halides containing 5 to 18 carbon atoms, preferably 5 to 10 carbon atoms, there being at least 2 carbon atoms between the carbonyl group and the omega double bond.
- Illustrative alkenoyl chlorides include 5-hexenoyl chloride, 6-heptenoyl chloride, 7-octenoyl chloride, 9-decenoyl chloride, 10-undecenoyl chloride, 13-tetradecenoyl chloride, and 17-octadecenoyl chloride.
- the more preferred alkenoyl chlorides are 5-hexenoyl chloride and 10-undecenoyl chloride.
- Illustrative alkenyl halides include 3-butenyl chloride, 4-pentenyl chloride, 5-hexenyl chloride, 6-heptenyl chloride, 7-octenyl chloride, 9-decenyl chloride, 10-undecenyl chloride, and 17-octadecyl chloride.
- Preferred alkenyl halides are 3-butenyl chloride and 5-hexenyl chloride.
- Terminating agents for use in Method I, Termination Types D and E may be chosen from omega-alkenylhalosilanes containing up to 18 methylene groups, preferably 4 or more methylene groups, which are commercially available
- Illustrative ⁇ -alkenylhalosilanes include, for example: 3-butenyldimethylchlorosilane
- every Method II initiator molecule contains an alkenyl group
- every resulting living polymer anion contains an alkenyl group
- Method I macromonomers, the efficiency and yield of the termination reaction by Method II does not affect the conversion of living polymer to macromonomer.
- graft copolymerization of the ⁇ -olefin and the macromonomer according to the present invention are conducted using a ZN coordination catalyst.
- ZN coordination catalyst systems are described by Seymour and Carraher,
- the preferred 2-component catalyst systems are dialkyl aluminum chloride/titanium trichloride or dialkyl aluminum sesquichloride/vanadium oxytrichloride. Reaction takes place in the presence of inert solvents in the temperature range of about -100°C to abut +100°C. Suitable nonpolar organic reaction solvents include heptane, toluene, hexane, cyclohexane, pentane, and the like. The amount of solvent is generally about 10 to 30% by weight based on the total weight of the reactants and solvent.
- the preferred graft copolymer is prepared by copolymerization of ⁇ -olefin and reinforcing (see Summary Reactions I, Method la, type C(a), above) macromonomer.
- the graft copolymer can be prepared by techniques which provide a degree of predictability of the properties of the end products. These and other polymer grafting techniques are described by Noshay and McGrath in Block Copolymers, Academic Press, New York (1977), pages 13-16.
- a substantial increase in shear strength results when macromonomer is copolymerized with ⁇ -olefin.
- the amount of macromonomer in the copolymer determines the shear properties of the copolymer. With increasing amounts of macromonomer the resultant copolymer becomes increasing less tacky. However, these materials are useful as hot-tackifying, heat activated, or semi structural adhesives.
- the ⁇ -olefins of the the ZN graft copolymer of the PSA composition have the following formula:
- R 7 is as previously defined.
- Preferred ⁇ -olefin comonomers include, but are not limited to, linear C 6 to C 14 ⁇ -olefins such as 1-hexene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene and the like; and branched ⁇ -olefins such as 2-methylbutene, 3-methylhexene,
- Alpha-olefins such as ethylene, propylene, 1-butylene, isobutylene, and 1-pentylene can be used.
- the PSA composition of the invention contains a tackifying resin which imparts tack, lower viscosity, improved coatability, good heat stability, and improved peel adhesion.
- a tackifying resin which imparts tack, lower viscosity, improved coatability, good heat stability, and improved peel adhesion.
- Compatible tackifying resin can be prepared by polymerization of monomers consisting primarily of olefins and diolefins and include, for example, residual by-product monomers of the isoprene manufacturing process. These hydrocarbon tackifying resins typically exhibit Ball and Ring softening points of from about 80°C to about 145°C; acid numbers from about 0 to 2, and
- tackifying resins based on a C 5 olefin fraction of this type are “Wingtack” 95 and “Wingtack” 115 tackifying resins available from Goodyear Tire and Rubber Co.
