Method of preparing conjugated diene-based polymer by continuous polymerization

US11312798B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11312798-B2
Application numberUS-201716763149-A
CountryUS
Kind codeB2
Filing dateDec 22, 2017
Priority dateNov 13, 2017
Publication dateApr 26, 2022
Grant dateApr 26, 2022

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  5. First independent claim

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Abstract

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The present invention relates to a method of preparing a conjugated diene-based polymer by continuous polymerization using two or more reactors, and relates to a method of preparing a conjugated diene-based polymer which is capable of providing a conjugated diene-based polymer having improved Mooney viscosity and excellent cis 1,4 bond content and linearity, by controlling the injection amount of a conjugated diene-based monomer to each reactor in a specific ratio and resolving the deterioration phenomenon of physical properties, which might be generated in continuous reaction.

First claim

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The invention claimed is: 1. A method of preparing a conjugated diene-based polymer comprising: firstly injecting a diene-based monomer to a first reactor to perform a polymerization reaction in a presence of a catalyst composition in a hydrocarbon solvent, and transporting a polymerization reaction product to a second reactor; and secondly injecting the diene-based monomer to the second reactor to perform a polymerization reaction in a presence of a hydrocarbon solvent and a catalyst composition, wherein injection amounts of the diene-based monomer satisfy the following Mathematical Formula 1: 2.7≤ x/y≤ 6.0  [Mathematical Formula 1] in Mathematical Formula 1, x is a first injection amount (weight) of the diene-based monomer, and y is a second injection amount (weight) of the diene-based monomer, wherein the method is a continuous preparation method, wherein cis 1,4 bond content (Cis, wt %) and Mooney viscosity (MV, MU) of a diene-based polymer polymerized in the first reactor and a diene-based polymer polymerized in the second reactor satisfy the following Mathematical Formula 2: −0.02≤(Δ Cis )/(Δ MV ))  [Mathematical Formula 2] in Mathematical Formula 2, ΔC is a value obtained by subtracting a cis 1,4 bond content of the diene-based polymer polymerized in the first reactor from a cis 1,4 bond content of the diene-based polymer polymerized in the second reactor, and ΔMV is a value obtained by subtracting a Mooney viscosity of the diene-based polymer polymerized in the first reactor from a Mooney viscosity of the diene-based polymer polymerized in the second reactor. 2. The method of claim 1 , wherein the diene-based monomer comprises 1,3-butadiene, isoprene, 1,3-pentadiene, 1,3-hexadiene, 2,3-dimethyl-1,3-butadiene, 2-ethyl-1,3-butadiene, 2-methyl-1,3-pentadiene, 3-methyl-1,3-pentadiene, 4-methyl-1,3-pentadiene, 2,4-hexadiene, piperylene, 3-butyl-1,3-octadiene, 2-phenyl-1,3-octadiene or a mixture of two or more thereof. 3. The method of claim 1 , wherein the polymerization reaction in the first reactor and the polymerization reaction in the second reactor is performed at a temperature of −20° C. to 200° C. 4. The method of claim 1 , wherein the catalyst composition comprises a lanthanide rare earth element-containing compound, and at least one of an alkylating agent, a halide or a conjugated diene-based monomer. 5. The method of claim 4 , wherein the lanthanide rare earth element-containing compound comprises a neodymium compound represented by the following Formula 1: in Formula 1, R a to R c are each independently hydrogen or alkyl of 1 to 12 carbon atoms, where R a and R c are not hydrogen at the same time. 6. The method of claim 5 , wherein the neodymium compound is one or more selected from the group consisting of Nd(2,2-diethyl decanoate) 3 , Nd(2,2-dipropyl decanoate) 3 , Nd(2,2-dibutyl decanoate) 3 , Nd(2,2-dihexyl decanoate) 3 , Nd(2,2-dioctyl decanoate) 3 , Nd(2-ethyl-2-propyl decanoate) 3 , Nd(2-ethyl-2-butyl decanoate) 3 , Nd(2-ethyl-2-hexyl decanoate) 3 , Nd(2-propyl-2-butyl decanoate) 3 , Nd(2-propyl-2-hexyl decanoate) 3 , Nd(2-propyl-2-isopropyl decanoate) 3 , Nd(2-butyl-2-hexyl decanoate) 3 , Nd(2-hexyl-2-octyl decanoate) 3 , Nd(2,2-diethyl octanoate) 3 , Nd(2,2-dipropyl octanoate) 3 , Nd(2,2-dibutyl octanoate) 3 , Nd(2,2-dihexyl octanoate) 3 , Nd(2-ethyl-2-propyl octanoate) 3 , Nd(2-ethyl-2-hexyl octanoate) 3 , Nd(2,2-diethyl nonanoate) 3 , Nd(2,2-dipropyl nonanoate) 3 , Nd(2,2-dibutyl nonanoate) 3 , Nd(2,2-dihexyl nonanoate) 3 , Nd(2-ethyl-2-propyl nonanoate) 3 , and Nd(2-ethyl-2-hexyl nonanoate) 3 .

Assignees

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Classifications

  • Optimisation of rolling resistance, e.g. weight reduction · CPC title

  • Narrow molecular weight distribution, i.e. Mw/Mn < 3 · CPC title

  • rare earths being present, e.g. triethylaluminium + neodymium octanoate · CPC title

  • C08F136/06Primary

    Butadiene · CPC title

  • selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides · CPC title

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What does patent US11312798B2 cover?
The present invention relates to a method of preparing a conjugated diene-based polymer by continuous polymerization using two or more reactors, and relates to a method of preparing a conjugated diene-based polymer which is capable of providing a conjugated diene-based polymer having improved Mooney viscosity and excellent cis 1,4 bond content and linearity, by controlling the injection amount …
Who is the assignee on this patent?
Lg Chemical Ltd
What technology area does this patent fall under?
Primary CPC classification C08F136/06. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Apr 26 2022 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 3 related publications on this page (citations in our corpus or others sharing the same primary CPC).