CN104558329B - A kind of diene's polymer and its preparation method and application - Google Patents

A kind of diene's polymer and its preparation method and application Download PDF

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CN104558329B
CN104558329B CN201310512794.5A CN201310512794A CN104558329B CN 104558329 B CN104558329 B CN 104558329B CN 201310512794 A CN201310512794 A CN 201310512794A CN 104558329 B CN104558329 B CN 104558329B
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diene polymer
structural unit
functionalized
diene
weight
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CN104558329A (en
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梁爱民
徐林
王妮妮
曲亮靓
康新贺
姜科
李传清
解希铭
刘辉
孙文娟
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Sinopec Beijing Research Institute of Chemical Industry
China Petroleum and Chemical Corp
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Sinopec Beijing Research Institute of Chemical Industry
China Petroleum and Chemical Corp
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Application filed by Sinopec Beijing Research Institute of Chemical Industry, China Petroleum and Chemical Corp filed Critical Sinopec Beijing Research Institute of Chemical Industry
Priority to US14/523,113 priority patent/US9296840B2/en
Priority to RU2014142923/04A priority patent/RU2599641C2/en
Priority to DE201410221690 priority patent/DE102014221690A1/en
Priority to BE2014/0796A priority patent/BE1022183B1/en
Priority to FR1460262A priority patent/FR3012455B1/en
Priority to KR1020140146390A priority patent/KR101660856B1/en
Priority to SG10201407122YA priority patent/SG10201407122YA/en
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/80Technologies aiming to reduce greenhouse gasses emissions common to all road transportation technologies
    • Y02T10/86Optimisation of rolling resistance, e.g. weight reduction 

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Abstract

The invention provides a kind of diene's polymer and its preparation method and application.Containing at least one conjugated diene construction unit in the strand of diene's polymer, wherein, also contain formula in the strand of diene's polymer(Ⅰ)Shown silane coupler construction unit, and the number-average molecular weight of diene's polymer is 50,000 100 ten thousand;R1‑R4For C1‑C20Straight or branched alkyl or contain heteroatomic C1‑C20Straight or branched alkyl, one or more of the hetero atom in halogen, oxygen, sulphur, silicon and phosphorus.Diene's polymer can not only be effectively improved the relation between anti-slippery and rolling resistance, can also improve in rubber mixing process due to using undesirable smell caused by silane coupler.

Description

Functionalized diene polymer and preparation method and application thereof
Technical Field
The present invention relates to a functionalized diene polymer, a process for the preparation of a functionalized diene polymer, a functionalized diene polymer prepared by the process, and the use of the functionalized diene polymer as a rubber-based gum.
Background
In recent years, with the development of the automobile industry and the rising of the oil price, people pay more attention to the safety and energy saving of automobiles, and tires having high wet skid resistance and low rolling resistance are required. However, it is often difficult to achieve both improved wet skid resistance and reduced rolling resistance. Therefore, according to different use requirements, an optimum balance between high wet skid resistance and low rolling resistance needs to be found.
For producing a tire with low rolling resistance, the anion-polymerized solution-polymerized butylbenzene has more remarkable advantages than emulsion-polymerized butylbenzene because the anion solution polymerization can effectively adjust the content and the glass transition temperature of a conjugated diene structural unit with a double bond in a side chain. This advantage is advantageous for balancing the relationship between the wet skid resistance and the rolling resistance of the tire. Further, studies have shown that the addition of a silane coupling agent during the kneading of a rubber composition can promote the dispersion of a filler in the raw rubber to some extent and improve the relationship between the wet skid resistance and the rolling resistance of the rubber to some extent, but the reactivity of the silane coupling agent with the raw rubber and carbon black is lowered by the influence of other additives during the kneading of the rubber composition. Further, addition of the silane coupling agent during the kneading of the rubber composition also causes an unpleasant odor. It is disclosed in EP447066 that a silane having a structure represented by formula (1) can be used as a modifier to improve wet skid resistance and reduce rolling resistance of styrene-butadiene rubber:
USi(OR′)jr' 4-i-j is represented by the formula (1),
wherein U is halogen, R 'and R' are C1-C20J is an integer from 1 to 4, i is an integer from 0 to 2, and the sum of i and j is from 2 to 4. The silane having the structure represented by formula (1) can be bonded to a polymer molecular chain by reacting a halogen with a catalyst residue at the end of the polymer molecular chain, however, usually, one polymer molecular chain can be bonded with only one silane molecule, and only a small influence is exerted on the interaction between the polymer molecular chains, and the wet skid resistance of the rubber cannot be effectively improved and the rolling resistance is reduced.
Disclosure of Invention
The invention aims to overcome the defect that the relation between the wet-skid resistance and the rolling resistance of rubber cannot be effectively improved by the existing method, and provides a functionalized diene polymer which has high wet-skid resistance and low rolling resistance, a preparation method of the functionalized diene polymer, a functionalized diene polymer prepared by the method, and application of the functionalized diene polymer in rubber.
The invention provides a functionalized diene polymer, wherein a molecular chain of the functionalized diene polymer contains at least one conjugated diene structural unit, wherein the molecular chain of the functionalized diene polymer also contains a silane coupling agent structural unit shown in a formula (I), and the number average molecular weight of the functionalized diene polymer is 5-100 ten thousand;
wherein R is1-R4Is C1-C20A straight or branched hydrocarbon group or C containing a hetero atom1-C20The heteroatom is selected from one or more of halogen, oxygen, sulfur, silicon and phosphorus.
The present invention also provides a process for the preparation of a functionalized diene polymer, wherein the process comprises contacting a diene polymer comprising at least one conjugated diene structural unit with a silane coupling agent in an inert atmosphere and in the presence of an initiator, said contacting being under conditions such that said silane coupling agent is chemically bonded to said diene polymer; the number average molecular weight of the diene polymer is 5-100 ten thousand, and the content of the conjugated diene structural unit with double bonds in the side chain in the diene polymer is 15-85 wt%, preferably 30-60 wt%, based on the weight of the conjugated diene structural unit in the diene polymer, and the silane coupling agent has a structure shown in a formula (II):
wherein R is1-R4Is C1-C20A straight or branched hydrocarbon group or C containing a hetero atom1-C20The heteroatom is selected from one or more of halogen, oxygen, sulfur, silicon and phosphorus.
