Process of controlling 1.2-structure content and distribution in polybutyldiene

A technology of polybutadiene and butadiene, applied in the field of polybutadiene control, can solve the problems of product performance degradation, widening of molecular weight distribution, and difficult temperature

Active Publication Date: 2006-11-15
CHINA PETROCHEMICAL CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The systems used in this patent include tetrahydrofuran / ethylene glycol dimethyl ether, tetrahydrofuran / diethylene glycol dimethyl ether, tetrahydrofuran / triethylene glycol dimethyl ether, tetrahydrofuran / hexamethylphosphoric triamide, tetrahydrofuran / tetramethyl However, due to the severe exothermic process of the anionic polymerization process using organolithium as the initiator, the temperature is difficult to control, so that the vinyl content in polybutadiene varies in a wide range
In other words, in the process of butadiene polymerization, as the molecular chain grows, the polymerization temperature gradually increases. After the temperature rises, the selectivity of the vinyl structure during polymerization will decrease. Low, high vinyl structure content, low butadiene content in late polymerization, if the polymerization temperature fluctuation exceeds 20 ° C, the difference in vinyl content in the butadiene chain may exceed 10%, resulting in product Defects
[0010] The content and distribution of vinyl groups in the polybutadiene chain can be controlled by adopting a single heavy ether in a continuous adding mode or first carrying out isothermal reaction and then carrying out adiabatic reaction, but studies have shown (Elastomer, 1999 No. 38): Ethers have a self-terminating effect in the polymerization system initiated by alkyllithium, that is, during the polymerization process, the ether will deactivate the active lithium and lead to the growth of the molecular chain, which will broaden the molecular weight distribution of the polymer, or oligomerization The content of the compound increases (the content of the oligomer is analyzed by gel permeation chromatography (GPC), which reduces the performance of the product

Method used

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  • Process of controlling 1.2-structure content and distribution in polybutyldiene
  • Process of controlling 1.2-structure content and distribution in polybutyldiene
  • Process of controlling 1.2-structure content and distribution in polybutyldiene

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1~10

[0023] Embodiments 1-10: Comparison of self-terminating side reactions and product performance of different regulating systems:

Embodiment 1

[0024] Embodiment 1: add 3500ml cyclohexane in 10L polymerization kettle, add the n-butyllithium of calculated amount (the Mn molecular weight of design base glue is 230,000), 57ml styrene, the main regulator tetrahydrofuran (tetrahydrofuran and tetrahydrofuran) of all calculated amounts The mole of n-butyllithium is 5), control a reaction temperature of 40 ~ 60 DEG C, add 400ml of butadiene after 25 minutes of reaction, and add the calculated auxiliary regulator B continuously with a metering pump after 5 minutes of butadiene addition. Glycol diethyl ether (the mole of ethylene glycol diethyl ether and n-butyllithium is 0.8), the addition time is 15 minutes, the temperature of butadiene polymerization rises from 40°C to 95°C, the reaction time is 35 minutes, and the second stage reaction is completed Then add 57ml of styrene to react for 25 minutes to obtain S-EB-S basic glue, test its 1,2-structure content with NMR spectrometer, and analyze its oligomer content with GPC; hydr...

Embodiment 2

[0025] Example 2: The co-regulator ethylene glycol diethyl ether was added together with the main regulator tetrahydrofuran at one time, and the remaining conditions were the same as in Example 1. The test data are shown in Table 1.

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Abstract

A process for controlling the content and distribution of 1,2-structure in polybutadiene features use of a tetrahydrofuran / ethanediol diether (or dibutylether) as its regulation system to make the content of 1,2-structures in 33-37% range and the uniform distribution of 1,2-structures in molecular chain.

Description

technical field [0001] The invention relates to a method for controlling the content and distribution of 1,2-structure in polybutadiene. Background technique [0002] S-EB-S, the hydrogenation product of polystyrene-polybutadiene-polystyrene thermoplastic elastomer SBS, as a new type of thermoplastic elastomer, is resistant to aging compared with SBS, and is widely used in various soft-touch handles , auto parts, wire and cable sheaths, sealing strips, modification of engineering plastics, adhesives and other fields. The S-EB-S thermoplastic elastomer requires that the middle block polybutadiene B of SBS must contain vinyl (1,2-structure) between 35 and 55%, so as to ensure that it becomes an elastomer instead of a plastic after hydrogenation ; In order to ensure the excellent performance of S-EB-S, it is also required that the 1,2-structure be evenly distributed in the mid-block polybutadiene B. This is because S-EB-S has the following structure: [0003] [0004] Ame...

Claims

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Application Information

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IPC IPC(8): C08F136/06C08F2/38C08F4/48
Inventor 梁红文李望明张志斌康铮彭小寒张君花
Owner CHINA PETROCHEMICAL CORP
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