WO2004106386A1 - Kautschukartige hydrierte vinyl-polybutadiene - Google Patents
Kautschukartige hydrierte vinyl-polybutadiene Download PDFInfo
- Publication number
- WO2004106386A1 WO2004106386A1 PCT/EP2004/005385 EP2004005385W WO2004106386A1 WO 2004106386 A1 WO2004106386 A1 WO 2004106386A1 EP 2004005385 W EP2004005385 W EP 2004005385W WO 2004106386 A1 WO2004106386 A1 WO 2004106386A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- vinyl
- hydrogenation
- units
- formula
- hydrogenated
- Prior art date
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60C—VEHICLE TYRES; TYRE INFLATION; TYRE CHANGING; CONNECTING VALVES TO INFLATABLE ELASTIC BODIES IN GENERAL; DEVICES OR ARRANGEMENTS RELATED TO TYRES
- B60C1/00—Tyres characterised by the chemical composition or the physical arrangement or mixture of the composition
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08C—TREATMENT OR CHEMICAL MODIFICATION OF RUBBERS
- C08C19/00—Chemical modification of rubber
- C08C19/02—Hydrogenation
Definitions
- the present invention relates to rubber-like hydrogenated vinyl polybutadienes with degrees of hydrogenation of 20 to 100%, which are prepared in a known manner by hydrogenation of vinyl polybutadienes.
- the hydrogenated vinyl polybutadienes according to the invention are distinguished by low glass transition temperatures and by low melting enthalpies.
- the hydrogenated vinyl polybutadienes according to the invention are very resistant to aging and have a high elasticity even at low temperatures. They are therefore outstandingly suitable for the production of all kinds of rubber moldings, such as technical rubber articles as well as tires and tire components that require good aging resistance and good elasticity at low temperatures, and for the rubber modification of thermoplastics and thermosets.
- Hydrogenated polybutadienes with a high vinyl content of 85 to 100% are known from European patent application EP-A 0 024 315.
- the hydrogenated vinyl-polybutadienes described there are distinguished by a high ozone resistance, but have the disadvantage that the elasticity of the products at lower temperatures leaves something to be desired due to the higher glass transition temperatures and melting enthalpies.
- hydrogenated polybutadienes with a vinyl content of> 20% by weight and less than 40% by weight and a degree of hydrogenation of 85 and greater are known from European patent application EP-A 1 258 498.
- the hydrogenated polymers described there have a high degree of crystallization with good mechanical properties and good heat and weather resistance, but have the disadvantage that the elasticity, due to the high crystal character, leaves something to be desired, particularly at low temperatures.
- US Pat. No. 4,025,478 discloses hot melt adhesive preparations based on hydrogenated vinyl polybutadiene, the vinyl content of which is 50 to 95%, the vinyl content being able to be adjusted to a double bond content of less than 15%, preferably less than 10%, by hydrogenation.
- the hydrogenated vinyl polybutadienes must have a Mooney viscosity of ⁇ 10.
- lubricant compositions which, inter alia, contain a hydrogenated polybutadiene as a component in a smaller amount, the has a weight in the range of 20,000 to 300,000 and has a vinyl content of 65 to 85%. The degree of hydrogenation of these products is 75 to 100%.
- the hydrogenated vinyl polybutadienes should have a certain molecular weight range which is generally from 30,000 to 200,000.
- these molecular weights or the associated Mooney viscosities are too low to obtain tires or tire components with good physical properties.
- the hydrogenated polyvinyl butadienes according to the invention are suitable for improving the impact resistance of thermoplastics when they are mixed with the hydrogenated poly vinyl butadienes according to the invention.
- the present invention therefore relates to hydrogenated vinyl polybutadienes with degrees of hydrogenation of 20 to 100%, Mooney viscosities in the range from 10 to 150 Mooney units (ML 1 + 4/100 ° C.), glass transition temperatures (T g ) of ⁇ - 57 ° C and enthalpy of fusion ( ⁇ H) ⁇ 30 J / g, which have a microstructure of
- hydrogenated vinyl polybutadienes An exception to the hydrogenated vinyl polybutadienes according to the invention is a hydrogenated vinyl polybutadiene with a trans content of 4.7%, a vinyl content of 0.2%, a Mooney viscosity of 27 and a molecular weight ratio M w according to US Pat. No. 4,025,478 / M n x 10 "3 of 291/96 as disclosed in Table 1 under No. 3.