- Other useful hydrocarbon tackifying resins include “Regalrez” 1078 and “Regalrez” 1126 tackifying resins available from Hercules Chemical Co., Inc. Wilmington, DE; ArkonTM resins, such as ArkonTM P115, available from Arakawa Forest Chemical Industries, Chicago, IL; and EscorezTM resins available from Exxon
- Suitable tackifying resins include the terpene polymers, such as polymeric resinous materials obtained by polymerization and/or copolymerization of terpene hydrocarbons such as alicyclic, mono and bicyclic monoteipenes and their mixtures including carene, isomerized pinene, terpentene, and various other terpenes.
- terpene polymers such as polymeric resinous materials obtained by polymerization and/or copolymerization of terpene hydrocarbons such as alicyclic, mono and bicyclic monoteipenes and their mixtures including carene, isomerized pinene, terpentene, and various other terpenes.
- Commercially available resins of the terpene type include the ZonarezTM terpene B-series and 7000 series available from Arizona Chemical Corp., Wayne, NJ 07470.
- Typical properties reported for the ZonarezTM terpene resins include ball and ring softening points of about 55°C to 125°C (ASTM E28-67), Acid Numbers of less than one (ASTM D465-59), and Saponification Numbers of less than one
- the terpene resin used in Examples below is a poly(beta-pinene) resin, PiccolyteTM S115 resin, available from Hercules Chemical Co., Inc., which has a Ball and Ring Softening Point of 115°C, an Acid Number of one, and Iodine Number of 190.
- the tackifying resins may contain ethylenic unsaturation; however, saturated tackifying resins are preferred for those applications where oxidation resistance is important.
- the total amount of tackifying resins in the composition is 1 to 150 parts, more preferably 5 to 50 parts, and most preferably 15 to 35 parts by weight per 100 parts of polymer.
- Incompatible tackifiers such as those based on rosin esters are not useful in the practice of the invention since they produce hazy blends. Furthermore, the presence of the incompatible tackifier results in a loss of tack.
- additives can also be included in the composition to provide adhesives for special end uses.
- additives may include pigments, dyes, plasticizers, fillers, stabilizers, ultraviolet absorbers, anti-oxidants, and the like.
- Plasticizers which can be employed include the well-known extender oils (aromatic, paraffinic, or napthanic) as well as wide variety of liquid polymers. Amount of additives used can vary from 0.1 to 50 weight percent depending on the end use desired.
- the adhesive composition of the present invention can be coated onto a wide range of substrate materials, some examples being polymer films such as polyethylene terephfhalate [PET], and biaxially oriented polypropylene [BOPP]; woven and non-woven fabrics; metals including metal foils such as aluminum, copper, lead, gold and the like; paper; glass; ceramics; and composite materials comprised of laminates of one or more of these materials.
- substrate materials some examples being polymer films such as polyethylene terephfhalate [PET], and biaxially oriented polypropylene [BOPP]; woven and non-woven fabrics; metals including metal foils such as aluminum, copper, lead, gold and the like; paper; glass; ceramics; and composite materials comprised of laminates of one or more of these materials.
- the present invention copolymers are useful to prepare PSA tapes and coated articles. Coating can be accomplished by methods known in the art on the desired substrates (representative substrates are mentioned above). Coatings having thicknesses in the range of 5 to 250 micrometers can be useful. When flexible substrates are used, the resulting tapes can be wound into rolls. For PSA tapes and transfer tapes it may be desirable to use primer and low adhesion backsize layers, or to interpose one or more release liners in the roll. Sheet stock such as labels and decals can also include at least one of a primer layer, a low adhesion backsize layer, and a releae liner.
- test methods used to evaluate the PSA coated flexible sheet materials are industry standard tests. The standard tests are described in detail in various publications of the American Society for Testing and Materials (ASTM). Philadelphia, PA. and the Pressure Sensitive Council (PSTC), Glenview III. The standard test methods are described in detail below. The reference source of each of the standard test methods is also given.
- the shear strength is a measure of the cohesiveness or internal strength of an adhesive. It is based upon the amount of force required to pull an adhesive strip from a standard flat surface in a direction parallel to the surface to which it has been affixed with a definite pressure. It is measured in units of time (minutes) required to pull a standard area of PSA coated sheet material from a stainless steel test panel under stress of a constant, standard load.
- the tests are conducted on adhesive coated strips applied to a stainless steel panel such that a 12.7 mm by 12.7 mm portion of each strip is in firm contact with the panel with one end portion of the tape being free.
