WO1998052981A1 - Procede de production d'ionomeres au moyen de terpolymeres d'ethylene - Google Patents
Procede de production d'ionomeres au moyen de terpolymeres d'ethylene Download PDFInfo
- Publication number
- WO1998052981A1 WO1998052981A1 PCT/US1997/008937 US9708937W WO9852981A1 WO 1998052981 A1 WO1998052981 A1 WO 1998052981A1 US 9708937 W US9708937 W US 9708937W WO 9852981 A1 WO9852981 A1 WO 9852981A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- inorganic metal
- acid
- terpolymer
- ethylene
- weight percent
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 47
- 229920001897 terpolymer Polymers 0.000 title claims abstract description 34
- 229920000554 ionomer Polymers 0.000 title claims abstract description 20
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 title claims description 16
- 239000005977 Ethylene Substances 0.000 title claims description 16
- 229910052751 metal Inorganic materials 0.000 claims abstract description 25
- 239000002184 metal Substances 0.000 claims abstract description 25
- 239000002253 acid Substances 0.000 claims abstract description 14
- 150000002148 esters Chemical class 0.000 claims abstract description 13
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims abstract description 10
- 125000004432 carbon atom Chemical group C* 0.000 claims abstract description 9
- 150000003839 salts Chemical class 0.000 claims abstract description 9
- 150000001735 carboxylic acids Chemical class 0.000 claims abstract description 8
- 238000004519 manufacturing process Methods 0.000 claims abstract description 6
- 238000006243 chemical reaction Methods 0.000 claims description 11
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 9
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 9
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 claims description 8
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 claims description 8
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims description 5
- -1 alkyl methacrylate Chemical compound 0.000 claims description 5
- 239000007864 aqueous solution Substances 0.000 claims description 5
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims description 4
- 229920000573 polyethylene Polymers 0.000 claims description 4
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 claims description 3
- 125000005250 alkyl acrylate group Chemical group 0.000 claims description 3
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 claims description 2
- 229910000000 metal hydroxide Inorganic materials 0.000 claims 1
- 150000004692 metal hydroxides Chemical class 0.000 claims 1
- 239000004711 α-olefin Substances 0.000 abstract description 6
- 239000000178 monomer Substances 0.000 description 13
- 238000006386 neutralization reaction Methods 0.000 description 9
- 239000002585 base Substances 0.000 description 6
- 229920001577 copolymer Polymers 0.000 description 6
- 150000002739 metals Chemical class 0.000 description 6
- 229920000642 polymer Polymers 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- 238000007127 saponification reaction Methods 0.000 description 3
- SOGAXMICEFXMKE-UHFFFAOYSA-N Butylmethacrylate Chemical compound CCCCOC(=O)C(C)=C SOGAXMICEFXMKE-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 229910052783 alkali metal Inorganic materials 0.000 description 2
- 150000001340 alkali metals Chemical class 0.000 description 2
- HUCVOHYBFXVBRW-UHFFFAOYSA-M caesium hydroxide Chemical compound [OH-].[Cs+] HUCVOHYBFXVBRW-UHFFFAOYSA-M 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- CPRMKOQKXYSDML-UHFFFAOYSA-M rubidium hydroxide Chemical compound [OH-].[Rb+] CPRMKOQKXYSDML-UHFFFAOYSA-M 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical compound CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 description 1
- 239000004831 Hot glue Substances 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 150000001252 acrylic acid derivatives Chemical class 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- RQPZNWPYLFFXCP-UHFFFAOYSA-L barium dihydroxide Chemical compound [OH-].[OH-].[Ba+2] RQPZNWPYLFFXCP-UHFFFAOYSA-L 0.000 description 1
- 238000010923 batch production Methods 0.000 description 1
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 1
- 229910052792 caesium Inorganic materials 0.000 description 1