The present invention also provides another process for the preparation of a functionalized diene polymer, wherein the process comprises the steps of:
(1) in an inert atmosphere and in the presence of an initiator, carrying out polymerization reaction on conjugated diene in a solvent to obtain a reaction product containing a diene polymer, wherein the polymerization reaction conditions enable the number average molecular weight of the obtained diene polymer to be 5-100 ten thousand, and the content of the conjugated diene structural unit with a double bond in a side chain in the diene polymer is 15-85 wt%, preferably 30-60 wt% based on the weight of the conjugated diene structural unit in the diene polymer;
(2) contacting the reaction product containing the diene polymer obtained in step (1) with a silane coupling agent in an inert atmosphere and in the presence of an initiator, said contacting being under conditions such that said silane coupling agent is chemically bonded to said diene polymer, said silane coupling agent having the structure represented by formula (ii):
wherein R is1-R4Is C1-C20A straight or branched hydrocarbon group or C containing a hetero atom1-C20The heteroatom is selected from one or more of halogen, oxygen, sulfur, silicon and phosphorus.
The invention also provides a functionalized diene polymer prepared by the method.
In addition, the invention also provides the application of the functionalized diene polymer as rubber-based rubber.
As described above, in the prior art, the silane coupling agent is generally added during the rubber mixing process to improve the wet skid resistance and reduce the rolling resistance of the rubber, but the reactivity of the silane coupling agent with the raw rubber and the carbon black is reduced, so that it is difficult to significantly improve the relationship between the wet skid resistance and the rolling resistance of the rubber, and an unpleasant odor is generated. The inventors of the present invention have made extensive studies and have found that the problem of a decrease in the reactivity of a silane coupling agent with raw rubber and carbon black caused during rubber kneading can be avoided and the relationship between wet skid resistance and rolling resistance of a tire made of the thus-obtained functionalized diene polymer can be effectively balanced by chemically bonding the silane coupling agent to the diene polymer and using the resultant functionalized diene polymer as a whole as a part or whole of a rubber-based rubber, and that an unpleasant odor caused by the use of the silane coupling agent during rubber kneading can be improved.
Additional features and advantages of the invention will be set forth in the detailed description which follows.
Detailed Description
The following describes in detail specific embodiments of the present invention. It should be understood that the detailed description and specific examples, while indicating the present invention, are given by way of illustration and explanation only, not limitation.
The molecular chain of the functionalized diene polymer provided by the invention contains at least one conjugated diene structural unit, wherein the molecular chain of the functionalized diene polymer also contains a silane coupling agent structural unit shown in a formula (I), and the number average molecular weight of the functionalized diene polymer is 5-100 ten thousand;
R1-R4is C1-C20A straight or branched hydrocarbon group or C containing a hetero atom1-C20The heteroatom is selected from one or more of halogen, oxygen, sulfur, silicon and phosphorus; preferably, R1-R3Is C1-C5A linear or branched alkyl group or a linear or branched alkoxy group of R4Is C1-C5Linear or branched alkylene groups of (a).
Said C is1-C5Specific examples of the linear or branched alkyl group of (a) include, but are not limited to: methyl, ethyl, n-propyl, isopropyl, n-butyl, sec-butyl, isobutyl, tert-butyl, n-pentyl, isopentyl, tert-pentyl and neopentyl; said C is1-C5Specific examples of the linear or branched alkoxy group of (a) include, but are not limited to: methoxy, ethoxy, n-propoxy, isopropoxy, n-butoxy, sec-butoxy, isobutoxy, tert-butoxy, n-pentoxy, isopentoxy, tert-pentoxy, and neopentoxy; said C is1-C5Specific examples of the linear or branched alkylene group of (a) include, but are not limited to: methylene, ethylene, n-propylene, isopropylene, n-butylene, isobutylene, n-pentylene, or isopentylene.
On the molecular chain of the functionalized diene polymer, conjugated diene structural units form the main chain of the polymer, and the silane coupling agent structural units shown in the formula (I) are bonded to the conjugated diene structural units forming the main chain.
Particularly preferably, in the formula (I), R1-R3Is methoxy, R4Is propylene, in this case, the silane coupling agent corresponding to the structural unit of the silane coupling agent represented by formula (I) is gamma-mercaptopropyltrimethoxysilane; or, R1-R3Is ethoxy, R4Is propylene, in this caseThe silane coupling agent corresponding to the structural unit of the silane coupling agent shown in the formula (I) is gamma-mercaptopropyltriethoxysilane; or, R1-R3Is methyl, R4In this case, the silane coupling agent corresponding to the structural unit of the silane coupling agent represented by the formula (I) is 2-trimethylsilylethylthiol.
The content of the conjugated diene structural unit and the silane coupling agent structural unit in the functionalized diene polymer is not particularly limited in the present invention and may be adjusted according to the amount of the conjugated diene monomer and the silane coupling agent used in the preparation process, but in order to provide the functionalized diene polymer with higher wet skid resistance and lower rolling resistance, the content of the conjugated diene structural unit is preferably 90 to 99.99% by weight, more preferably 98 to 99.8% by weight, and the content of the silane coupling agent structural unit is preferably 0.01 to 10% by weight, more preferably 0.2 to 2% by weight, based on the total weight of the functionalized diene polymer.