- Preferred according to the invention are hydrogenated vinyl polybuatienes which have a degree of hydrogenation of 20 to 100% and Mooney viscosities in the range from 10 to 150, glass transition temperatures of ⁇ -80 ° C. and melting enthalpies of 0 to 30 J / g and have a microstructure of
- the hydrogenated vinyl polybutadienes according to the invention have molecular weights (Mn) in the range from 20,000 to 500,000, preferably 60,000 to 300,000.
- the molecular weight ratio M w / M n has values in the range from 1 to 20, preferably 1 to 10.
- the hydrogenated vinyl polybutadienes according to the invention of the above-mentioned specification are obtained in a known manner by hydrogenation of corresponding vinyl polybutadienes which have a vinyl content of 40 to 64, preferably 45 to 60% by weight and a 1,4-butenyl content of 36 to 60, preferably 40 to 55% by weight.
- the vinyl polybutadienes suitable as starting products for the hydrogenation are known in a known manner by Ziegler-Natta polymerization or by ionic polymerization in suitable solvents and with the addition of known reagents for adjusting the vinyl content and by adding appropriate regulators and coupling agents for adjusting the molecular weight and the molecular weight distribution.
- the suitable selection of the initiators for the polymerization, of the solvent, of the molecular weight regulator and of the reagents for adjusting the vinyl content can give vinyl-polybutadienes which have the aforementioned vinyl content and butenyl content and a glass transition temperature of ⁇ -80 ° C., preferably ⁇ -90 ° C, enthalpies of fusion from 0 to 40 J / g, preferably 0 to 30 J / g and Mooney viscosities ML1 + 4 (100 ° C) from 10 to 150 Mooney units, preferably 10 to 120 Mooney units.
- a preferred embodiment for the production of vinyl polybutadienes with the above-mentioned physical parameters is accomplished, for example, by the polymerization of butadiene in the presence of butyllithium as the initiator and in the presence of cyclohexane as the solvent.
- the amount of initiator used is about 0.05 to 250 milliequivalents of metal, based on 100 g of butadiene used.
- the vinyl content of approx. 10 to 12% which occurs in the anionic polymerization of butadiene in suitable nonpolar solvents is not sufficient for the preparation of the polymers according to the invention, it is necessary to add the desired vinyl content suitable additives or rendomizers.
- suitable additives or randomizers are also known. Examples include amine compounds (eg US Pat. No. 3,985,829), ethers or the alcoholates of alkali metals. In this connection, reference is made, for example, to DE-A 10 217 800.
- the reagents for adjusting the vinyl content are usually used in molar ratios of 1: 1 to 80: 1, preferably 1: 1 to 40: 1 (additive / initiator).
- a preferred regulator is 1,2-butadiene.
- Preferred couplers are derived from silicon and tin compounds and are described, for example, in HLHsieh and R. Quirk “Anionic Polymerization, Principles and Practical Applications” Marcel Dekker Inc. New York, Basel, 1966, pages 197-235. Also others Coupling agents such as multivinyl compounds, for example divinylbenzene, are known (for example US Pat. No. 4,107,236).
- the polymerization reaction is carried out under inert conditions (exclusion of water, oxygen and carbon dioxide) in order to avoid deactivation of the initiator and / or of the living polymers.
- Polymerization temperatures of approximately -30 to 180 ° C. and reaction times of approximately 0.1 to 10 hours are common.
- the polymerization can be carried out either batchwise or continuously.
- the pressure during the polymerization is set in the range from approximately 0.1 MPa to 5 MPa.
- the polymerization conversions are around 50 to 100%.
- the polymerization is stopped by additives such as water, alcohols, phenols and / or acids.
- additives such as water, alcohols, phenols and / or acids.
- the polymerization is preferably not stopped, since the amount of hydrogenation catalyst required can be minimized in this way.
- Unreacted monomer is removed from the reaction mixture before the hydrogenation reaction.
- the hydrogenation is carried out “in situ”, it is preferred not to use water vapor for this, but rather to “flash” unreacted butadiene without first cooling the reaction mixture.
