WO2012085846A1 - Method of producing an impermeable rubber layer - Google Patents

Method of producing an impermeable rubber layer Download PDF

Info

Publication number
WO2012085846A1
WO2012085846A1 PCT/IB2011/055828 IB2011055828W WO2012085846A1 WO 2012085846 A1 WO2012085846 A1 WO 2012085846A1 IB 2011055828 W IB2011055828 W IB 2011055828W WO 2012085846 A1 WO2012085846 A1 WO 2012085846A1
Authority
WO
WIPO (PCT)
Prior art keywords
impermeable rubber
chch
producing
rubber layers
group
Prior art date
Application number
PCT/IB2011/055828
Other languages
French (fr)
Inventor
Salvatore Cotugno
Paolo FIORENZA
Paolo Straffi
Original Assignee
Bridgestone Corporation
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Bridgestone Corporation filed Critical Bridgestone Corporation
Publication of WO2012085846A1 publication Critical patent/WO2012085846A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/16Nitrogen-containing compounds
    • C08K5/17Amines; Quaternary ammonium compounds
    • C08K5/19Quaternary ammonium compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B60VEHICLES IN GENERAL
    • B60CVEHICLE TYRES; TYRE INFLATION; TYRE CHANGING; CONNECTING VALVES TO INFLATABLE ELASTIC BODIES IN GENERAL; DEVICES OR ARRANGEMENTS RELATED TO TYRES
    • B60C1/00Tyres characterised by the chemical composition or the physical arrangement or mixture of the composition
    • B60C1/0008Compositions of the inner liner
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/34Silicon-containing compounds
    • C08K3/346Clay
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/18Homopolymers or copolymers of hydrocarbons having four or more carbon atoms
    • C08L23/20Homopolymers or copolymers of hydrocarbons having four or more carbon atoms having four to nine carbon atoms
    • C08L23/22Copolymers of isobutene; Butyl rubber ; Homo- or copolymers of other iso-olefins

