WO1995026367A1 - Elastomeres a double reseau obtenus a partir de reseau d'elastomere oriente - Google Patents
Elastomeres a double reseau obtenus a partir de reseau d'elastomere oriente Download PDFInfo
- Publication number
- WO1995026367A1 WO1995026367A1 PCT/US1995/003875 US9503875W WO9526367A1 WO 1995026367 A1 WO1995026367 A1 WO 1995026367A1 US 9503875 W US9503875 W US 9503875W WO 9526367 A1 WO9526367 A1 WO 9526367A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- elastomeric
- curing
- cross
- orientation
- strain
- Prior art date
Links
- 229920001971 elastomer Polymers 0.000 title claims abstract description 78
- 239000000806 elastomer Substances 0.000 title claims abstract description 46
- 238000000034 method Methods 0.000 claims abstract description 49
- 230000008569 process Effects 0.000 claims abstract description 28
- 239000013536 elastomeric material Substances 0.000 claims abstract description 25
- 238000002425 crystallisation Methods 0.000 claims abstract description 15
- 230000008025 crystallization Effects 0.000 claims abstract description 15
- 244000043261 Hevea brasiliensis Species 0.000 claims description 16
- 229920003052 natural elastomer Polymers 0.000 claims description 16
- 229920001194 natural rubber Polymers 0.000 claims description 16
- 230000002040 relaxant effect Effects 0.000 claims description 13
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 claims description 12
- 150000002978 peroxides Chemical class 0.000 claims description 10
- 239000000463 material Substances 0.000 claims description 9
- 229920000642 polymer Polymers 0.000 claims description 9
- 229920002857 polybutadiene Polymers 0.000 claims description 7
- 239000005062 Polybutadiene Substances 0.000 claims description 6
- 229920002367 Polyisobutene Polymers 0.000 claims description 6
- 229920001577 copolymer Polymers 0.000 claims description 6
- 229920003048 styrene butadiene rubber Polymers 0.000 claims description 6
- 239000002174 Styrene-butadiene Substances 0.000 claims description 5
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 4
- 238000010059 sulfur vulcanization Methods 0.000 claims description 4
- 229920003051 synthetic elastomer Polymers 0.000 claims description 4
- 239000005061 synthetic rubber Substances 0.000 claims description 4
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 claims description 3
- MTAZNLWOLGHBHU-UHFFFAOYSA-N butadiene-styrene rubber Chemical compound C=CC=C.C=CC1=CC=CC=C1 MTAZNLWOLGHBHU-UHFFFAOYSA-N 0.000 claims description 2
- 229920003193 cis-1,4-polybutadiene polymer Polymers 0.000 claims description 2
- 239000011115 styrene butadiene Substances 0.000 claims description 2
- 238000001723 curing Methods 0.000 description 32
- 239000005060 rubber Substances 0.000 description 32
- 238000004132 cross linking Methods 0.000 description 20
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 6
- 235000021355 Stearic acid Nutrition 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 3
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 3
- 230000005855 radiation Effects 0.000 description 3
- 239000008117 stearic acid Substances 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- 239000011787 zinc oxide Substances 0.000 description 3
- DMWVYCCGCQPJEA-UHFFFAOYSA-N 2,5-bis(tert-butylperoxy)-2,5-dimethylhexane Chemical compound CC(C)(C)OOC(C)(C)CCC(C)(C)OOC(C)(C)C DMWVYCCGCQPJEA-UHFFFAOYSA-N 0.000 description 2
- 241001441571 Hiodontidae Species 0.000 description 2
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 2
- 239000003963 antioxidant agent Substances 0.000 description 2
- 230000003078 antioxidant effect Effects 0.000 description 2
- 235000006708 antioxidants Nutrition 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 229920001084 poly(chloroprene) Polymers 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- ZNRLMGFXSPUZNR-UHFFFAOYSA-N 2,2,4-trimethyl-1h-quinoline Chemical compound C1=CC=C2C(C)=CC(C)(C)NC2=C1 ZNRLMGFXSPUZNR-UHFFFAOYSA-N 0.000 description 1
- XMNIXWIUMCBBBL-UHFFFAOYSA-N 2-(2-phenylpropan-2-ylperoxy)propan-2-ylbenzene Chemical compound C=1C=CC=CC=1C(C)(C)OOC(C)(C)C1=CC=CC=C1 XMNIXWIUMCBBBL-UHFFFAOYSA-N 0.000 description 1
- BWGNESOTFCXPMA-UHFFFAOYSA-N Dihydrogen disulfide Chemical group SS BWGNESOTFCXPMA-UHFFFAOYSA-N 0.000 description 1
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical group CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 1