The number average molecular weight and molecular weight distribution of the functionalized diene polymer are not particularly limited in the present invention, and for example, the number average molecular weight may be from 5 to 100 ten thousand, preferably from 15 to 20 ten thousand, and the molecular weight distribution may be from 1 to 4, preferably from 1 to 1.5. The number average molecular weight and the molecular weight distribution were both determined by Gel Permeation Chromatography (GPC) with a model LC-10AT from Shimadzu, THF as the mobile phase, narrow-distribution polystyrene as the standard, and a test temperature of 25 ℃.
According to the present invention, the conjugated diene structural unit is a structural unit derived from a conjugated diene, that is, a structural unit formed by polymerization of a conjugated diene. The conjugated diolefins are various unsaturated chain hydrocarbons having a conjugated double bond (i.e., -C = C-) in the molecular structure. The conjugated diene may be conventionally selected in the art and may be suitably selected according to the application of the resulting functionalized diene polymer, for example, the conjugated diene may be selected from one or more of butadiene, isoprene, 1, 3-pentadiene, 1, 3-hexadiene and 2, 3-dimethylbutadiene, preferably butadiene and/or isoprene.
The process for the preparation of a functionalized diene polymer according to the present invention comprises contacting a diene polymer comprising at least one conjugated diene structural unit with a silane coupling agent in an inert atmosphere and in the presence of an initiator, said contacting being under conditions such that said silane coupling agent is chemically bonded to said diene polymer; the number average molecular weight of the diene polymer is 5-100 ten thousand, and the content of the conjugated diene structural unit with double bonds in the side chain in the diene polymer is 15-85 wt%, preferably 30-60 wt%, based on the weight of the conjugated diene structural unit in the diene polymer, and the silane coupling agent has a structure shown in a formula (II):
wherein R is1-R4Is C1-C20A straight or branched hydrocarbon group or C containing a hetero atom1-C20The heteroatom is selected from one or more of halogen, oxygen, sulfur, silicon and phosphorus; preferably, R1-R3Is C1-C5A linear or branched alkyl group or a linear or branched alkoxy group of R4Is C1-C5Linear or branched alkylene groups of (a).
The content of the conjugated diene structural unit with the side chain containing double bonds can be measured by a nuclear magnetic resonance spectrometer of AVANCE DRX400MHz, which is purchased from Bruker company of Switzerland, wherein, the solvent is deuterated chloroform. Specific assay methods are well known to those skilled in the art and will not be described herein.
According to the present invention, the diene polymer can be prepared by various methods known in the art, for example, the preparation method may include: in an inert atmosphere and in the presence of an initiator, polymerizing conjugated diene in a solvent under such conditions that the obtained diene polymer has a number average molecular weight of 5 to 100 ten thousand and the content of the conjugated diene structural unit having a double bond in a side chain in the diene polymer is 15 to 85% by weight, preferably 30 to 60% by weight, based on the weight of the conjugated diene structural unit in the diene polymer.
According to the invention, the inert atmosphere refers to any gas or gas mixture that does not chemically react with the reactants and products, such as one or more of nitrogen and a gas from group zero of the periodic table of the elements. The inert atmosphere may be maintained by introducing any one or a mixture of the above gases which do not chemically react with the reactants and the products into the reaction system.
According to the present invention, the initiator may be any of various initiators capable of initiating polymerization of the conjugated diene, for example, an organolithium initiator, in the preparation of the diene polymer. The organolithium initiator may be, for example, a mono-organolithium initiator of the formula RLi, wherein R is a linear or branched alkyl, cycloalkyl or aryl group. Specifically, the mono-organolithium initiator may be selected from one or more of ethyllithium, propyllithium, isopropyllithium, n-butyllithium, sec-butyllithium, pentyllithium, hexyllithium, cyclohexyllithium, phenyllithium, methylphenyllithium, and naphthyllithium, preferably n-butyllithium and/or sec-butyllithium. In addition, dilithium initiators, such as trimethylenedilithium and/or tetramethylenedilithium, may also be employed in the present invention. The amount of the initiator used in the present invention is not particularly limited and may be appropriately selected depending on the designed molecular weight. It will be readily understood by those skilled in the art that when it is desired to prepare a diene polymer having a relatively large molecular weight, the amount of initiator used can be reduced, but the rate of polymerization will be correspondingly reduced; when it is desired to prepare a diene polymer having a smaller molecular weight, the amount of the initiator used may be increased, but the polymerization rate is increased accordingly. Therefore, in consideration of the polymerization rate and the molecular weight of the obtained diene polymer, it is preferable to use the initiator in an amount of 0.15 to 2.5mmol based on 100g of the total weight of the conjugated diene.
The conditions for the polymerization reaction in the present invention are not particularly limited, and generally include polymerization temperature, polymerization pressure and polymerization time. Among them, in order to more facilitate the polymerization reaction, the polymerization temperature is preferably 10 to 160 ℃, more preferably 40 to 80 ℃, and the polymerization pressure is preferably 0.05 to 0.5MPa, more preferably 0.1 to 0.3 MPa. Generally, the extension of the polymerization time is advantageous for the improvement of the conversion of the reactant and the yield of the reaction product, but the extension of the polymerization time is not significant for the improvement of the conversion of the reactant and the yield of the reaction product, and therefore, the polymerization time is preferably 0.5 to 10 hours, more preferably 0.5 to 2 hours, in view of the combination of the polymerization efficiency and effect.
In the present invention, the pressures are gauge pressures.
According to the present invention, the solvent may be any of various substances capable of acting as a reaction medium in the preparation of the diene polymer, and for example, may be a hydrocarbon solvent and/or an ether solvent. The hydrocarbon solvent may be C5-C7And (3) one or more of cycloalkanes, aromatics and isoparaffins. Specific examples of the hydrocarbon solvent may include, but are not limited to: one or more of benzene, toluene, pentane, heptane, n-hexane, and cyclohexane. The ether solvent may be C4-C15Monoethers and/or polyethers. Specific examples of the ether solvent may include, but are not limited to: t-butoxyethoxyethane and/or tetrahydrofuran. These solvents may be used alone or in combination. The amount of the solvent to be used may be appropriately selected depending on the amount of the monomer, and for example, the amount of the solvent may be such that the total concentration of the conjugated diene may be 1 to 30% by weight, preferably 5 to 20% by weight.