- TVFDJXOCXUVLDH-UHFFFAOYSA-N caesium atom Chemical compound [Cs] TVFDJXOCXUVLDH-UHFFFAOYSA-N 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 125000004185 ester group Chemical group 0.000 description 1
- SUPCQIBBMFXVTL-UHFFFAOYSA-N ethyl 2-methylprop-2-enoate Chemical compound CCOC(=O)C(C)=C SUPCQIBBMFXVTL-UHFFFAOYSA-N 0.000 description 1
- 239000005043 ethylene-methyl acrylate Substances 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 1
- 239000000347 magnesium hydroxide Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- PNJWIWWMYCMZRO-UHFFFAOYSA-N pent‐4‐en‐2‐one Natural products CC(=O)CC=C PNJWIWWMYCMZRO-UHFFFAOYSA-N 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 239000007870 radical polymerization initiator Substances 0.000 description 1
- 238000010526 radical polymerization reaction Methods 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 229910052701 rubidium Inorganic materials 0.000 description 1
- IGLNJRXAVVLDKE-UHFFFAOYSA-N rubidium atom Chemical compound [Rb] IGLNJRXAVVLDKE-UHFFFAOYSA-N 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- UUCCCPNEFXQJEL-UHFFFAOYSA-L strontium dihydroxide Chemical compound [OH-].[OH-].[Sr+2] UUCCCPNEFXQJEL-UHFFFAOYSA-L 0.000 description 1
- 229910001866 strontium hydroxide Inorganic materials 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 229920006029 tetra-polymer Polymers 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Classifications
-
- 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
- C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F210/02—Ethene
-
- 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
- C08F8/00—Chemical modification by after-treatment
- C08F8/44—Preparation of metal salts or ammonium salts
Definitions
- the present invention relates to a process for the production of ionomers from ethylene terpolymers and in particular ethylene-alkyl acrylate- acrylic acid terpolymers.
- (meth)acrylate copolymers are recognized in the art. Such ionomers can be employed within a variety of environments. For example, they can be employed in place of traditional polyolefins within adhesive combinations such as hot melt adhesive combinations. Furthermore, such ionomers can be particularly useful in multilayer films as seal layers.
- U.S. Patent 3,970,626 to Hurst et al relates to a batch process for the production of ionomers.
- this process relates to the caustic hydrolysis of ethylene-(meth)acrylate copolymers using an excess of sodium hydroxide in an aqueous solution.
- such processes typically require long residence times, i.e., on the order of several hours, and yield a product in a form which requires further processing, i.e., an emulsion rather than a solid polymer.
- Patent 5,218,057 to Kurkov et al discloses a continuous process for the production of such ionomers within a reaction vessel, e.g., a reactive extruder.
- this method involves the saponification of ethylene-alkyl (meth)acrylate copolymers such as EMAC ® (an ethylene methacrylate copolymer product of Chevron Chemical Co.) with an aqueous solution of an alkali metal base under saponification reaction conditions within a reactive extruder.
- EMAC ® an ethylene methacrylate copolymer product of Chevron Chemical Co.
- the present invention is based on the ability to produce ionomers from an ethylene terpolymer by neutralization of at least a portion of the acidic components of the terpolymer with a metal-containing solution such as an alkali metal base.
- this process comprises contacting: (a) a terpolymer containing structural units produced from (i) ⁇ -olefins having from 2 to 8 carbon atoms; (ii) esters of alpha, beta-ethylenically-unsaturated carboxylic acids; and (iii) carboxylic acids with (b) an inorganic metal-containing base under conditions effective to convert at least a portion of the acid functionality to inorganic metal salts thereof.
- the present invention relates to ionomers produced by the inventive process.
- the present invention relates to a process for the neutralization of an ethylene terpolymer so as to produce an ionomer thereof.
- terpolymer can include three or more monomer constituents as well as substituted derivatives thereof.
- terpolymer as used herein is intended to refer to true interpolymers of ethylene and the other monomers, as well as blends of copolymers of ethylene and acid monomers, e.g., acrylic acid with copolymers of ethylene and ester monomers, e.g., acrylates.