- the panel with coated strip attached is held in a rack such that the exposed face of the backing of the strip forms an angle of 182° at the edge of the panel when a mass of one kilogram is applied as a hanging weight from the free end of the coated strip.
- the 2° greater than 180° is used to negate any peel forces, thus ensuring that only the shear forces are measured, to determine the holding power of the tape being tested.
- the time elapsed for each tape example to separate from the test panel is recorded as the shear strength.
- RT Shear The time at which the mass falls at room temperature.
- 1000+ The time at which the mass falls at room temperature.
- RT Shear is below about 30 minutes, the adhesive of the tape has generally failed by "pop off”.
- Peel adhesion is the force required to remove a coated flexible sheet material from a test panel measured at a specific angle and rate of removal. In the examples, this force is expressed in Newtons per 100 mm (N/100 mm) width of coated sheet. The procedure followed is:
- test specimen 12.7 mm wide is applied to a horizontally
- a 2.2 Kg rubber roller is used to press a 12.7 cm length of specimen into firm contact with the glass surface.
- the glass test plate is clamped in the jaws of a tensile testing machine which is capable of moving the plate away from the scale at a constant rate of 2.3 meters per minute.
- Compatibilities of various base polymers with the tackifying resins and the plasticizers are determined by melting the samples of each blend between glass plates and observing the clarity of blends.
- Number average molecular weight of the macromonomer is determined by the initiator/monomer ratio and the amount of initiator may vary from about 0.001 to about 0.1 per mole of monomer, or higher. Preferably, the concentration of the initiator will be from about 0.002 to about 0.04 mole initiator per mole of monomer. The smaller the initiator/monomer ratio the higher the number average molecular weight.
- the inherent viscosity is measured by conventional means using a
- Toluene was used as a solvent.
- the differential refractometer detector was a Hewlett-Packard Model 79877A. The system was calibrated using polystyrene standards and employing the least squares fit. All GPC calculations were performed on a Hewlett Packard Model 3388 integrator and all molecular weights averages are polystyrene equivalent molecular weights. The molecular weight averages and polydispersities were calculated according to standard procedures. GPC test methods are further explained in "Modern Size Exclusion Liquid Chromatography" Practical Gel Permeation Chromatography, John Wiley and Sons, 1979.
- a 10-undecenoyl-terminated polystyrene polymeric monomer having an average molecular weight of about 10,000 was prepared.
- a 1-liter, four-necked flask, fitted with a thermometer, mechanical stirrer, septum, Dean-Stark trap and condenser was charged with 500g reagent grade toluene and heated therein to reflux under a slow argon stream.
- a portion (150 g) of the toluene was removed through the trap to eliminate water from the system, leaving 350g (approximately
- Styrene monomer was first purified by passing over 200 mesh silica gel under argon and then 30 g (288 mmole) of this styrene monomer was introduced into the reaction flask by syringe through the septum to produce 8% by weight of the solution of styrene monomer in toluene.
- the solution was maintained at 60°C.
- About 5 to 10 drops of a 1.4 M solution of n-butyllithium in hexane was added dropwise to the monomer solution until a faint yellow color persisted, indicating completion of the reaction with the impurities.
- 2.2 mL of the solution was added rapidly, causing an exothermic reaction.
- the flask contents were maintained at 60°C.
- the reaction was essentially completed in 1 hour. The reaction was run an additional 2 hours to ensure the complete conversion of the monomer to the polymer. The contents were cooled to 35°C. Ethylene oxide gas was introduced over the reaction mixture and the solution was rapidly agitated for 15 minutes until the orange color the polystyryllithium had completely disappeared. The reaction was then quenched with 2.5 grams of 10-undecenoyl chloride. The reaction mixture was stirred for an additional 2 hours at room temperature. The resultant polymer solution was then reduced in volume to approximately one-third and added dropwise to a large excess of isopropanol.
- the precipitated polymer was collected on a large sintered funnel, dried overnight under ambient conditions, further dried at 65°C for 24 hours in a forced air oven and finally completely dried in vacuo. It was designated MAC-3b.