According to the invention, after the polymerization has been completed, a coupling agent may also be added to the polymerization system in order to couple together at least part of the diene polymers. The kind of the coupling agent is well known to those skilled in the art, and may be, for example, one or more of polyvinyl compounds, halides, ethers, aldehydes, ketones, esters, and the like. Specifically, the coupling agent may be selected from one or more of divinylbenzene, tetravinylsilane, tetrachloromethane, silicon tetrachloride, tin tetrachloride, dimethyl terephthalate, and epoxidized soybean oil, and preferably from one or more of divinylbenzene, silicon tetrachloride, and tin tetrachloride. When the coupling agent is a silane compound, the silane compound is different from the silane coupling agent having the structure represented by formula (ii).
The amount of the coupling agent used in the present invention is not particularly limited, and may be suitably selected depending on the amount of the initiator used, and for example, the molar ratio of the coupling agent to the initiator may be 0.1 to 2:1, preferably 0.1 to 1: 1.
According to the present invention, it is preferable that a structure modifier is further added during the preparation of the diene polymer, so that the microstructure of the diene polymer can be effectively controlled. The structure modifier may be any of various existing substances capable of modifying the microstructure of the diene polymer, and may be, for example, one or more selected from the group consisting of diethyl ether, dibutyl ether, tetrahydrofuran, ethylene glycol dimethyl ether, diethylene glycol dimethyl ether, dioxane, crown ether, tetrahydrofurfuryl alcohol diethyl ether, triethylamine, tetramethylethylenediamine, hexamethylphosphoric triamide, potassium tert-butoxide, potassium tert-amylate, potassium laurate, potassium alkylbenzenesulfonate and sodium alkylbenzenesulfonate. Generally, the molar ratio of the structure-modifying agent to the initiator used for the preparation of the diene polymer may be from 1 to 100:1, preferably from 80 to 100: 1.
Generally, anionic polymerization systems do not have significant termination and transfer reactions, and the reactive sites remain when all of the monomer is consumed. Therefore, after the polymerization reaction is completed, the resulting polymer solution should be contacted with a terminating agent to inactivate the active centers. The amount of the terminator to be used may be appropriately selected depending on the amount of the initiator to be used for preparing the diene polymer, and in general, the molar ratio of the terminator to the initiator to be used for preparing the diene polymer may be from 0.1 to 1: 1. The terminator may be any of various agents capable of inactivating the anionic active sites, and for example, may be selected from one or more of water, methanol, ethanol, and isopropanol, preferably isopropanol.
The conditions for contacting the diene polymer with the silane coupling agent in the present invention are not particularly limited as long as the silane coupling agent can be chemically bonded to the diene polymer, and for example, the contacting conditions generally include a contacting temperature, a contacting pressure and a contacting time. Generally, in order to facilitate the chemical bonding of the silane coupling agent to the diene polymer, the contact temperature is preferably from 20 to 150 ℃, more preferably from 40 to 90 ℃, the contact pressure is preferably from 0.01 to 1MPa, more preferably from 0.1 to 0.5MPa, and the contact time is preferably from 0.2 to 24 hours, more preferably from 0.5 to 5 hours.
According to the present invention, in order to achieve both the initiation rate and the molecular weight of the functionalized diene polymer when the diene polymer is brought into contact with the silane coupling agent, the amount of the initiator is preferably 0.01 to 0.1% by weight, more preferably 0.01 to 0.08% by weight, based on the total weight of the diene polymer and the silane coupling agent having the structure represented by formula (II). The initiator may be one or more of radical initiators such as azo-type initiators, peroxide-type initiators, and redox-type initiators, which are well known to those skilled in the art.
The azo initiator may be selected from one or more of dimethyl azobisisobutyrate, azobisisobutyramidine hydrochloride, azobisformamide, azobisisopropylimidazoline hydrochloride, azobisisobutyronitrile formamide, azobiscyclohexylcarbonitrile, azobiscyanovaleric acid, azobisdiisopropylimidazoline, azobisisobutyronitrile, azobisisovaleronitrile, and azobisisoheptonitrile.
The peroxide initiator may be selected from one or more of hydrogen peroxide, ammonium persulfate, sodium persulfate, potassium persulfate, benzoyl peroxide, and benzoyl peroxide tert-butyl ester.
The redox initiator is selected from one or more of sulfate-sulfite, persulfate-thiourea, persulfate-organic salt and ammonium persulfate-fatty amine. Specifically, the sulfate-sulfite may be selected from one or more of sodium sulfate-sodium sulfite, potassium sulfate-potassium sulfite, and ammonium sulfate-ammonium sulfite; the persulfate-thiourea can be one or more selected from sodium persulfate-thiourea, potassium persulfate-thiourea and ammonium persulfate-thiourea; the persulfate-organic salt can be selected from one or more of sodium persulfate-potassium acetate, potassium persulfate-potassium acetate and ammonium persulfate-ammonium acetate; the ammonium persulfate-fatty amine may be selected from ammonium persulfate-N, N-tetramethylethylenediamine and/or ammonium persulfate-diethylamine.
The amounts of the diene polymer and the silane coupling agent having a structure represented by formula (II) to be used according to the present invention may be selected and varied within a wide range, and for example, the amount of the silane coupling agent may be 0.01 to 10g, preferably 0.1 to 5g, more preferably 0.2 to 2g, based on 100g of the diene polymer.