- 229920004941 NATSYN® 2200 Polymers 0.000 description 1
- 229920000459 Nitrile rubber Polymers 0.000 description 1
- 229920005549 butyl rubber Polymers 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- YACLQRRMGMJLJV-UHFFFAOYSA-N chloroprene Chemical compound ClC(=C)C=C YACLQRRMGMJLJV-UHFFFAOYSA-N 0.000 description 1
- 230000001427 coherent effect Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- AFZSMODLJJCVPP-UHFFFAOYSA-N dibenzothiazol-2-yl disulfide Chemical compound C1=CC=C2SC(SSC=3SC4=CC=CC=C4N=3)=NC2=C1 AFZSMODLJJCVPP-UHFFFAOYSA-N 0.000 description 1
- -1 dicumyl peroxide) Chemical class 0.000 description 1
- 150000001993 dienes Chemical class 0.000 description 1
- 230000005251 gamma ray Effects 0.000 description 1
- 230000009477 glass transition Effects 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 125000004573 morpholin-4-yl group Chemical group N1(CCOCC1)* 0.000 description 1
- IUJLOAKJZQBENM-UHFFFAOYSA-N n-(1,3-benzothiazol-2-ylsulfanyl)-2-methylpropan-2-amine Chemical compound C1=CC=C2SC(SNC(C)(C)C)=NC2=C1 IUJLOAKJZQBENM-UHFFFAOYSA-N 0.000 description 1
- DZCCLNYLUGNUKQ-UHFFFAOYSA-N n-(4-nitrosophenyl)hydroxylamine Chemical compound ONC1=CC=C(N=O)C=C1 DZCCLNYLUGNUKQ-UHFFFAOYSA-N 0.000 description 1
- 150000001451 organic peroxides Chemical class 0.000 description 1
- PMJHHCWVYXUKFD-UHFFFAOYSA-N penta-1,3-diene Chemical compound CC=CC=C PMJHHCWVYXUKFD-UHFFFAOYSA-N 0.000 description 1
- 229920001568 phenolic resin Polymers 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920001195 polyisoprene Polymers 0.000 description 1
- 238000003847 radiation curing Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 238000004073 vulcanization Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/24—Crosslinking, e.g. vulcanising, of macromolecules
- C08J3/244—Stepwise homogeneous crosslinking of one polymer with one crosslinking system, e.g. partial curing
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2321/00—Characterised by the use of unspecified rubbers
Definitions
- the present invention relates to the general area of modifying the structure of elastomers in order to obtain improved mechanical properties. More particularly, the present invention is directed to processes for modifying elastomeric structures to improve mechanical properties thereof, such as modulus, that involve subjecting elastomeric material to multiple curing steps that are controlled so as to introduce and apportion cross-links in each curing step to result in predetermined proportions of cross-link densities in the resultant elastomeric material as a result of the respective curing steps.
- the present invention is directed to processes for modifying elastomeric materials that involve subjecting elastomeric material to an initial curing step under controlled conditions effective to result in a pre-cured elastomeric material comprising a first network having a number of cross-links within the range of about 5% to about 35% of the total cross-links of the resultant elastomeric material that has been subjected to another curing step while being subjected to an orientation strain under conditions effective to result in an elastomeric double network having desired total cross ⁇ links.
- U.S. Patent No. 2,488,188, BALDWIN discloses that it is advantageous to first cure rubber slightly, then stretch it, followed by finish-curing the rubber while the rubber is in the stretched state to improve certain properties, e.g., tensile strength, elongation, elasticity, and elastic limit. It is disclosed that the invention applies to the curing of various types of natural rubber and unsaturated synthetic rubber polymers, such as chlorobutadiene polymers, copolymers of butadiene and acrylonitrile, copolymers of isobutylene with various diolefins, such as butadiene, isoprene, methyl butadiene, and the like.
- Fig. 1 is graph showing the ratio of the double-to-single network moduli at various residual strains.
- Fig. 2 is a graph showing the dependence of residual strain on stress strain isotherms.
- Fig. 3 is a graph showing tensile strength measured for natural rubber double network samples of various residual strains.
- Fig. 4 is a graph showing theoretical ratios of double-to- single network moduli at various residual strains using consecutive equations of Mooney and Rivlin.