- Gel permeation chromatography revealed a number average molecular weight of 10,050, a weight average molecular weight of 13,270. Its polydispersity was 1.32. Analysis confirmed that the
- a 5-hexenyldimethylsilyl-terminated polystyrene polymeric monomer having an average molecular weight of about 10,000 was prepared. An oven dried
- a 3-butenyl-terminated polystyrene macromonomer having an average molecular weight of about 12,000 was prepared.
- Styrene (15 g, 144 mmole) was added to 200 g of cyclohexane under anhydrous conditions in the reaction flask producing 7.5 weight percent solution of monomer in the solvent.
- Approximately 5 to 10 drops of 0.07 molar solution of 3-butenyllithium in hexane were added to the monomer solution to remove impurities and then 19.7 mL of the 3-butenyllithium were rapidly added at 0-5°C.
- the temperature of the reaction was slowly raised to 60°C and maintained at that temperature throughout the course of the reaction.
- macromonomer has a structure that was essentially:
- IrganoxTM 1010 antioxidant available from Ciba-Geigy
- Ciba-Geigy Ciba-Geigy
- Example 1 The procedure in Example 1 was repeated except that 95 g of 1-octene and 5 g of MAC-3b were used to prepare the copolymer. The copolymer was obtained in 85 percent conversion.
- Example 13 The procedure and components of Example 6 were used except that a tackifier was added to the copolymer.
- Example 13 The procedure and components of Example 6 were used except that a tackifier was added to the copolymer.
- Example 13 The procedure and components of Example 13 were used except a tackifier was added to the copolymer.
- Example 13 The procedure in Example 13 was repeated except that 95 g of 1-hexene and 5 g of MAC-6c were used to prepare the copolymer. The copolymer was obtained in 72 percent conversion.
- Example 21 The procedure and components of Example 16 were used except a tackifier was added to the copolymer.
- Example 21 The procedure and components of Example 16 were used except a tackifier was added to the copolymer.
- Example 13 The procedure in Example 13 was repeated except that 95 g of 1-octene and 5g of MAC-6c were used to prepare the copolymer. The copolymer was obtained in 56 percent conversion.
- Example 24 The procedure and components of Example 21 were used except a tackifier was added to the copolymer.
- Example 24
- Example 25 The procedure in Example 13 was repeated except that 85 g of 1-hexene and 15 g of MAC-10 were used to prepare the copolymer. The copolymer was obtained in 65 percent conversion.
- Example 25 The procedure in Example 13 was repeated except that 85 g of 1-hexene and 15 g of MAC-10 were used to prepare the copolymer. The copolymer was obtained in 65 percent conversion.
- Example 25 The procedure in Example 13 was repeated except that 85 g of 1-hexene and 15 g of MAC-10 were used to prepare the copolymer. The copolymer was obtained in 65 percent conversion. Example 25
- Example 24 The procedure and components of Example 24 were used except a tackifier was added to the copolymer.
- Example 13 The procedure in Example 13 was repeated except that 95 g of
- Example 25 The procedure and components of Example 25 were used except a tackifier was added to the copolymer.
- Example 13 The procedure in Example 13 was repeated except that 95 g of 1-hexene and 5 g of MAC-20a were used to prepare the copolymer. The copolymer was obtained in 56 percent conversion. Examples 30-32
- Example 29 The procedure and components of Example 29 were used except that a tackifier was added to the copolymer. PREPARATION OF PRESSURE-SENSITIVE ADHESIVE TAPES
- Pressure-sensitive adhesive compositions were prepared from the macromonomer containing graft copolymers by blending the indicated quantity of tackifying resin with 100 parts by weight graft copolymer. Sufficient toluene was added to form a solution with a viscosity suitable for knife coating (5-15% solids) to produce a coating thickness of 25- ⁇ m of dry coating.
- composition was knife coated onto 38- ⁇ m biaxially oriented poly(ethylene- terephthlate) film.
- the coating was dried for 5 minutes at 150°F (65°C) and conditioned for 24 hours at 90% relative humidity and 90°F (37°C) to prepare PSA tapes suitable for testing.