In addition, the present invention provides another process for preparing a functionalized diene polymer, wherein the process comprises the steps of:
(1) in an inert atmosphere and in the presence of an initiator, carrying out polymerization reaction on conjugated diene in a solvent to obtain a reaction product containing a diene polymer, wherein the polymerization reaction conditions enable the number average molecular weight of the obtained diene polymer to be 5-100 ten thousand, and the content of the conjugated diene structural unit with a double bond in a side chain in the diene polymer is 15-85 wt%, preferably 30-60 wt% based on the weight of the conjugated diene structural unit in the diene polymer;
(2) contacting the reaction product containing the diene polymer obtained in step (1) with a silane coupling agent in an inert atmosphere and in the presence of an initiator, said contacting being under conditions such that said silane coupling agent is chemically bonded to said diene polymer, said silane coupling agent having the structure represented by formula (ii):
wherein R is1-R4Is C1-C20A straight or branched hydrocarbon group or C containing a hetero atom1-C20The heteroatom is selected from one or more of halogen, oxygen, sulfur, silicon and phosphorus; preferably, R1-R3Is C1-C5A linear or branched alkyl group or a linear or branched alkoxy group of R4Is C1-C5Linear or branched alkylene groups of (a).
The kinds and amounts of the substances in steps (1) and (2) and the conditions of the polymerization reaction and the contacting conditions can be reasonably selected according to the above description, and will not be described again.
According to the present invention, various additives may also be optionally added to the resulting functionalized diene polymer after the functionalized diene polymer has been prepared. The additive may be, for example, an anti-aging agent, which enables the resulting functionalized diene polymer to have good anti-aging properties. The kind and amount of the antioxidant can be selected conventionally in the field, and will not be described in detail herein.
According to the present invention, after the anti-aging agent is added, the functionalized diene polymer can be precipitated from the solution by purification precipitation, centrifugation, filtration, decantation, hot water coagulation, etc., or the solvent in the reaction system can be removed by gas stripping, which is known to those skilled in the art and will not be described herein.
The invention also provides a functionalized diene polymer prepared by the method.
In addition, the invention also provides the application of the functionalized diene polymer as rubber-based rubber.
The present invention will be described in detail below by way of examples.
In the following examples and comparative examples, the mercapto conversion was measured using an agilent 7890A gas chromatograph under the following test conditions: chromatographic column SPB-560m 0.32mm 1.0um capillary column, column flow rate 2.0ml/min, column temperature 220 ℃, gasification chamber temperature 220 ℃, detection chamber temperature 250 ℃, split ratio 50: 1, the sample amount is 0.3 ul. The content of the conjugated diene structural unit with the side chain containing double bonds is measured by adopting a nuclear magnetic resonance spectrometer of the Bruker company of Switzerland, the model number of which is AVANCE DRX400MHz, wherein the solvent is deuterated chloroform. The number average molecular weight and molecular weight distribution were determined by Gel Permeation Chromatography (GPC) using ALLIANCE2690, WATERS, USA, THF as the mobile phase, narrow distribution polystyrene as the standard, and a temperature of 25 ℃. The Mooney viscosity was measured by the method specified in GB/T1232-92 using a Mooney viscometer model SMV-300 from Shimadzu, Japan. The content of the conjugated diene structural unit = charge amount of conjugated diene ÷ (charge amount of conjugated diene + charge amount of the silane coupling agent having the structure represented by formula (ii) × mercapto conversion) × 100%; the content of the silane coupling agent = charge amount of the silane coupling agent × mercapto conversion ÷ (charge amount of the conjugated diene + charge amount of the silane coupling agent × mercapto conversion) × 100%.
Example 1
This example serves to illustrate the functionalized diene polymer provided by the present invention and the process for its preparation.
(1) In a 5 liter stainless steel stirring tank, 2288g of cyclohexane, 180.00g of butadiene and 1.0g of tetrahydrofurfuryl alcohol ether were added under protection of high purity nitrogen, and then heated to 50 ℃ and 1.2mmol of n-butyllithium were added and the reaction was initiated with controlling the pressure at 0.2MPa for 2 hours to obtain a solution containing a diene polymer. The number average molecular weight of the diene polymer is 16 ten thousand, and the content of the conjugated diene structural unit of which the side chain contains double bonds in the diene polymer is 55.40 wt% based on the weight of the butadiene structural unit in the diene polymer.
(2) 0.8ml (0.836 g) of gamma-mercaptopropyltrimethoxysilane was added to the product obtained in the step (1) and immediately sampled for mercapto group testing, and then 6.7mg of azobisisobutyronitrile was added after heating to 75 ℃ and reacting for 3 hours with controlling the pressure at 0.2MPa to obtain a functionalized diene polymer and sampled for mercapto group testing. To the above functionalized diene polymer was added 0.2g of the antioxidant Irganox1520 and dried in vacuo at 60 ℃ for 24 h. Wherein the mercapto conversion is 80%, the mooney viscosity of the functionalized diene polymer is 45, the number average molecular weight is 16 ten thousand, and the molecular weight distribution is 1.1; based on the total weight of the functionalized diene polymer, the content of butadiene structural units was 99.63 wt% and the content of gamma-mercaptopropyltrimethoxysilane structural units was 0.37 wt%. The polymer has no unpleasant odor.
Example 2
This example serves to illustrate the functionalized diene polymer provided by the present invention and the process for its preparation.
(1) In a 5 liter stainless steel stirring tank, 2288g of cyclohexane, 200.00g of butadiene and 0.65g of tetrahydrofurfuryl alcohol ether were added under protection of high purity nitrogen, and then heated to 40 ℃ and 1.0mmol of n-butyllithium was added and the reaction was initiated with controlling the pressure at 0.1MPa for 2 hours to obtain a solution containing a diene polymer. The number average molecular weight of the diene polymer was 16.6 ten thousand, and the content of a conjugated diene structural unit having a double bond in a side chain in the diene polymer was 39.90% by weight based on the weight of a butadiene structural unit in the diene polymer.