- the conditions of curing such as cure times and temperatures, are adjusted and controlled so that about 5% to about 35%, and more typically between about 5% to about 10%, of the total cross ⁇ links in the resultant double network elastomer are produced during the initial cure.
- the pre-cured elastomer is stretched or strained during an orientation to at least 200% elongation, and more typically 600% elongation, and subjected to additional curing under conditions effective to produce a resultant elastomer double network having a desired cross-link density wherein between about 65% to about 95%, and more typically between about 90% to about 95%, of the total cross ⁇ links in the resultant elastomer double network are introduced during additional curing.
- pre-cured sheets of a rubber such as natural rubber (NR) , polybutadiene (PBD) , and styrene-butadiene rubber (SBR)
- NR natural rubber
- PBD polybutadiene
- SBR styrene-butadiene rubber
- the final dimensions of the article reflect the relative cross-link densities arising from the two acts of curing, i.e., pre-curing and additional curing, along with the orientation during the second or additional cure.
- the modulus of the double network elastomer produced in accordance with the present invention is higher than a conventional rubber or single network elastomer having the same total cross-link density.
- the failure properties of the double network elastomer of the present invention are equivalent to the conventional rubber or single network elastomer when no crystallization takes place.
- the resistance to failure of the double network elastomer of the present invention is better than that of the conventional rubber or single network elastomer having the same total cross-link density.
- the present invention enables higher modulus to be realized while simultaneously maintaining or improving failure performance.
- (iii) maintains or improves failure properties of elastomers.
- rubber is cured while unrelaxed, e.g., while stretched, such that the subsequent state of elastic equilibrium is shifted away from zero strain.
- the resultant double network elastomer structure provides thermodynamically stable orientation, which significantly alters the mechanical properties of an elastomer.
- the failure properties are maintained by keeping a constant cross-link density, while the modulus is enhanced by double network formation.
- an enhancement of strain crystallizability can be obtained by virtue of the double network process. This leads to significantly better failure properties, since the strain crystallization is the primary mechanism for failure resistance.
- the process of the present invention involves the following steps: a) curing elastomeric material under conditions of substantially zero strain, time and temperature to result in a pre-cured elastomeric network comprising less than about 40%, and more typically less than about 35%, of total cross-links that are present in the resultant elastomeric double network structure; b) subjecting the pre-cured elastomeric material to an orientation technique to result in an oriented elastomeric material having at least about 200% elongation; and c) curing the oriented elastomeric material while maintaining such orientation under conditions effective to result in a resultant elastomeric structure comprising a predetermined cross-link density of at least about 60%, and more typically at least about 65%, of total cross-links present in the resultant elastomeric double network structure, wherein the resultant elastomeric double network structure exhibits enhanced modulus.
- the cure times and temperatures are adjusted and controlled so that most typically between about 5% to about 35%, and most often between about 5% to about 10%, of the total cross-links of the resultant elastomeric double network structure are produced during initial cure at zero strain.
- the pre-cured elastomer is stretched during an orientation to at least about 200% elongation, and more typically 600% elongation, and cured to produce a resultant elastomer double network having between about 65% to about 95% and more typically between about 90% to about 95% of the total cross-links.
- conditions during the curing steps are effective to result in magnitude of orientation sufficient to result in enhanced modulus.
- suitable methods of cross-linking include essentially all conventional curing methods, i.e., sulfur vulcanization, efficient vulcanization
- elastomers include: for neoprenes, metal oxides; phenolformaldehyde resins for butyl rubber; and for butyl and other unsaturated rubbers, p-benzoquinone dioxime.
- achieving a desired proportioning of the total cross-link density is accomplished in different manners depending on the particular method of cross-linking.
- time and temperature are the primary variables used to control the cross-link apportionment. Radiation curing would rely on dose,
- curing systems i.e., radiation intensity and exposure time.
- curing systems selected from the group consisting of sulfur vulcanization, peroxide curing, and radiative curing.
- Sulfur vulcanization typically has two stages.
- the first stage referred to as the induction or scorch period, involves the curing agents reacting with themselves prior to actual cross-linking reaction.
- the time of the second stage, where cross-links are actually formed is important.
- the length of time for each stage of the process is dependent on the temperature and the amount and type of curatives used.
- the scorch period at a given cure temperature, it is possible for the first cross-link density of a soluble network rubber to have a smaller percentage of the total cross-links even while experiencing a longer cure time than the second cross-linking period.