Definitions

  • the present invention relates to a method of producing an impermeable rubber layer.
  • the invention relates to an innerliner made from an aqueous emulsion, to which the following description refers purely by way of example.
  • a thinner impermeable layer in the tyre industry, basically amounts to using less material, which has obvious advantages in terms of output, tyre weight reduction, tyre rolling resistance, and overall vehicle fuel consumption.
  • Banbury mixers which involves at least two mixing steps : a longer, high-temperature first mixing step to form the basic mix, and in which ingredients such as carbon black, zinc oxide, stearic acid, wax, antioxiders, etc. are added and mixed with the polymer base; and a cooler second mixing step to complete the basic mix, and in which curing agents, such as sulphur, and accelerants and/or retarding agents are added to the mix from the first step.
  • the purpose of the cooler second step is to ensure dispersion of the curing agents below temperatures that could prematurely cure the mix.
  • the resulting mix must then be extruded or calendered to the required shape.
  • the impermeability of rubber can be enhanced using fillers, which, if mixed properly, form a steric obstruction capable of greatly improving impermeability.
  • fillers such as clay, kaolin, mica, etc. form an air barrier in the finished product, preventing airflow through it, and so making it more impermeable.
  • Any anisotropy of the filler may also improve rubber impermeability.
  • the impermeability of polymer materials to gas or low-molecular-weight substances is also known to increase with glass transition (Tg) .
  • Tg glass transition
  • PET polyethylene terephthalate
  • PET polyethylene terephthalate
  • mechanically coupling rubber and high-Tg polymers, such as PET invariably poses serious difficulties.
  • enhancing the impermeability and so enabling a reduction in the thickness of rubber products the above solutions nevertheless pose various processing problems.
  • Using the traditional Banbury mixer method for example, mixing a clay-containing polymer base is highly energy-intensive, and does not always guarantee effective blending and/or compatibility of all the mix ingredients. Poor blending and/or compatibility of fillers with the rest of the rubber matrix impairs the mechanical characteristics of the end product; and the above problems are further compounded when the polymer base comprises high-Tg polymers.
  • the extruded impermeable layer may also vary in thickness, due to the extrusion process itself; and, because it is eventually applied, at the manufacturing stage, to a shape that also varies in thickness, all these varying thickness points may result in small fractures in the impermeable layer, caused by mechanical and thermal expansion of the tyre at the tyre building stage .
  • the Applicant has surprisingly discovered a method of producing mixes for impermeable rubber layers, which, compared with those of the known art, are less energy- intensive, thinner, and more impermeable.
  • a method of producing impermeable rubber layers comprising:
  • X is an anionic atom or group
  • Ri, R 2 and R 3 which may be the same or different, are each C m H2m+ir where m ranges between 1 and 3, or CH2CHCH2 or CHCHCH 3 ;
  • R4, R6 and R 7 which may be the same or different, are each CH 2 CHCH 2 or CHCHCH 3 ;
  • n 0 or 1
  • y is 1 when n is 1; y is 1 or 2 when n is 0;
  • R 5 is an aliphatic group C 15 -C 2 2 when n is 0; and is an aliphatic group C 8 -Ci 6 when n is 1;
  • R 2 and R 3 are preferably CH 2 CHCH 2 , and, more preferably, n is 1, and R5 is a saturated aliphatic group .
  • R5 comprises a double bond, and n is 0.
  • the surface-active agent has a molecular formula in the group comprising :
  • X " is I " or Br " .
  • Part of the aqueous emulsion was subsequently sprayed or brushed onto a substrate, and the water was evaporated.
  • the five mixes (A-E) according to the invention differed by comprising a different one of the following five surface-active agents (a, b, c, d, e) of molecular formula (I) :
  • the emulsions were formed by dispersing all the ingredients in the Table below simultaneously in enough water to form a homogeneous emulsion.
  • the resulting aqueous solution was agitated mechanically for 30 minutes and then sonicated for 15 minutes to form an aqueous emulsion.
  • a control mix (Ctrl) was also produced using the traditional Banbury mixing method, and with the same composition as the mixes according to the invention, but obviously without the surface-active agent, and comprising stearic acid necessary for conventional curing .
  • the Table below shows the compositions in phr of the control mix, and the mixes produced from respective emulsions in accordance with the present invention.
  • the Table also shows mixing power consumption; the impermeability index, for the same thickness, with respect to that of the control mix; and thickness for the same impermeability.
  • the impermeability indices refer to impermeability to oxygen, and were determined from respective 0.3 mm thick mix layers, which, in the case of mixes A-E, were formed by spraying or brushing the respective emulsions onto a 1 mm substrate.
  • the measurements were made using conventional equipment, such as a MOCON OX-TRA (2/20 module) at 0% relative humidity and 30 °C temperature.
  • the method according to the present invention provides for producing more impermeable, less energy-intensive rubber layers.
  • high-Tg polymers and large amounts of filler can be employed, while still ensuring homogeneous blending of the ingredients, and lower energy consumption.
  • the fillers used in the impermeable layer according to the present invention are prefe'rably defined by mineral particles with a diameter of 0.2 to 2 ⁇ , and an aspect ratio of 5 to 30 and preferably 8 to 20, and are preferably in the group comprising kaolin, clay, mica, feldspar, silica, graphite, bentonite, and alumina.
  • the impermeable layers produced according to the present invention have the major advantage of being producible thinner, and of being more impermeable and less energy- intensive .
  • Reducing the thickness of the impermeable layer amounts, in the examples described, to a roughly 5% reduction in tyre weight as a whole, with obvious advantages in terms of rolling resistance.
  • the impermeable layers according to the present invention also have the advantage of being formed directly upon application, i.e. with no short- or long- term storage, which could degrade the rubber.
  • the impermeable layers may even be applied to the built tyre, after all the expansion work is completed, thus safeguarding against cracks and surface defects frequently encountered in impermeable layers produced using conventional methods .
  • water-mixed impermeable layers may also be used to repair impermeable layers produced using conventional methods.

Abstract

A method of producing impermeable rubber layers, and which includes: a step of preparing an aqueous emulsion containing at least a cross-linkable polymer base, and a surface-active agent of molecular formula (I) { [R1R2R3NR5 (NR4R6R7) n] (n+1) +) y (n+1)Xy- where : X is an anionic atom or group; R1, R2 and R3, which may be the same or different, are each CmH2m+1, where m ranges between 1 and 3, or CH2CHCH2 or CHCHCH3; R4, R6 and R7, which may be the same or different, are each CH2CHCH2 or CHCHCH3; n is 0 or 1; y is 1 when n is 1; y is 1 or 2 when n is 0; R5 is an aliphatic group C15-C22 when n is 0; and is an aliphatic group C8-C16 when n is 1; when n is 0, at least one of R1, R2, R3 and R5 has a double bond.