- the hydrogenation of the vinyl polybutadiene obtained was also carried out in a known manner using the known hydrogenation catalysts.
- the catalysts are known to the person skilled in the art and are described for example in US-A 3113986, US-A 3333024, US-A 3700633, US-A 4107236, US-A 3700633, US-A 3595942, 4028485, 3135716, 3150209, 3496154, 3498960, 4145298, 4238202, 3231635, 3265765, 3322856, 5030779, 3541064, 3644588, FR-A 1581146, 2393608, WO-A 9314130.
- the hydrogenation is preferably carried out with a nickel salt in combination with an aluminum alkyl (see here e.g. EP-A 1 258 498).
- Ni-n-octanoate Ni-acetylacetonate, Ni-2-ethylhexanoate and / or Ni-versatate.
- Aluminum alkyls are, for example: triisobutyl aluminum, trimethyl aluminum, Triethyl aluminum and / or tri-n-propyl aluminum. Triethyl aluminum and Ni-n-octanoate are preferred.
- the molar ratio of Al alkyl to Ni salt is approximately 1: 1 to 10: 1, preferably 2: 1 to 5: 1.
- the hydrogenation is carried out at temperatures of approximately 50 to 120 ° C. and a hydrogenation pressure of approximately 1 atm to 100 atm.
- the hydrogenated polymers are worked up in a customary manner by first separating off the hydrogenation catalysts in a suitable manner and isolating the hydrogenation product by removing the solvent used.
- the hydrogenation catalyst - in the present case nickel salt in combination with an aluminum alkyl - is removed from the hydrogenation solution by treating the hydrogenation solution with a suitable complexing agent and an oxidizing agent.
- the nickel formed during the hydrogenation of the vinyl polybutadiene is oxidized and brought into a soluble form with the complexing agent.
- the resulting nickel complex is then washed out of the hydrogenation solution with water.
- the nickel is removed from the hydrogenation solution by a so-called stripping process.
- a complexing agent is added to the hydrogenation solution and stripped with steam under oxidative conditions.
- Nitrilotriacetic acid, ethylenediaminetetraacetic acid, oxalic acid and or or citric acid, preferably citric acid, are suitable as complexing agents for the nickel formed.
- the amount of complexing agents is approximately 0.01 g to 3 g, based on 100 g of polymer.
- the amount of nickel remaining in the polymer depends, among other things. on the amount of catalyst used, the concentration of the polymer solution, the oxidizing agent and the type and amount of the complexing agent.
- Both air and pure oxygen can serve as the oxidizing agent.
- additives such as anti-aging agents or vulcanization aids or stretching oils
- the known additives are used in the usual amounts for this.
- the amount of the additives depends on the intended use of the hydrogenated vinyl-polybutadienes obtained.
- BR polybutadiene
- SBR Styrene / butadiene rubber
- DR butyl rubber
- EPM and EPDM hydrogenated nitrile rubber
- HNBR hydrogenated nitrile rubber
- CR polychloroprene
- NBR nitrile rubber
- BVM Ethylene / vinyl acetate copolymers
- CM and CSM chlorinated or chlorosulfonated polyethylene
- the respective mixing ratio of the rubbers to one another can easily be determined by preliminary tests and depends on the later intended use of the hydrogenated vinyl-polybutadienes according to the invention.
- Another object of the present invention is the use of the hydrogenated vinyl polybutadienes according to the invention with the physical properties and microstructure described above for the production of moldings of all kinds, in particular for the production of tires and tire components such as tire treads and tire sidewalls.
- technical rubber articles e.g. Hoses and sealing rings are made from the elastic, hydrogenated vinyl polybutadienes according to the invention.
- the hydrogenated vinyl polybutadienes according to the invention can also be mixed with thermoplastics or thermosets, for example to increase the impact resistance of these polymers.
- the thermoplastics used for this are: styrene / acrylonitrile copolymers, polybutylene terephthalate, polyethylene terephthalate; Polyoxymethylene, polystyrene, polycarbonate and polyvinyl chloride.
- the following thermosets can be used: Unsaturated polyester resins, epoxy resins as well as phenol / formaldehyde and melamine / formaldehyde resins.