- Peroxide curing involves the formation of thermal decomposition of an organic peroxide. These react with the elastomer to produce polymer radicals which combine to form a cross-link. Therefore, the rate of cross-linking is dependent on the rates of peroxide decomposition and polymer radical production.
- Radiative puring typically also proceeds via radical mechanisms.
- the polymer radicals produced through the use of energizing radiation combine to produce a cross-link.
- the number of cross-links produced by this technique is a function of the duration and intensity of radiation used.
- orientation is accomplished using orientation techniques.
- typical orientation techniques include those selected from the group of orientation procedures comprising uniaxial extension, biaxial extension, simple shear, planar shear, and inflation.
- the strains at which the second cross-linking is to be introduced into the elastomeric double network is specified to be in the range from 20% to 600% elongation. Below 20% elongation, there are no beneficial effects on properties as compared to conventional rubbers. More typically, however, the lower limit of elongation is about 200% elongation.
- the upper limit for the cross-linking strain is in principle the material's maximum extensibility; however, in practice this yields an overly large "rejection rate", that is, many samples fail during their production. For practical reasons, therefore, the strain during cross-linking is more typically limited to not greater than 600%.
- the number of cross-links generated in the first network is specified to be in the range from about 5% to about 35% of the total cross-links introduced into the resultant double network material. If less than 5% of the total cross-links ultimately present in the final resultant double network are introduced during the initial stage of cross-linking in forming the first network, then the material will not have the coherent strength to survive the second stage of the cross-linking process. No beneficial effects are realized in double network material if the number of cross-links introduced into the first network exceeds about 35 % of the total number of cross-links in the resultant double network elastomer.
- conventional procedures for the measurement of cross-link density are used.
- conventional cross-link measurement procedures include (i) determination of the degree of swelling in a solvent, and (ii) determining the equilibrium (fully-relaxed) modulus.
- suitable elastomeric material includes members selected from the group consisting of elastomers not capable of strain induced crystallization, and elastomers capable of strain-induced crystallization, wherein elastomeric materials not capable of strain-induced crystallization comprise at least one member selected from the group consisting of unsaturated synthetic rubber polymers, copolymers of butadiene and styrene, copolymers of butadiene and acrylonitrile, and elastomers capable of strain induced crystallization include members selected from the group consisting of natural rubber (NR) polybutadiene (PBD) , styrene butadiene (SBR), polyisobutylene (PIB), and high cis 1,4 - polybutadiene (high cis 1,4 - PBR) .
- NR natural rubber
- PBD polybutadiene
- SBR styrene butadiene
- PIB polyisobutylene
- the conditions during curing are sufficient to maintain a constant cross link density in said double network elastomer while the modulus is enhanced, and while at least failure performance of the elastomeric structure is maintained.
- a rubber incapable of strain crystallizing by virtue of its chemical structure, such as SBR, nitrile rubber, and the like, compared in a fully relaxing deformation cycle to a non-relaxing deformation cycle.
- a rubber capable of strain crystallization e.g., natural rubber, neoprene, and the like, will have a markedly longer fatigue life for non-relaxing deformations as compared to fully relaxing deformations.
- the present invention in part, is based on the discovery that one can take advantage of double network elastomers and attain non-relaxing deformation levels of performance even when they are subjected to fully relaxing deformation cycles. This is a result of the intrinsic orientation of the double network rubber. Accordingly, elastomeric or rubber parts and devices may be designed and developed without the constraint of having to avoid fully relaxing deformations. Furthermore, applications for which fully relaxing conditions are unavoidable can obviously benefit from the use of double network technology in accordance with the present invention.
- Example I The following example was conducted to demonstrate aspects of the present invention.
- Fig. 1 the ratio of double-to single-network moduli has been plotted at various residual strains. The data is taken from Fig. 2 at an extension ratio of 1.1. In Fig. 2, dependence of residual strain on stress-strain isotherms is
- the double-network rubbers and the single- network rubber i.e., residual strain of 1.0 have the same total cross-link density.
- Fig. 3 the tensile strength measured for natural rubber double-networks samples of various residual strains has been plotted on the graph. Also shown is the tensile strength of a single-network rubber (residual strain of 1.0) having the same total cross-link density.
- the double-networks posses an elevated modulus while maintaining strength.
- Second Cure 90 minutes at 160°C while strained to indicated level.