(2) 0.6ml (0.627 g) of gamma-mercaptopropyltrimethoxysilane was added to the product obtained in the step (1), and immediately sampling was conducted for mercapto group testing, and then 13mg of azobisisobutyronitrile was added after heating to 40 ℃ and controlling the pressure at 0.1MPa for 5 hours to obtain a functionalized diene polymer, and sampling was conducted for mercapto group testing. To the above functionalized diene polymer was added 0.2g of the antioxidant Irganox1520 and dried in vacuo at 60 ℃ for 24 h. Wherein the mercapto conversion is 82%, the mooney viscosity of the functionalized diene polymer is 49, the number average molecular weight is 16.6 ten thousand, and the molecular weight distribution is 1.3; the content of butadiene structural units was 99.74 wt% and the content of gamma-mercaptopropyltrimethoxysilane structural units was 0.26 wt%, based on the total weight of the functionalized diene polymer. The polymer has no unpleasant odor.
Example 3
This example serves to illustrate the functionalized diene polymer provided by the present invention and the process for its preparation.
(1) In a 5-liter stainless steel stirring tank, 2288g of hexane, 52.00g of isoprene and 5ml of tetrahydrofuran were added under high-purity nitrogen protection, followed by heating to 75 ℃ and then adding 0.4mmol of n-butyllithium and initiating the reaction under a pressure of 0.3MPa for 0.5 hour to obtain a solution containing a diene polymer. The number average molecular weight of the diene polymer is 16.1 ten thousand, and the content of a conjugated diene structural unit with a double bond in a side chain in the diene polymer is 35.00 weight percent based on the weight of an isoprene structural unit in the diene polymer;
(2) 1.06ml (1.045 g) of gamma-mercaptopropyltriethoxysilane was added to the product obtained in step (1), and immediately sampled for mercapto group testing, then heated to 90 ℃ and 30mg of azobisisobutyronitrile was added and reacted for 0.5 hour under a pressure of 0.5MPa to obtain a functionalized diene polymer, and sampled for mercapto group testing. To the above functionalized diene polymer was added 0.08g of the antioxidant Irganox1520 and dried in vacuo at 60 ℃ for 24 h. Wherein the mercapto conversion is 89%, the mooney viscosity of the functionalized diene polymer is 46, the number average molecular weight is 16.1, and the molecular weight distribution is 1.05; the content of isoprene structural units was 98.24 wt% and the content of gamma-mercaptopropyltriethoxysilane structural units was 1.76 wt%, based on the total weight of the functionalized diene polymer. The polymer has no unpleasant odor.
Example 4
This example serves to illustrate the functionalized diene polymer provided by the present invention and the process for its preparation.
A functionalized diene polymer was prepared according to the procedure of example 1, except that the gamma-mercaptopropyltrimethoxysilane was replaced with the same weight part of 2-trimethylsilylethylthiol to give a functionalized diene polymer. Wherein the mercapto conversion is 72%, the mooney viscosity of the functionalized diene polymer is 41, the number average molecular weight is 15.6, and the molecular weight distribution is 1.03; the content of butadiene structural units was 99.67 wt% and the content of 2-trimethylsilylethylthiol structural units was 0.33 wt%, based on the total weight of the functionalized diene polymer. The polymer has no unpleasant odor.
Comparative example 1
This comparative example serves to illustrate a reference diene polymer and a process for its preparation.
A diene polymer was prepared by following the procedure of example 1 except that the step (2) was not included to obtain a diene polymer. Wherein the Mooney viscosity was 45, the number-average molecular weight was 16 ten thousand, and the molecular weight distribution was 1.09.
Comparative example 2
This comparative example serves to illustrate a reference functionalized diene polymer and a process for its preparation.
(1) 1500g of cyclohexane, 20g of butadiene and 2.7g of tetrahydrofurfuryl alcohol ether are added in a 5 l stainless steel stirred tank under the protection of high-purity nitrogen, and then after heating to 40 ℃ 12mmol of n-butyllithium are added and the reaction is initiated for 1 hour with the pressure being controlled at 0.4MPa to give a solution containing a diene polymer. The number average molecular weight of the diene polymer is 1000, and the content of the conjugated diene structural unit of which the side chain contains double bonds in the diene polymer is 67% by weight based on the weight of the conjugated diene structural unit in the diene polymer.
(2) Adding 20g of gamma-mercaptopropyltrimethoxysilane into the product obtained in the step (1), immediately sampling for a sulfydryl test, then heating to 100 ℃, adding 1g of lauroyl peroxide, controlling the pressure at 0.4MPa, reacting for 5 hours to obtain a functionalized diene polymer, and sampling for a sulfydryl test. Finally dried in vacuum at 80 ℃ for 24 h. Wherein the functionalized diene polymer has a mercapto conversion of 80% and a number average molecular weight of 1788. The content of gamma-mercaptopropyltrimethoxysilane structural units was 44.4 wt.%, based on the total weight of the functionalized diene polymer.
Examples 5 to 8
Examples 5-8 serve to illustrate the preparation of rubber containing functionalized diene polymer.
(1) Preparation of rubber compound:
respectively, 35 parts by weight of the functionalized diene polymer prepared in examples 1 to 4, 10 parts by weight of natural rubber, 55 parts by weight of solution-polymerized styrene-butadiene rubber SSBR2305 (available from Waals rubber trade company, Dongguan), 1 part by weight of stearic acid (available from Hongkong Shi chemical Co., Ltd., SA 1801), 10 parts by weight of abrasion-resistant furnace black N330 (available from Tianjin Jinqiu Shikui carbon black chemical Co., Ltd.), and 60 parts by weight of white carbon 115GR (available from Texas corporation) were uniformly mixed and subjected to Haake heat treatment at a temperature of 150 ℃, a rotation speed of 30rpm/min and a time of 7 min. After completion of the heat treatment, the above mixture was charged into an open mill, and 2.5 parts by weight of zinc oxide (zinc products, Liuzhou Co., Ltd.), 1 part by weight of stearic acid (Hongkong Shi chemical Co., Ltd., SA 1801), 2 parts by weight of an antioxidant 4020, 1.4 parts by weight of N-cyclohexyl-2-benzothiazolesulfenamide (He Geoho chemical Co., Ltd., CZ), 0.75 part by weight of diphenylguanidine (Cangzhou Lima Dow rubber raw materials trade Co., Ltd., DPG) and 6 parts by weight of a silane coupling agent Si69 (Texaco Co., Ltd.) were added and kneaded at 50. + -. 5 ℃ for 60 minutes to obtain a kneaded compound H1-H4.