- thermoplastics to the hydrogenated vinyl polybutadienes used also depends on the later intended use of these thermoplastics. It can therefore easily be determined by appropriate preliminary tests. - ⁇ -
- the polymerization of butadiene is carried out using n-butyllithium as the polymerization catalyst and cyclohexane as the solvent.
- the vinyl contents are adjusted by adding tetramethylethylenediamine (TMEDA) and t-butoxyethoxyethane (BEE) and by varying the polymerization temperature.
- TMEDA tetramethylethylenediamine
- BEE t-butoxyethoxyethane
- the polymerizations were carried out in a 1.7 liter steel reactor. For this purpose, 2/3 of the empty reactor was filled with dry cyclohexane under protective gas. Then butadiene was metered in and a butadiene concentration of 12 to 13% by weight in cyclohexane was set.
- the randomizers TMEDA or BEE were then added, the vinyl content being controlled by varying the molar ratio of randomizer / BuLi (see Tables 2 and 3). After the addition of the randomizer, BuLi was added in a concentration of 1 to 2 mmol Li to 100 g monomer (see Table 2). The polymerization was at 30 ° C and at
- the vinyl content, the degree of hydrogenation and the remaining microstructure were determined by ⁇ -NMR spectroscopy in CDC1 3 .
- Tg glass transition temperature
- the vinyl content depends on the polymerization temperature and the molar ratio Bu-Li / TMEDA (Tab. 1) and the molar ratio BuLi / BEE (Tab. 2).
- the hydrogenation of vinyl polybutadiene was carried out using a hydrogenation catalyst based on Ni octanoate [Ni (Oct) 2 ] and triethyl aluminum (TEA).
- the hydrogenation catalyst was preformed from Ni (Oct) 2 and TEA in a 25 ml Schlenck vessel under argon.
- the Schlenk vessel was filled with 2-5 ml of dry cyclohexane, then 0.7-1.0 ml of TEA was added (corresponding to the amount of polymer present in the reactor).
- a 10% solution of Ni (Oct) 2 in cyclohexane was added dropwise at about 15 ° C. while stirring and cooling.
- the catalyst solution was freshly prepared in each case and used immediately after the preparation.
- the vinyl polybutadiene was isolated from the solution, as described above, after the end of the polymerization, an aliquot was characterized and the remaining amount of the vinyl polybutadiene was dissolved and hydrogenated in cyclohexane.
- Vulkanox BKF A solution of Vulkanox BKF is added to the samples, as described for the production of vinyl-polybutadiene samples, ethanol precipitated, dried and characterized.
- the hydrogenation was complete after about 2 hours, recognizable from the fact that the polymer solution no longer absorbed hydrogen.
- the amount of residual hydrogen remaining in the reactor and in the polymer solution was removed by introducing argon to a pressure of 3 bar and then releasing the pressure, this procedure being repeated three times.
- the degrees of hydrogenation were determined by H-NMR.
- the samples were also characterized by means of DSC in order to determine glass transition temperatures (Tg), melting temperatures (Tm) and melting enthalpies (DH).
- BuLi is the polymerization catalyst
- the vinyl content is determined by -NMR c) polymerization temperature.
- Tg (DSC) is the glass temperature determined with DSC.
- the hydrogenation catalyst is produced in the hydrogenation reactor without separate preforming.
- the catalyst components TEA, Ni (Oct) 2 are gradually added directly to the hydrogenation reactor after every 10 minutes.
- the hydrogenation catalyst is produced in the hydrogenation reactor.
- TEA is added first, followed by Ni (Oct) 2 .
- Ni (Oct) 2 is added after the addition of Ni (Oct) 2 .