- Example II The following example was conducted to demonstrate aspects of the present invention. In this Example II, unlike Example I, the cure distribution was not weighted towards the second network.
- Example III The following example was conducted to demonstrate aspects of the present invention using a: Sulfurless Cure System. Natural Rubber 100 parts N2 34 Black 55 parts
- First Cure 15 minutes at 145°C
- Second Cure Stretch to 400% the 32 minutes at 145 ⁇ C
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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)
- Tires In General (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Un procédé permettant de modifier des structures élastomères et d'améliorer des propriétés mécaniques comprend plusieurs étapes. On applique tout d'abord une technique d'orientation à un matériau élastomère précuit afin d'obtenir un matériau élastomère orienté; on cuit ensuite ce matériau élastomère orienté tout en maintenant son orientation dans des conditions permettant d'obtenir une structure élastomère présentant une densité de réticulation prédéterminée et un module amélioré, l'orientation étant suffisamment importante pour entraîner une amélioration du module. Généralement, les techniques d'orientation utilisées peuvent être les suivantes: étirage uniaxial, étirage biaxial, cisaillement simple, cisaillement planaire et gonflement. Le matériau élastomère est capable ou non de cristallisation induite par déformation. On obtient l'amélioration du module en maintenant au moins les propriétés de rupture de la structure élastomère. Les conditions pendant la cuisson suffisent à maintenir une densité de réticulation constante dans l'élastomère à double réseau et à améliorer le module.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US21931894A | 1994-03-29 | 1994-03-29 | |
| US08/219,318 | 1994-03-29 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1995026367A1 true WO1995026367A1 (fr) | 1995-10-05 |
Family
ID=22818798
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US1995/003875 WO1995026367A1 (fr) | 1994-03-29 | 1995-03-29 | Elastomeres a double reseau obtenus a partir de reseau d'elastomere oriente |
Country Status (1)
| Country | Link |
|---|---|
| WO (1) | WO1995026367A1 (fr) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8227551B2 (en) | 2008-11-10 | 2012-07-24 | The University Of Massachusetts | Polymeric compositions, methods of manufacture thereof and articles comprising the same |
| US10336018B2 (en) * | 2016-09-28 | 2019-07-02 | Acushnet Company | Method of making a golf ball incorporating at least one elongated thermoset layer |
| US10465070B2 (en) * | 2016-09-28 | 2019-11-05 | Acushnet Company | Golf balls incorporating double network cross-linked compositions comprising a base thermoset composition |
| US10465072B2 (en) * | 2016-09-28 | 2019-11-05 | Acushnet Company | Golf balls incorporating double network cross-linked compositions comprising a base thermoplastic |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2488112A (en) * | 1945-12-29 | 1949-11-15 | Standard Oil Dev Co | Process of curing isobutyleneisoprene copolymers |
| US3684782A (en) * | 1967-09-12 | 1972-08-15 | Paolo Longi | Manufactured shaped articles of unsaturated olefinic copolymers |
| US4740335A (en) * | 1985-08-10 | 1988-04-26 | Firma Carl Freudenberg | Process for producing a deep-drawn article from a partially-crystalline polymeric material |
-
1995
- 1995-03-29 WO PCT/US1995/003875 patent/WO1995026367A1/fr active Application Filing
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2488112A (en) * | 1945-12-29 | 1949-11-15 | Standard Oil Dev Co | Process of curing isobutyleneisoprene copolymers |
| US3684782A (en) * | 1967-09-12 | 1972-08-15 | Paolo Longi | Manufactured shaped articles of unsaturated olefinic copolymers |
| US4740335A (en) * | 1985-08-10 | 1988-04-26 | Firma Carl Freudenberg | Process for producing a deep-drawn article from a partially-crystalline polymeric material |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8227551B2 (en) | 2008-11-10 | 2012-07-24 | The University Of Massachusetts | Polymeric compositions, methods of manufacture thereof and articles comprising the same |
| US10336018B2 (en) * | 2016-09-28 | 2019-07-02 | Acushnet Company | Method of making a golf ball incorporating at least one elongated thermoset layer |
| US10465070B2 (en) * | 2016-09-28 | 2019-11-05 | Acushnet Company | Golf balls incorporating double network cross-linked compositions comprising a base thermoset composition |
| US10465072B2 (en) * | 2016-09-28 | 2019-11-05 | Acushnet Company | Golf balls incorporating double network cross-linked compositions comprising a base thermoplastic |
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