- the preferred embodiments discuss "ethylene" terpolymers, as will be seen, the present invention also encompasses the use of polymers produced from other ⁇ -olefins.
- the terpolymers of the present invention include structural units produced from:
- alpha-olefins having from 2 to 8 carbon atoms
- esters of alpha, beta-ethylenically-unsaturated carboxylic acids and, (iii) carboxylic acids.
- Monomer (i) includes alpha-olefins having from 2 to 8 carbon atoms.
- Preferably monomer (i) comprises alpha-olefins having from 2 to 3 carbon atoms, and more preferably, monomer (i) is ethylene.
- Monomer (ii) comprises esters of ,j8-ethylenically-unsaturated carboxylic acids, preferably having from 4 to 22 carbon atoms. More preferably, monomer (ii) has from 4 to 13 carbon atoms, and still more preferably has from 4 to 8 carbon atoms. Examples of monomer (ii) include methyl acrylate, methyl methacrylate, ethyl acrylate, ethyl methacrylate, butyl acrylate, and butyl methacrylate. Methyl acrylate is the preferred monomer (ii).
- Monomer (iii) can comprise any carboxylic acid and is preferably an ⁇ ,j8-ethylenically unsaturated carboxylic acid such as those discussed above with respect to the esters of monomer (ii).
- carboxylic acids include acrylic acid and methacrylic acid.
- the combined ester and acid content in the terpolymer is in the range of 5 to 25% by weight and more preferably in the range of 10 to 20% by weight.
- terpolymers examples include terpolymers comprising from about 70 to 95% by weight of polymerized ethylene from about 2.5 to about 27.5 % by weight polymerized C, to C l9 , preferably, C t to C 5 , alkyl acrylate or methacrylate and about 2.5 to 27.5% by weight of polymerized acrylic acid or methacrylic acid.
- Exemplary terpolymers include ethylene-methyl acrylate-acrylic acid terpolymers, ethylene-methyl methacrylate-acrylic acid terpolymers, ethylene-methyl acrylate-methacrylic acid terpolymers, ethylene-ethyl acrylate-acrylic acid terpolymers, and ethylene-propylene-methyl acrylate- acrylic acid terpolymer. Ethylene-methyl acrylate-acrylic acid terpolymers are preferred.
- the ethylene polymers may comprise a wide range of melt indices generally between about 0.1 and 1000, more preferably about 1 to about 500 and still more preferably about 2.5 to about 10 g/lOmin.
- the ethylene terpolymers employed within the present invention may be produced by a technique recognized within the art, for example, free radical initiated processes such as those described within U.S. Patent 3,350,372 which is incorporated herein by reference in its entirety for all purposes.
- free radical initiated processes such as those described within U.S. Patent 3,350,372 which is incorporated herein by reference in its entirety for all purposes.
- such processes involve introducing ethylene, the ester, e.g., methyl acrylate, and the carboxylic acid into a high pressure reactor along with any one of a number of recognized free radical polymerization initiators, i.e., catalysts, suitable for producing the desired polymer.
- the process of the present invention comprises a neutralization of the terpolymer with an inorganic metal-containing base so as to convert at least a portion of the acid structural units to an inorganic metal salt thereof.
- the inorganic metal-containing base comprises a metal present in a solvent.
- the metal can comprise any metal which is capable of being effectively employed in a neutralization reaction so as to convert at least a portion of the acid functionality to a metal salt thereof.
- Suitable metals include Group IA metals, Group IIA metals, and transition metals. Specific examples of suitable metals include lithium, sodium, potassium, rubidium, cesium, calcium, magnesium, zinc, titanium, cobalt, nickel, and copper.
- the solvent can be any solvent which does not prevent this neutralization reaction from occurring.
- One suitable solvent is water.
- the base comprises an aqueous solution of an oxide of the Group IA and/or a hydroxide of the Group IA or Group IIA metals and in particular, the Group IA metals, discussed above.