- the mixture is stirred for an hour before the addition of hydrogen.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002524667A CA2524667A1 (en) | 2003-05-30 | 2004-05-19 | Rubber-type hydrogenated vinyl polybutadienes |
EP04733789A EP1633789A1 (de) | 2003-05-30 | 2004-05-19 | Kautschukartige hydrierte vinyl-polybutadiene |
BRPI0410882-5A BRPI0410882B1 (pt) | 2003-05-30 | 2004-05-19 | Vinil-polibutadienos hidrogenados tipo borracha , seus empregos, e seus processos de preparação |
MXPA05012945A MXPA05012945A (es) | 2003-05-30 | 2004-05-19 | Vinil-polibutadienos hidrogenados similares a caucho. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10324304.6 | 2003-05-30 | ||
DE10324304A DE10324304A1 (de) | 2003-05-30 | 2003-05-30 | Kautschukartige hydrierte Vinyl-Polybutadiene |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2004106386A1 true WO2004106386A1 (de) | 2004-12-09 |
Family
ID=33441440
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2004/005385 WO2004106386A1 (de) | 2003-05-30 | 2004-05-19 | Kautschukartige hydrierte vinyl-polybutadiene |
Country Status (9)
Country | Link |
---|---|
US (1) | US7176262B2 (de) |
EP (1) | EP1633789A1 (de) |
CN (1) | CN100577690C (de) |
BR (1) | BRPI0410882B1 (de) |
CA (1) | CA2524667A1 (de) |
DE (1) | DE10324304A1 (de) |
MX (1) | MXPA05012945A (de) |
TW (1) | TW200508260A (de) |
WO (1) | WO2004106386A1 (de) |
Families Citing this family (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102005044453A1 (de) | 2005-09-17 | 2007-03-22 | Lanxess Deutschland Gmbh | Peroxidisch vernetzte hydrierte Vinylpolybutadiene sowie deren Verwendung zur Herstellung von technischen Gummiartikeln mit gutem Rückverformungsverhalten über einen breiten Temperaturbereich |
DE102005054091A1 (de) * | 2005-11-12 | 2007-05-16 | Lanxess Deutschland Gmbh | Schwefelvernetzte hydrierte Vinylpolybutadiene sowie deren Verwendung zur Herstellung von technischen Gummiartikeln mit guten Rückverformungsverhalten über einen breiten Temperaturbereich |
DE102005061473A1 (de) * | 2005-12-22 | 2007-07-05 | Lanxess Deutschland Gmbh | Hochgefüllte Kautschukmischungen und Vulkanisate auf Basis von hydrierten Vinylpolybutadienen |
DE102006031317A1 (de) * | 2006-07-01 | 2008-01-03 | Lanxess Deutschland Gmbh | Schichtartig aufgebaute Vulkanisate auf Basis von hydriertem Vinylpolybutadien |
US20130172493A1 (en) * | 2011-12-30 | 2013-07-04 | Exxonmobil Research And Engineering Company | Process for making dendritic polyolefins from telechelic polycyclic olefins |
RU2538955C1 (ru) * | 2013-07-09 | 2015-01-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Башкирский государственный университет" | Способ получения гидрированных производных 1,2-полибутадиенов |
RU2538956C1 (ru) * | 2013-07-09 | 2015-01-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Башкирский государственный университет" | Способ получения гидрированных 1,2-полибутадиенов |
RU2539182C1 (ru) * | 2013-10-25 | 2015-01-20 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Башкирский государственный университет" | Способ получения гидрированных 1,2-полибутадиенов |
TWI653245B (zh) * | 2013-12-30 | 2019-03-11 | Arlanxeo Deutschland Gmbh | 含有苯酚之氫化腈橡膠 |
US10428203B2 (en) | 2014-09-08 | 2019-10-01 | Sumitomo Rubber Industries, Ltd. | Pneumatic tire |
JP6716942B2 (ja) | 2016-02-18 | 2020-07-01 | 住友ゴム工業株式会社 | 空気入りタイヤ及び空気入りタイヤの製造方法 |
JP6805502B2 (ja) * | 2016-02-18 | 2020-12-23 | 住友ゴム工業株式会社 | 空気入りタイヤ |
JP6972534B2 (ja) | 2016-10-31 | 2021-11-24 | 住友ゴム工業株式会社 | 混練機投入用ポリマー |
JP6862787B2 (ja) | 2016-11-22 | 2021-04-21 | 住友ゴム工業株式会社 | 空気入りタイヤ |
EP3378877B1 (de) * | 2017-02-28 | 2019-06-19 | Evonik Oil Additives GmbH | Als schmiermitteladditive nützliche hydrierte polybutadiene |