(2) And (3) vulcanization:
and (2) respectively carrying out vulcanization treatment on the mixed rubber H1-H4 obtained in the step (1) on a flat vulcanizing machine for 40 minutes at 150 ℃ and 12MPa to obtain vulcanized rubber S1-S4.
Comparative example 3
This comparative example serves to illustrate the preparation of a rubber containing a reference diene polymer.
A rubber was prepared by following the procedure of example 5 except that the functionalized diene polymer obtained in example 1 was replaced with the diene polymer obtained in comparative example 1 and the amount of the diene polymer added was 34.87 parts by weight, and further, during the preparation of the rubber compound, 0.13 part by weight of gamma-mercaptopropyltrimethoxysilane was added to obtain a reference vulcanized rubber DS 1.
Comparative example 4
This comparative example serves to illustrate the preparation of a reference vulcanizate.
A vulcanized rubber was prepared by following the procedure of example 5 except that the functionalized diene polymer prepared in preparation example 3 was replaced with a mixture of 99.17 parts by weight of the diene polymer obtained in comparative example 1 and 0.83 part by weight of the functionalized diene polymer obtained in comparative example 2 to obtain a vulcanized rubber DS 2.
Test examples 1 to 4
Test examples 1-4 are provided to illustrate the testing of the properties of the vulcanizates S1-S4 provided by the present invention.
(1) Testing of mechanical properties:
respectively preparing vulcanized rubbers S1-S4 into vulcanized rubber sheets with the thickness of 2 mm; the obtained vulcanized rubber sheet was cut into a dumbbell-shaped standard sheet by a type 1 dumbbell cutter as specified in GB/T528-1998, and the mechanical properties of the vulcanized rubber sheet were measured by a rubber tensile machine (AG-20 KNG, manufactured by Shimadzu corporation, Japan) at a test temperature of 25 ℃ and a pulling speed of 500 mm/min to obtain the tensile strength at break and the elongation at break of the vulcanized rubber, and the results are shown in Table 1.
(2) Test of shore a hardness:
the results obtained were shown in Table 1, and tested according to the method specified in GB/T531-1999.
(3) And (3) testing the deformation resistance:
vulcanized rubbers S1 to S4 were cut into dumbbell-shaped standard pieces by a type 1 dumbbell cutter as specified in GB/T528-92, and the test pieces were pulled apart at a test temperature of 25 ℃ and a pulling speed of 500 mm/min. Placing the sample after tensile fracture for 3min, then jointing the two fractured parts together, measuring the distance between two parallel lines after jointing, and calculating the permanent deformation value after breaking according to the following formula:
Sb=100(Lt-L0)/L0wherein S isbPermanent set at break,%; l istThe distance between two parallel lines after the sample is anastomosed is mm; l is0Initial test length, mm. The results obtained are shown in table 1.
(4) And (3) heat buildup property test:
the measurement was carried out using a compression heat generation tester model Y3000E from Beijing Yongshen electronics, wherein the test temperature was 55 ℃, the test time was 25 minutes, and the compression frequency was 30 times/sec. The results obtained are shown in table 1.
(5) Wet skid resistance and rolling resistance test:
the wet-skid resistance and rolling resistance of vulcanized rubber S1-S4 were measured by a DMA-2980 type viscoelastic spectrometer manufactured by TA of America, wherein the test frequency was 2Hz, the temperature rise rate was 5 ℃/min, the test temperature was 100 ℃, and the sample size was 40mm × 5mm × 1 mm. The wet skid resistance of the vulcanized rubber is represented by tan at 0 ℃, and the larger the tan is, the better the wet skid resistance of the vulcanized rubber is represented; tan at 60 ℃ represents the rolling resistance of the vulcanized rubber, and the smaller tan represents the smaller rolling resistance of the vulcanized rubber; the dispersion of the filler in the rubber is characterized by the value Tan (0 ℃ C.)/Tan (60 ℃ C.), a higher value indicating a better dispersion of the filler. The results obtained are shown in table 1.
Comparative test examples 1 to 2
This comparative test example is intended to illustrate the testing of properties with a reference vulcanizate.
The reference vulcanizates DS1 and DS2 obtained from comparative example 2 and comparative example 3 were tested for their properties according to the methods of test examples 1-4 and the results are shown in Table 1.
TABLE 1
From the above results, it can be seen that the functionalized diene polymer provided by the present invention is not only effective in improving the relationship between wet skid resistance and rolling resistance, but also in improving the unpleasant odor caused by the use of a silane coupling agent during rubber compounding.
The preferred embodiments of the present invention have been described in detail, however, the present invention is not limited to the specific details of the above embodiments, and various simple modifications may be made to the technical solution of the present invention within the technical idea of the present invention, and these simple modifications are within the protective scope of the present invention.
It should be noted that the various features described in the above embodiments may be combined in any suitable manner without departing from the scope of the invention. The invention is not described in detail in order to avoid unnecessary repetition.
In addition, any combination of the various embodiments of the present invention is also possible, and the same should be considered as the disclosure of the present invention as long as it does not depart from the spirit of the present invention.

Claims (20)

1. A functionalized diene polymer, the molecular chain of the functionalized diene polymer contains at least one conjugated diene structural unit, characterized in that the molecular chain of the functionalized diene polymer also contains a modifier structural unit shown in formula (I), and the number average molecular weight of the functionalized diene polymer is 5-100 ten thousand;
wherein R is1-R4Is C1-C20A straight or branched hydrocarbon group or C containing a hetero atom1-C20The heteroatom is oxygen;
based on the total weight of the functionalized diene polymer, the content of the conjugated diene structural unit is 98-99.8 wt%, and the content of the modifier structural unit is 0.2-2 wt%.