Description

METHOD OF PRODUCING AN IMPERMEABLE RUBBER LAYER
TECHNICAL FIELD
The present invention relates to a method of producing an impermeable rubber layer.
More specifically, the invention relates to an innerliner made from an aqueous emulsion, to which the following description refers purely by way of example. BACKGROUND ART
As is known, many industrial applications need to produce increasingly thin impermeable layers, but without impairing the impermeability of the layers themselves .
In the tyre industry, a thinner impermeable layer, known as an innerliner, basically amounts to using less material, which has obvious advantages in terms of output, tyre weight reduction, tyre rolling resistance, and overall vehicle fuel consumption.
Mixes for impermeable layers, such as innerliners, are normally produced using internal, so-called Banbury mixers, which involves at least two mixing steps : a longer, high-temperature first mixing step to form the basic mix, and in which ingredients such as carbon black, zinc oxide, stearic acid, wax, antioxiders, etc. are added and mixed with the polymer base; and a cooler second mixing step to complete the basic mix, and in which curing agents, such as sulphur, and accelerants and/or retarding agents are added to the mix from the first step. The purpose of the cooler second step is to ensure dispersion of the curing agents below temperatures that could prematurely cure the mix. The resulting mix must then be extruded or calendered to the required shape.
Highly impermeable rubber products are normally produced with a butyl rubber matrix.
As is known, the impermeability of rubber can be enhanced using fillers, which, if mixed properly, form a steric obstruction capable of greatly improving impermeability. In other words, when mixed with the polymer base, fillers such as clay, kaolin, mica, etc. form an air barrier in the finished product, preventing airflow through it, and so making it more impermeable.
Any anisotropy of the filler may also improve rubber impermeability.
The impermeability of polymer materials to gas or low-molecular-weight substances is also known to increase with glass transition (Tg) . A typical example of this is polyethylene terephthalate (PET) , widely used for packaging in the food and drink industry. Using conventional technology, however, mechanically coupling rubber and high-Tg polymers, such as PET, invariably poses serious difficulties. While enhancing the impermeability and so enabling a reduction in the thickness of rubber products, the above solutions nevertheless pose various processing problems. Using the traditional Banbury mixer method, for example, mixing a clay-containing polymer base is highly energy-intensive, and does not always guarantee effective blending and/or compatibility of all the mix ingredients. Poor blending and/or compatibility of fillers with the rest of the rubber matrix impairs the mechanical characteristics of the end product; and the above problems are further compounded when the polymer base comprises high-Tg polymers.
High energy consumption of the production process not only raises environment issues, but also increases cost.
Current technology is also limited in its ability to produce layers below a given thickness. In fact, the extrusion and/or calendaring step, to which the mix is subjected to form the impermeable layer, demands a minimum thickness of rarely less than 0.5 mm.
The extruded impermeable layer may also vary in thickness, due to the extrusion process itself; and, because it is eventually applied, at the manufacturing stage, to a shape that also varies in thickness, all these varying thickness points may result in small fractures in the impermeable layer, caused by mechanical and thermal expansion of the tyre at the tyre building stage .
The Applicant has surprisingly discovered a method of producing mixes for impermeable rubber layers, which, compared with those of the known art, are less energy- intensive, thinner, and more impermeable.
DISCLOSURE OF INVENTION
According to the present invention, there is provided A method of producing impermeable rubber layers; said method being characterized by comprising:
a step of preparing an aqueous emulsion comprising at least a cross-linkable polymer base, and a surface-active agent of molecular formula (I)
( [R1R2R3 R5 (NR4R6R7) n] (n+1) +) y (n+l)Xy- (I) where :
X is an anionic atom or group;
Ri, R2 and R3, which may be the same or different, are each CmH2m+ir where m ranges between 1 and 3, or CH2CHCH2 or CHCHCH3;
R4, R6 and R7, which may be the same or different, are each CH2CHCH2 or CHCHCH3;
n is 0 or 1;
y is 1 when n is 1; y is 1 or 2 when n is 0;
R5 is an aliphatic group C15-C22 when n is 0; and is an aliphatic group C8-Ci6 when n is 1;
when n is 0, at least one of Ri, R2, R3 and R5 comprises a double bond.
Ri, R2 and R3 are preferably CH2CHCH2, and, more preferably, n is 1, and R5 is a saturated aliphatic group .
Preferably, R5 comprises a double bond, and n is 0.
Preferably, the surface-active agent has a molecular formula in the group comprising :
[ (CH3) 3 (CH2) sCHCH (CH2) 7CH3] + X";
[ (CH2CHCH2)3N(CH2)15CH3]+ X";
[(CH3) (CH2CHCH2)2N (CH2) 15CH3]+ X";
[(CH2CHCH2) (CH3)2N (CH2) 15CH3]+ X";