US20230303734A1 (en) | 2020-09-28 | 2023-09-28 | Arlanxeo Deutschland Gmbh | Partially hydrogenated diene polymers |
US12006436B2 (en) * | 2020-11-13 | 2024-06-11 | The Goodyear Tire & Rubber Company | Rubber composition and a tire |
WO2023129959A1 (en) * | 2021-12-29 | 2023-07-06 | Bridgestone Corporation | Hydrogenated polybutadiene polymers and rubber compositions incorporating same |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1520489A (en) * | 1974-12-03 | 1978-08-09 | Inst Francais Du Petrole | Polybutadiene dervatives and lubricating compositions con-taining them |
US4445562A (en) * | 1981-05-07 | 1984-05-01 | The Firestone Tire & Rubber Company | Sealant compositions having, as an essential component, hydrogenated polybutadiene as network polymer |
US5405911A (en) * | 1992-08-31 | 1995-04-11 | Shell Oil Company | Butadiene polymers having terminal functional groups |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3600311A (en) * | 1968-09-03 | 1971-08-17 | Petrolite Corp | Hydrocarbon systems containing branched alkyline polymers |
FR2219219B1 (de) * | 1973-02-22 | 1976-06-11 | Inst Francais Du Petrole | |
US4025478A (en) * | 1975-02-07 | 1977-05-24 | Phillips Petroleum Company | Hot melt adhesive |
US4187360A (en) * | 1975-07-18 | 1980-02-05 | Phillips Petroleum Company | Heat-shrinkable or heat-expandable products from hydrogenated polybutadiene |
AU538067B2 (en) | 1979-08-20 | 1984-07-26 | Firestone Tire And Rubber Co., The | Hydrogenated polybutadiene |
US4238202A (en) | 1979-08-31 | 1980-12-09 | Phillips Petroleum Company | Hydrocarbon fuels with carburetor detergent properties |
US5030779A (en) | 1989-06-08 | 1991-07-09 | Shell Oil Company | Hydrogenation catalyst and hydrogenation process wherein said catalyst is used |
KR100463298B1 (ko) | 2000-10-25 | 2004-12-23 | 아사히 가세이 가부시키가이샤 | 수소 첨가 중합체 |
-
2003
- 2003-05-30 DE DE10324304A patent/DE10324304A1/de not_active Withdrawn
-
2004
- 2004-05-19 CN CN200480014848A patent/CN100577690C/zh not_active Expired - Fee Related
- 2004-05-19 WO PCT/EP2004/005385 patent/WO2004106386A1/de active Application Filing
- 2004-05-19 MX MXPA05012945A patent/MXPA05012945A/es active IP Right Grant
- 2004-05-19 CA CA002524667A patent/CA2524667A1/en not_active Abandoned
- 2004-05-19 BR BRPI0410882-5A patent/BRPI0410882B1/pt not_active IP Right Cessation
- 2004-05-19 EP EP04733789A patent/EP1633789A1/de not_active Withdrawn
- 2004-05-26 US US10/854,385 patent/US7176262B2/en not_active Expired - Fee Related
- 2004-05-28 TW TW093115190A patent/TW200508260A/zh unknown
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1520489A (en) * | 1974-12-03 | 1978-08-09 | Inst Francais Du Petrole | Polybutadiene dervatives and lubricating compositions con-taining them |
US4445562A (en) * | 1981-05-07 | 1984-05-01 | The Firestone Tire & Rubber Company | Sealant compositions having, as an essential component, hydrogenated polybutadiene as network polymer |
US5405911A (en) * | 1992-08-31 | 1995-04-11 | Shell Oil Company | Butadiene polymers having terminal functional groups |
Also Published As
Publication number | Publication date |
---|---|
DE10324304A1 (de) | 2004-12-16 |
US20040242797A1 (en) | 2004-12-02 |
CA2524667A1 (en) | 2004-12-09 |
EP1633789A1 (de) | 2006-03-15 |
CN1798772A (zh) | 2006-07-05 |
BRPI0410882A (pt) | 2006-07-04 |
BRPI0410882B1 (pt) | 2014-01-14 |
US7176262B2 (en) | 2007-02-13 |
CN100577690C (zh) | 2010-01-06 |
MXPA05012945A (es) | 2006-02-28 |
US20050197466A9 (en) | 2005-09-08 |
TW200508260A (en) | 2005-03-01 |
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