- the tackifiers used in the PSA formulations were:
Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE69131073T DE69131073T2 (en) | 1990-11-15 | 1991-10-25 | MACROMONOMER-CONTAINING PRESSURE-SENSITIVE ADHESIVE COMPOSITIONS MADE OF POLYOLEFIN |
KR1019930701431A KR100191964B1 (en) | 1990-11-15 | 1991-10-25 | Polyolefin pressure-sensitive adhesive compositions containing macromonomers |
JP50079192A JP3222463B2 (en) | 1990-11-15 | 1991-10-25 | Polyolefin pressure-sensitive adhesive containing macromonomer |
AU89106/91A AU657717B2 (en) | 1990-11-15 | 1991-10-25 | Polyolefin pressure-sensitive adhesive compositions containing macromonomers |
EP92902577A EP0557463B1 (en) | 1990-11-15 | 1991-10-25 | Polyolefin pressure-sensitive adhesive compositions containing macromonomers |
BR919106966A BR9106966A (en) | 1990-11-15 | 1991-10-25 | ADHESIVE COMPOSITION, PRESSURE-SENSITIVE, ARTICLE, AND LAMINATED STRUCTURE |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US614,251 | 1990-11-15 | ||
US07/614,251 US5294668A (en) | 1990-11-15 | 1990-11-15 | Polyolefin pressure-sensitive adhesive compositions containing macromonomers |
Publications (1)
Publication Number | Publication Date |
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WO1992008765A1 true WO1992008765A1 (en) | 1992-05-29 |
Family
ID=24460463
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1991/007849 WO1992008765A1 (en) | 1990-11-15 | 1991-10-25 | Polyolefin pressure-sensitive adhesive compositions containing macromonomers |
Country Status (9)
Country | Link |
---|---|
US (2) | US5294668A (en) |
EP (1) | EP0557463B1 (en) |
JP (1) | JP3222463B2 (en) |
KR (1) | KR100191964B1 (en) |
AU (1) | AU657717B2 (en) |
BR (1) | BR9106966A (en) |
CA (1) | CA2094497C (en) |
DE (1) | DE69131073T2 (en) |
WO (1) | WO1992008765A1 (en) |
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AU648586B2 (en) * | 1990-09-19 | 1994-04-28 | Minnesota Mining And Manufacturing Company | Moisture-curable polyolefin pressure-sensitive adhesives |
WO1993011184A1 (en) * | 1991-11-27 | 1993-06-10 | Minnesota Mining And Manufacturing Company | Radiation curable saturated polyolefin pressure-sensitive adhesive |
US5346980A (en) * | 1992-04-14 | 1994-09-13 | Minnesota Mining And Manufacturing Company | Crosslinkable silarylene-siloxane copolymers |
US5859088A (en) * | 1993-04-13 | 1999-01-12 | Minnesota Mining And Manufacturing Company | Radiation-curable poly(α-olefin) adhesives |
EP0707604B1 (en) * | 1993-07-08 | 2000-05-10 | Avery Dennison Corporation | Acrylic-saturated rubber hybrid pressure-sensitive adhesives |
US5853642A (en) * | 1994-07-29 | 1998-12-29 | Minnesota Mining And Manufacturing Company | Process for the in-line polymerization of olefinic monomers |
US5747551A (en) * | 1994-12-05 | 1998-05-05 | Acheson Industries, Inc. | UV curable pressure sensitive adhesive composition |
US6586082B1 (en) | 1995-11-15 | 2003-07-01 | 3M Innovative Properties Company | Polymer-saturated paper articles |
US6177190B1 (en) | 1998-05-29 | 2001-01-23 | 3M Innovative Properties Company | Radiation curable poly(1-alkene) based pressure-sensitive adhesives |
KR101312197B1 (en) | 2000-02-15 | 2013-09-27 | 히타치가세이가부시끼가이샤 | Semiconductor Device |
US6544643B1 (en) | 2000-09-26 | 2003-04-08 | 3M Innovative Properties Company | Pressure sensitive adhesive comprising poly(1-alkene) elastomer and multifunctional (meth)acrylate, articles prepared therefrom and a method of making |
DE10129611A1 (en) * | 2001-06-20 | 2003-01-09 | Tesa Ag | PSA, especially for non-polar surfaces |
US20030143409A1 (en) * | 2001-07-06 | 2003-07-31 | Di Stefano Frank Vito | Blends of high Tg polymer emulsions and pressure sensitive adhesive polymer emulsions useful as pressure sensitive adhesives |