[ (CH2CHCH2) 3N (CH2) 12N (CH2CHCH2) 3 ] 2 + 2X".
Preferably, X" is I" or Br".
BEST MODE FOR CARRYING OUT THE INVENTION
The following are non-limiting examples, for a clearer understanding of the invention.
EXAMPLES
The following is a description of five mixes (A-E) in accordance with the present invention, each produced by forming a respective aqueous emulsion by dispersing and mixing the mix components in water.
Part of the aqueous emulsion was subsequently sprayed or brushed onto a substrate, and the water was evaporated.
The five mixes (A-E) according to the invention differed by comprising a different one of the following five surface-active agents (a, b, c, d, e) of molecular formula (I) :
surface-active agent (a) of molecular formula [ (CH3)3N(CH2)8CHCH(CH2)7CH3]+ I";
surface-active agent (b) of molecular formula [ (CH2CHCH2)3N(CH2)i5CH3]+ Br";
surface-active agent (c) of molecular formula t(CH3) (CH2CHCH2)2N(CH2)i5CH3]+ I";
- surface-active agent (d) of molecular formula t(CH2CHCH2) (CH3)2N(CH2)15CH3]+ I';
surface-active agent (e) of molecular formula [ (CH2CHCH2) 3N (CH2) 12N ( CH2CHCH2 ) 3 ] 2 + 2Br~.
More specifically, the emulsions were formed by dispersing all the ingredients in the Table below simultaneously in enough water to form a homogeneous emulsion. The resulting aqueous solution was agitated mechanically for 30 minutes and then sonicated for 15 minutes to form an aqueous emulsion.
The above method of producing the aqueous emulsions in no way constitutes a limitation of the present invention .
A control mix (Ctrl) was also produced using the traditional Banbury mixing method, and with the same composition as the mixes according to the invention, but obviously without the surface-active agent, and comprising stearic acid necessary for conventional curing .
The Table below shows the compositions in phr of the control mix, and the mixes produced from respective emulsions in accordance with the present invention.
For each mix, the Table also shows mixing power consumption; the impermeability index, for the same thickness, with respect to that of the control mix; and thickness for the same impermeability.
More specifically, the impermeability indices refer to impermeability to oxygen, and were determined from respective 0.3 mm thick mix layers, which, in the case of mixes A-E, were formed by spraying or brushing the respective emulsions onto a 1 mm substrate. The measurements were made using conventional equipment, such as a MOCON OX-TRA (2/20 module) at 0% relative humidity and 30 °C temperature.
TABLE
Ctrl A B C D E
BUTYL RUBBER 100 100 100 100 100 100
CARBON BLACK 30 30 30 30 30 30
CLAY 50 50 50 50 50 50
PROCESS OIL 0 15 15 15 15 15 15
RESIN 5 5 5 5 5 5
STEARIC ACID 2 ZnO 3 3 3 3 3 3
ACCELERANTS 1,5 1,5 1,5 1,5 1,5 1,5
SULPHUR 0,5 0,5 0,5 0, 5 0,5 0,5
SURFACE-ACTIVE AGENT — 2
(a)
SURFACE-ACTIVE AGENT — — 2
(b)
SURFACE-ACTIVE AGENT 2 — —
(c)
SURFACE-ACTIVE AGENT 2 -- (d)
SURFACE-ACTIVE AGENT 2
(e)
MIXING POWER (KWh) 35 20 20 20 20 20
PERMEABILITY INDEX 100 105 107 105 105 108
THICKNESS FOR A 0, 90 0, 86 0,84 0,86 0,86 0, 83 GIVEN IMPERMEABILIY
(mm)
As shown clearly in the Table, compared with conventional Banbury mixing methods, the method according to the present invention provides for producing more impermeable, less energy-intensive rubber layers.
To improve the impermeability of the rubber layer using the method according to the present invention, high-Tg polymers and large amounts of filler can be employed, while still ensuring homogeneous blending of the ingredients, and lower energy consumption.
The fillers used in the impermeable layer according to the present invention are prefe'rably defined by mineral particles with a diameter of 0.2 to 2 μπι, and an aspect ratio of 5 to 30 and preferably 8 to 20, and are preferably in the group comprising kaolin, clay, mica, feldspar, silica, graphite, bentonite, and alumina.
In short, compared with the known art, the impermeable layers produced according to the present invention have the major advantage of being producible thinner, and of being more impermeable and less energy- intensive .
In fact, using an aqueous emulsion comprising surface-active agents of molecular formula (I), the various ingredients - especially those that are difficult to mix using conventional methods - are dispersed effectively and cheaply; and very thin layers can be formed, by virtue of being formed directly on the application surface, once the water in the applied emulsion evaporates.
Reducing the thickness of the impermeable layer amounts, in the examples described, to a roughly 5% reduction in tyre weight as a whole, with obvious advantages in terms of rolling resistance.
The impermeable layers according to the present invention also have the advantage of being formed directly upon application, i.e. with no short- or long- term storage, which could degrade the rubber.
The impermeable layers may even be applied to the built tyre, after all the expansion work is completed, thus safeguarding against cracks and surface defects frequently encountered in impermeable layers produced using conventional methods .
Finally, the water-mixed impermeable layers may also be used to repair impermeable layers produced using conventional methods.