- Specific examples of preferred Group IA and Group IIA hydroxides include LiOH, KOH, RbOH, CsOH, Mg(OH) 2 , Ca(OH) 2 , Sr(OH) 2 and Ba(OH) 2 with solutions of sodium hydroxide, lithium hydroxide, and potassium hydroxide being more preferred.
- the hydroxide is present within an aqueous solution at a concentration of from about 1 to about 50 weight % , preferably, about 5 to about 20 weight % .
- the neutralization reaction can occur under conditions which are effective in order to provide the conversion of at least a portion of the acid functionality to a metal salt thereof.
- the temperature should be sufficient to melt and process the terpolymer, e.g., provide effective mixing the balance of components, it can also be relatively mild, e.g., less than about 100°C.
- the process of the present invention can provide for the partial neutralization of the terpolymer, i.e., only a portion of the acid structural units are neutralized.
- the product in such a process is a quaternary polymer having four functionalities, e.g., the ethylene, the ester, the carboxylate salt and the carboxylic acid.
- the process of the present invention can provide for the complete neutralization, i.e., substantially all, if not all, of the acid functionalities are converted into metal salts.
- the product of such a process will be a terpolymer having three functionalities, i.e., the ethylene backbone, the ester, and the ionic metal-neutralized carboxylic acid.
- the process of the present invention can occur under batch or continuous reaction environments in any suitable reactor vessel. Typical batch reactors include autoclaves while typical continuous reactors include at least one extruding vessel, e.g., at least one reactive extruder. Preferably, the reaction is preformed continuously in a reactive extruder.
- a reactive extruder which is useful in producing compositions of this invention comprises an extruder having a terpolymer feed section, one or more reaction sections, a subsequent devolatilization section, and an extrusion section. Typically, these sections are separately jacketed to allow for heating or cooling within each section. These sections can also be vented with one or more vent ports per section to allow the escape of volatile components.
- the reactive extruder will also have optional means for introducing reactants into any reaction sections as well as means for mixing components in the reaction section(s) and means for conveying the components through the extruder.
- the means for mixing and conveying components to be reacted are screws.
- Reactive extruders can have a single screw or multiple screws. Each screw typically has a central shaft with a key-way or spline upon which mixing elements are secured.
- the reactive extruder may have either co- rotating or counter-rotating screws.
- a suitable reactive extruder is a Werner and Pfleiderer corrosion resistant ZSK-40 mm twin screw extruder.
- the process provides a heretofore unrecognized technique for providing a desired product in a more efficient and flexible manner.
- the ionomer produced by the inventive process has a number of advantages over those produced by typical saponification reactions. For example, because such ionomers can be produced under less severe processing conditions, e.g., lower temperatures, they can be subjected to less degradation and discoloration.
- the process of the present invention provides not only for these improved terpolymers but is also capable of providing tetrapolymers. That is, the process is capable of providing for partial neutralization of the acid groups and therefore an ionomer which contains not only the ester groups but also the acid group, which ionomer can have enhanced processability.
