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Method of preparing a poly(phenylene ether), poly(phenylene ether) made thereby, and article comprising the poly(phenylene ether)

A technology of phenylene ether and reaction mixture, which is applied in chemical/physical/physicochemical fixed reactors, color/spectral characteristic measurement, etc., and can solve problems such as product quality change restrictions

Pending Publication Date: 2021-08-17
SHPP GLOBAL TECH BV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Batch operations may suffer limitations including batch-to-batch variation in product quality

Method used

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  • Method of preparing a poly(phenylene ether), poly(phenylene ether) made thereby, and article comprising the poly(phenylene ether)
  • Method of preparing a poly(phenylene ether), poly(phenylene ether) made thereby, and article comprising the poly(phenylene ether)
  • Method of preparing a poly(phenylene ether), poly(phenylene ether) made thereby, and article comprising the poly(phenylene ether)

Examples

Experimental program
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Embodiment

[0051] The materials used in the following examples are described in Table 1.

[0052] Table 1

[0053]

[0054] The reaction mixtures used in Comparative Example 1 and Example 1 were prepared according to the compositions described in Table 2. The amount of each component is given in weight percent based on the total weight of the feed composition. The components were stirred thoroughly to ensure dissolution of the copper catalyst compound, and the resulting mixture was filtered to remove undissolved copper. In the following examples, the reaction mixture was charged to the feed vessel.

[0055] Table 2

[0056] components Concentration in feed (wt%) DMP 6.0 Cu 2 O / HBr 1

0.5 DBA 0.3 DMBA 0.9 diamine mixture 2

0.6 Toluene 91.7

[0057] 1 Cu 2 The weight ratio of O:HBr (48% aqueous solution w / w) is 1.00:11.5;

[0058] 2 The diamine mixture contained 0.2329 grams of DBEDA, 0.1242 grams of DDAC and 0.4193 gr...

Embodiment 1

[0068] The following examples were performed using an Advanced Flow Reactor, AFR, commercially available from Corning. The flow reactor used is a reactor in the form of a plate, where there are multiple plates arranged in series to provide sufficient reactor volume. The above feed composition (as liquid phase) and oxygen (as gas phase) flow through the reactor in co-current. The reaction mixture is pumped through the reactor at a predetermined flow rate. Once the reactor was full of liquid, the reactor was heated to 30°C by passing hot liquid through heat transfer plates surrounding the reactor. At the outlet of the reactor, the liquid phase is collected and the polymer is recovered and isolated to provide the desired poly(phenylene ether).

[0069] Flow reactor process conditions and parameters are given in Table 5. The reaction is carried out in a single reactor.

[0070] table 5

[0071] parameter set point Reactor volume 64ml (8 modules) liquid...

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Abstract

A method for preparing a poly(phenylene ether) includes feeding an oxygen-containing gas phase to a single continuous flow reactor containing a reaction mixture, and oxidatively polymerizing the reaction mixture to form a poly(phenylene ether) in the single reactor. The reaction mixture includes a phenol, a transition metal catalyst, and an organic solvent. A poly(phenylene ether) made by the method and articles including the poly(phenylene ether) are also disclosed. Methods for quantifying phenol concentration and poly(phenylene ether) molecular weight in the reaction mixture are also discussed.

Description

[0001] Citations to related applications [0002] This application claims priority from EP 18201167.6 filed on October 18, 2018, which is hereby incorporated by reference in its entirety. Background technique [0003] Poly(phenylene ether) (poly(phenylene ether)) constitutes a family of engineering thermoplastics that are valued for their chemical and physical properties. Poly(phenylene ether) can be prepared by the oxidative linkage of phenol (phenol) with oxygen in the presence of a catalyst (eg, a copper-amine catalyst). Typical preparations of poly(phenylene ethers) are based on batch processes. Batch operations may suffer from limitations including variations in product quality between batches. Accordingly, there remains a need in the art for improved processes for preparing poly(phenylene ethers) that provide polymer products with reduced reaction times. It is also desirable to provide polymer products with high molecular weight and narrow molecular weight distributio...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08G65/44B01J19/18
CPCC08G65/44G01N21/35
Inventor 西瓦库马尔·斯里拉马吉里萨米尔·阿纳帕特拉杰什·乔杜里拉维纳斯·曼查纳布哈努·基兰·万卡亚拉施韦塔·赫格德拉梅什·纳拉亚纳约格莎·苏巴亚霍
Owner SHPP GLOBAL TECH BV