Claims

1) A method of producing impermeable rubber layers; said method being characterized by comprising:
- a step of preparing an aqueous emulsion comprising at least a cross-linkable polymer base, and a surface-active agent of molecular formula (I)
( [R1R2R3NR5 (NR4R6R7) n] <n+1) + ) y (n+l)Xy- (I) where :
X is an anionic atom or group;
Ri, R2 and R3, which may be the same or different, are each CmHm+i, where m ranges between 1 and 3, or CH2CHCH2 or CHCHCH3;
R4, R6 and R7, which may be the same or different, are each CH2CHCH2 or CHCHCH3;
n is 0 or 1;
y is 1 when n is 1; y is 1 or 2 when -n is 0;
R5 is an aliphatic group Ci5-C22 when n is 0; and is an aliphatic group C8-Ci6 when n is 1;
when n is 0, at least one of Rx, R2, R3 and R5 comprises a double bond.
2) A method of producing impermeable rubber layers, as claimed in Claim 1, characterized in that Ri, R2 and R3 are CH2CHCH2.
3) A method of producing impermeable rubber layers, as claimed in Claim 2, characterized in that n is 1, and R5 is a saturated aliphatic group.
4) A method of producing impermeable rubber layers, as claimed in Claim 1, characterized in that R5 comprises a double bond, and n is 0.
5) A method of producing impermeable rubber layers, as claimed in Claim 1, characterized in that said surface-active agent of molecular formula (I) has a molecular formula in the group comprising :
[ (CH3)3N ( CH2)8CHCH(CH2)7CH3]+ X";
[ (CH2CHCH2)3N ( CH2)i5CH3]+ X";
[(CH3) (CH2CHCH2 ) 2N(CH2)i5CH3]+ X";
[ ( CH2CHCH2 ) (CH3)2N(CH2)15CH3]+ X";
[ (CH2CHCH2) 3N (CH2) 12N (CH2CHCH2) 3 ] 2+ 2X".
6) A method of producing impermeable rubber layers, as claimed in one of the foregoing Claims, characterized in that X" is I" or Br'.
7) A method of producing impermeable rubber layers, as claimed in one of the foregoing Claims, characterized in that said aqueous emulsion comprises a mineral filler comprising particles with a diameter of 0.2 to 2 \im and an aspect ratio of 5 to 30.
8) A method of producing impermeable rubber layers, as claimed in Claim 7, characterized in that said mineral filler comprises particles with an aspect ratio of 8 to 20.
9) A method of producing impermeable rubber layers, as claimed in Claim 7 or 8 , characterized in that said mineral filler is in the group comprising kaolin, clay, mica, feldspar, silica, graphite, bentonite, and alumina".
10) A method of producing impermeable rubber layers, as claimed in one of the foregoing Claims, characterized in that said cross-linkable polymer base comprises polymers with a Tg of over 0°C.
11) An impermeable rubber layer, characterized by being made using the method as claimed in one of the foregoing Claims.
12) An innerliner, characterized by being made from an impermeable rubber layer as claimed in Claim 11.
13) An innerliner repair layer, characterized by being made from an impermeable rubber layer as claimed in Claim 11.
14) A tyre, characterized by comprising an innerliner as claimed in Claim 12, or a repair layer as claimed in Claim 13.
PCT/IB2011/055828 2010-12-20 2011-12-20 Method of producing an impermeable rubber layer WO2012085846A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ITTO2010A001015 2010-12-20
IT001015A ITTO20101015A1 (en) 2010-12-20 2010-12-20 METHOD FOR THE CONSTRUCTION OF A WATERPROOF RUBBER LAYER