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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)
- General Chemical & Material Sciences (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
Cette invention se rapporte à un procédé servant à produire des ionomères contenant des unités structurelles à insaturation éthylénique, ce procédé consistant à mettre en contact: (a) un terpolymère contenant des unités structurelles produites à partir: (i) d'au moins une α-oléfine ayant 2 à 8 atomes de carbone; (ii) au moins un ester d'acides carboxyliques à insaturation alpha, bêta-éthylénique; et (iii) d'au moins un acide carboxylique; avec (b) une base contenant un métal inorganique dans des conditions propres à convertir au moins une partie des fonctions acides en sels de métal inorganique de ces fonctions.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/US1997/008937 WO1998052981A1 (fr) | 1997-05-19 | 1997-05-19 | Procede de production d'ionomeres au moyen de terpolymeres d'ethylene |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/US1997/008937 WO1998052981A1 (fr) | 1997-05-19 | 1997-05-19 | Procede de production d'ionomeres au moyen de terpolymeres d'ethylene |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1998052981A1 true WO1998052981A1 (fr) | 1998-11-26 |
Family
ID=22260965
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1997/008937 WO1998052981A1 (fr) | 1997-05-19 | 1997-05-19 | Procede de production d'ionomeres au moyen de terpolymeres d'ethylene |
Country Status (1)
Country | Link |
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WO (1) | WO1998052981A1 (fr) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7335424B2 (en) | 2001-03-29 | 2008-02-26 | Exxonmobil Chemical Patents Inc. | Ionomer laminates and articles formed from ionomer laminates |
US7405008B2 (en) | 2001-03-29 | 2008-07-29 | Exxonmobil Chemical Patents Inc. | Ionomer laminates and articles formed from ionomer laminates |
US7479327B2 (en) | 2003-05-27 | 2009-01-20 | Exxonmobil Chemical Patents Inc. | Tie-layer materials for use with ionomer-based films and sheets as skins on other materials |
US7544420B2 (en) | 2003-05-27 | 2009-06-09 | Exxonmobil Chemical Patents Inc. | Backing layers and substrates for articles formed from ionomer laminates |
US8076000B2 (en) | 2003-05-27 | 2011-12-13 | Exxonmobil Chemical Patents Inc. | Tie-layer materials for use with ionomer-based films and sheets as skins on other materials |
WO2013016398A1 (fr) | 2011-07-28 | 2013-01-31 | Dow Global Technologies Llc | Formulations de mélange polymère appropriées pour applications de cuir synthétique |
US8404773B2 (en) | 2008-03-17 | 2013-03-26 | Dow Global Technologies Llc | Coating composition, method of producing the same, articles made therefrom, and method of making such articles |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4990574A (en) * | 1988-03-02 | 1991-02-05 | Sumitomo Rubber Industries, Ltd. | Process for production of modified resin |
US5320905A (en) * | 1985-09-16 | 1994-06-14 | The Dow Chemical Company | Ionomers of ethylene/carboxylic acid copolymers |
-
1997
- 1997-05-19 WO PCT/US1997/008937 patent/WO1998052981A1/fr active Application Filing
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5320905A (en) * | 1985-09-16 | 1994-06-14 | The Dow Chemical Company | Ionomers of ethylene/carboxylic acid copolymers |
US4990574A (en) * | 1988-03-02 | 1991-02-05 | Sumitomo Rubber Industries, Ltd. | Process for production of modified resin |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7335424B2 (en) | 2001-03-29 | 2008-02-26 | Exxonmobil Chemical Patents Inc. | Ionomer laminates and articles formed from ionomer laminates |
US7405008B2 (en) | 2001-03-29 | 2008-07-29 | Exxonmobil Chemical Patents Inc. | Ionomer laminates and articles formed from ionomer laminates |
US7479327B2 (en) | 2003-05-27 | 2009-01-20 | Exxonmobil Chemical Patents Inc. | Tie-layer materials for use with ionomer-based films and sheets as skins on other materials |
US7544420B2 (en) | 2003-05-27 | 2009-06-09 | Exxonmobil Chemical Patents Inc. | Backing layers and substrates for articles formed from ionomer laminates |
US8076000B2 (en) | 2003-05-27 | 2011-12-13 | Exxonmobil Chemical Patents Inc. | Tie-layer materials for use with ionomer-based films and sheets as skins on other materials |
US8404773B2 (en) | 2008-03-17 | 2013-03-26 | Dow Global Technologies Llc | Coating composition, method of producing the same, articles made therefrom, and method of making such articles |
US8546477B2 (en) | 2008-03-17 | 2013-10-01 | Dow Global Technologies Llc | Coating composition, method of producing the same, articles made therefrom, and method of making such articles |
WO2013016398A1 (fr) | 2011-07-28 | 2013-01-31 | Dow Global Technologies Llc | Formulations de mélange polymère appropriées pour applications de cuir synthétique |
US9605377B2 (en) | 2011-07-28 | 2017-03-28 | Dow Global Technologies Llc | Polymeric blend formulations suitable for synthetic leather applications |
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