US7013818B2 (en) | 2001-10-18 | 2006-03-21 | Guangdong Esquel Textiles Co. Ltd. | Wrinkle free garment and method of manufacture |
US7192560B2 (en) * | 2001-12-20 | 2007-03-20 | 3M Innovative Properties Company | Methods and devices for removal of organic molecules from biological mixtures using anion exchange |
US7347976B2 (en) | 2001-12-20 | 2008-03-25 | 3M Innovative Properties Company | Methods and devices for removal of organic molecules from biological mixtures using a hydrophilic solid support in a hydrophobic matrix |
US7541402B2 (en) | 2002-10-15 | 2009-06-02 | Exxonmobil Chemical Patents Inc. | Blend functionalized polyolefin adhesive |
EP1558655B1 (en) | 2002-10-15 | 2012-08-29 | ExxonMobil Chemical Patents Inc. | Multiple catalyst system for olefin polymerization and polymers produced therefrom |
US7700707B2 (en) | 2002-10-15 | 2010-04-20 | Exxonmobil Chemical Patents Inc. | Polyolefin adhesive compositions and articles made therefrom |
US7981600B2 (en) * | 2003-04-17 | 2011-07-19 | 3M Innovative Properties Company | Methods and devices for removal of organic molecules from biological mixtures using an anion exchange material that includes a polyoxyalkylene |
US20050130177A1 (en) * | 2003-12-12 | 2005-06-16 | 3M Innovative Properties Company | Variable valve apparatus and methods |
US7727710B2 (en) * | 2003-12-24 | 2010-06-01 | 3M Innovative Properties Company | Materials, methods, and kits for reducing nonspecific binding of molecules to a surface |
US7939249B2 (en) * | 2003-12-24 | 2011-05-10 | 3M Innovative Properties Company | Methods for nucleic acid isolation and kits using a microfluidic device and concentration step |
EP2140001A2 (en) * | 2007-04-25 | 2010-01-06 | 3M Innovative Properties Company | Methods for nucleic acid amplification |
DE102013224774A1 (en) * | 2013-12-03 | 2015-06-03 | Tesa Se | Multi-layered product |
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- 1990-11-15 US US07/614,251 patent/US5294668A/en not_active Expired - Lifetime
-
1991
- 1991-10-25 BR BR919106966A patent/BR9106966A/en not_active IP Right Cessation
- 1991-10-25 CA CA002094497A patent/CA2094497C/en not_active Expired - Fee Related
- 1991-10-25 DE DE69131073T patent/DE69131073T2/en not_active Expired - Fee Related
- 1991-10-25 JP JP50079192A patent/JP3222463B2/en not_active Expired - Fee Related
- 1991-10-25 KR KR1019930701431A patent/KR100191964B1/en not_active IP Right Cessation
- 1991-10-25 AU AU89106/91A patent/AU657717B2/en not_active Ceased
- 1991-10-25 EP EP92902577A patent/EP0557463B1/en not_active Expired - Lifetime
- 1991-10-25 WO PCT/US1991/007849 patent/WO1992008765A1/en active IP Right Grant
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1993
- 1993-12-21 US US08/171,002 patent/US5354619A/en not_active Expired - Lifetime
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US4693935A (en) * | 1986-05-19 | 1987-09-15 | Minnesota Mining And Manufacturing Company | Polysiloxane-grafted copolymer pressure sensitive adhesive composition and sheet materials coated therewith |
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Also Published As
Publication number | Publication date |
---|---|
KR100191964B1 (en) | 1999-06-15 |
JPH06502447A (en) | 1994-03-17 |
US5354619A (en) | 1994-10-11 |
CA2094497A1 (en) | 1992-05-16 |
KR930702463A (en) | 1993-09-09 |
DE69131073D1 (en) | 1999-05-06 |
AU657717B2 (en) | 1995-03-23 |
DE69131073T2 (en) | 1999-09-16 |
US5294668A (en) | 1994-03-15 |
JP3222463B2 (en) | 2001-10-29 |
CA2094497C (en) | 1997-12-16 |
BR9106966A (en) | 1993-08-31 |
EP0557463B1 (en) | 1999-03-31 |
EP0557463A1 (en) | 1993-09-01 |
AU8910691A (en) | 1992-06-11 |
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