Publications (1)

Publication Number Publication Date
WO2012085846A1 true WO2012085846A1 (en) 2012-06-28

Family

ID=43737404

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/IB2011/055828 WO2012085846A1 (en) 2010-12-20 2011-12-20 Method of producing an impermeable rubber layer

Country Status (2)

Country Link
IT (1) ITTO20101015A1 (en)
WO (1) WO2012085846A1 (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3840382A (en) * 1972-01-11 1974-10-08 O Burke Silica pigment and elastomer-silica pigment masterbatches and production processes relating thereto
US20070161734A1 (en) * 2005-12-20 2007-07-12 Hiroyuki Fudemoto Nano-composite and method thereof
EP2181861A1 (en) * 2008-10-30 2010-05-05 Bridgestone Corporation Water-based cement for producing tyres

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3840382A (en) * 1972-01-11 1974-10-08 O Burke Silica pigment and elastomer-silica pigment masterbatches and production processes relating thereto
US20070161734A1 (en) * 2005-12-20 2007-07-12 Hiroyuki Fudemoto Nano-composite and method thereof
EP2181861A1 (en) * 2008-10-30 2010-05-05 Bridgestone Corporation Water-based cement for producing tyres

Also Published As

Publication number Publication date
ITTO20101015A1 (en) 2012-06-21

Similar Documents

Publication Publication Date Title
CN101704965B (en) High-temperature-resistant liquid sealant
EP2509800B1 (en) Method for preparing impermeable rubber layers
KR20160086869A (en) Improvements in the mixing and processing of rubber compositions containing polar fillers
EP2954002B1 (en) Tyre innerliner compound
JP2008538379A (en) Process for producing EPDM rubber compound reinforced with precipitated silica, process for obtaining reinforced rubber profile, colored extruded rubber profile and use thereof
CN107446160B (en) Functionalization montmorillonite Reinforced PVC/NBR elastic body sealing strip and preparation method thereof
CN109206832A (en) A kind of ABS material and preparation method thereof of the extremely low warpage of 3D printing without cracking
WO2012085846A1 (en) Method of producing an impermeable rubber layer
CN108424560A (en) A kind of Tire tread rubber composition and its preparation method and application
KR101829449B1 (en) Composition for fluororubber having excellent mechanical strength
KR101716057B1 (en) The rubber composition having a self-cleaning function, a preparation method thereof and the tire prepared by using it
KR101766053B1 (en) Rubber composition for rim cushion of low-fuel tire
CN105968636A (en) Environmentally friendly material for cable jacket and preparation method thereof
JP5687660B2 (en) Rubber composition for tire and pneumatic tire
EP3408112B1 (en) Rubber compound to produce an inner liner layer
JP7374541B2 (en) Powder composition containing polyimide, method for producing molded product made from the powder composition
KR20160046359A (en) Bladder rubber composition for vulcanizing tire
KR102612230B1 (en) Method of manufacturing tire tread rubber and tire tread manufactured by using it
CN107523247A (en) A kind of fluid sealant for aeroge compound insulating glass and preparation method thereof
CN106995609A (en) A kind of rubber hose of oil resistant
KR101829144B1 (en) Tire innerliner rubber composition and Tire by using the same
WO2023157661A1 (en) Rubber composition for tires
KR20160069214A (en) Tire Rubber Composition Having Improved Low-Fuel Property
KR101132532B1 (en) A tread rubber composition having improved antiabration property and rolling resistance property and a method for preparation of the same
CN104292837A (en) High-elasticity synthetic rubber for color selector and preparation method thereof

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 11813414

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 11813414

Country of ref document: EP

Kind code of ref document: A1