2. A functionalized diene polymer according to claim 1, wherein R1-R3Is C1-C5A linear or branched alkyl group or a linear or branched alkoxy group of R4Is C1-C5Linear or branched alkylene groups of (a).
3. A functionalized diene polymer according to claim 1 or 2, wherein in formula (I), R is1-R3Is methoxy, R4Is propylene; or,
R1-R3is ethoxy, R4Is propylene;
R1-R3is methyl, R4Is an ethylene group.
4. A functionalized diene polymer according to claim 1 or 2, wherein the conjugated diene structural units are structural units derived from a conjugated diene selected from one or more of butadiene, isoprene, 1, 3-pentadiene, 1, 3-hexadiene and 2, 3-dimethylbutadiene.
5. A functionalized diene polymer according to claim 1 or claim 2, wherein the functionalized diene polymer has a number average molecular weight of from 15 to 20 ten thousand and a molecular weight distribution of from 1 to 4.
6. A functionalized diene polymer according to claim 5, wherein the functionalized diene polymer has a molecular weight distribution of from 1 to 1.5.
7. A process for the preparation of a functionalized diene polymer, characterized in that it comprises contacting a diene polymer comprising at least one conjugated diene structural unit with a modifier in an inert atmosphere and in the presence of an initiator, said contacting being under conditions such that said modifier is chemically bonded to said diene polymer; the number average molecular weight of the diene polymer is 5-100 ten thousand, and based on the weight of a conjugated diene structural unit in the diene polymer, the content of the conjugated diene structural unit of which the side chain contains double bonds in the diene polymer is 15-85 wt%, and the modifier has a structure shown in a formula (II):
wherein R is1-R4Is C1-C20A straight or branched hydrocarbon group or C containing a hetero atom1-C20The heteroatom is oxygen;
the modifier is used in an amount such that the conjugated diene structural units are present in an amount of 98 to 99.8 weight percent and the modifier structural units derived from the modifier are present in an amount of 0.2 to 2 weight percent, based on the total weight of the functionalized diene polymer.
8. The production process according to claim 7, wherein the content of the conjugated diene structural unit having a double bond in a side chain in the diene polymer is from 30 to 60% by weight based on the weight of the conjugated diene structural unit in the diene polymer.
9. The method of claim 7, wherein R1-R3Is C1-C5Straight or branched alkyl or straight or branched alkoxy of,R4Is C1-C5Linear or branched alkylene groups of (a).
10. The process according to claim 7, wherein the diene polymer is obtained by: in an inert atmosphere and in the presence of an initiator, carrying out polymerization reaction on conjugated diene in a solvent, wherein the polymerization reaction conditions enable the number average molecular weight of the obtained diene polymer to be 5-100 ten thousand, and the content of the conjugated diene structural unit with double bonds in side chains in the diene polymer is 15-85 wt% based on the weight of the conjugated diene structural unit in the diene polymer.
11. The production process according to claim 10, wherein the content of the conjugated diene structural unit having a double bond in a side chain in the diene polymer is from 30 to 60% by weight based on the weight of the conjugated diene structural unit in the diene polymer.
12. A process for the preparation of a functionalized diene polymer, the process comprising the steps of:
(1) in an inert atmosphere and in the presence of an initiator, carrying out polymerization reaction on conjugated diene in a solvent to obtain a reaction product containing a diene polymer, wherein the polymerization reaction condition enables the number average molecular weight of the obtained diene polymer to be 5-100 ten thousand, and the content of a conjugated diene structural unit with a double bond in a side chain in the diene polymer is 15-85 wt% based on the weight of the conjugated diene structural unit in the diene polymer;
(2) contacting the reaction product comprising the diene polymer obtained in step (1) with a modifier in an inert atmosphere and in the presence of an initiator, said contacting being under conditions such that said modifier is chemically bonded to said diene polymer, said modifier having the structure of formula (ii):
wherein R is1-R4Is C1-C20A straight or branched hydrocarbon group or C containing a hetero atom1-C20The heteroatom is oxygen;
the modifier is used in an amount such that the conjugated diene structural units are present in an amount of 98 to 99.8 weight percent and the modifier structural units derived from the modifier are present in an amount of 0.2 to 2 weight percent, based on the total weight of the functionalized diene polymer.
13. The production process according to claim 12, wherein the content of the conjugated diene structural unit having a double bond in a side chain in the diene polymer is from 30 to 60% by weight based on the weight of the conjugated diene structural unit in the diene polymer.
14. The method of claim 12, wherein R1-R3Is C1-C5A linear or branched alkyl group or a linear or branched alkoxy group of R4Is C1-C5Linear or branched alkylene groups of (a).
15. The production method according to any one of claims 10 to 14, wherein the polymerization conditions include a polymerization temperature of 10 to 160 ℃, a polymerization pressure of 0.05 to 0.5MPa, and a polymerization time of 0.5 to 10 hours.
16. The production process according to claim 15, wherein the polymerization conditions include a polymerization temperature of 40 to 80 ℃, a polymerization pressure of 0.1 to 0.3MPa, and a polymerization time of 0.5 to 2 hours.
17. The production process according to any one of claims 7 to 14, wherein the conditions for contacting the diene polymer with the modifier include a contact temperature of 20 to 150 ℃, a contact pressure of 0.01 to 1MPa, and a contact time of 0.2 to 24 hours.
18. The process according to claim 17, wherein the conditions for contacting the diene polymer with the modifier comprise a contact temperature of 40 to 90 ℃, a contact pressure of 0.1 to 0.5MPa and a contact time of 0.5 to 5 hours.
19. A functionalized diene polymer prepared by the process of any one of claims 7 to 18.
20. Use of a functionalized diene polymer according to any one of claims 1 to 6 and 19 as rubber-based gum.
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