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Production of 4,4'-bisphenol sulphone

A manufacturing method and technology of phenol sulfone, which are applied in chemical instruments and methods, preparation of organic compounds, organic chemistry, etc., can solve the problems of difficult to deal with solid blocks, rising manufacturing costs, and no post-processing operation is beneficial, and can promote water The effect of easy removal, simple reflux operation, and easy recycling

Inactive Publication Date: 2007-06-20
NIPPON SODA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, there is a problem that the reaction product obtained after the solvent is distilled off becomes a solid block that is industrially difficult to handle, and it is necessary to control the reaction conditions for adjusting the removal rate of the solvent and the isomerization rate
[0011] In addition, in this invention, two types of solvents are used: a suspending agent (for example, Aisopa-(registered trademark of Exxon Chemical Co., Ltd.) H, initial boiling point 176°C) and an entrainer (for example, Aisopa-E, initial boiling point 115°C) It is indispensable, but when using solvents with different physical properties as described above, the problem is that when the solvent is reused, it will be difficult to manage the boiling point, etc., and it will also lead to an increase in production costs.
[0012] Therefore, in above-mentioned prior art, also do not have the method that the aftertreatment operation after reaction is favorable

Method used

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  • Production of 4,4'-bisphenol sulphone
  • Production of 4,4'-bisphenol sulphone

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0103] Put 98.7g (1.05mol) of phenol, 75ml of Aisopa-H, and 50ml of mesitylene into a 500ml four-neck flask equipped with a stirrer, a thermometer, and a water separation tube. After adding 51.6 g (0.50 mol) of 95% sulfuric acid dropwise, the temperature was raised.

[0104] Distillation of the reaction liquid started from around 148° C., the distillate was condensed in a water separation tube and separated into two layers, and the upper organic layer was continuously returned to the reaction system. The temperature of the reaction system reached 170° C. after about 4 hours from the start of the temperature rise, the generation of water stopped, and the amount of water separated in the water separation tube was 20.5 g. Thereafter, 50 ml of AISOPA-H was added, and it took 3 hours for the temperature of the reaction system to reach 175° C. to distill off mesitylene. The composition of the reactant was analyzed by high-performance liquid chromatography (HPLC), and the result was...

Embodiment 2

[0108] Put 98.7g (1.05mol) of phenol and 100ml of AISOPA-G into a 500ml four-necked flask equipped with a stirrer, a thermometer, and a water separation tube, and add 51.6g of 95% sulfuric acid dropwise to the mixture at 50°C under stirring. (0.50 mol), the temperature was raised.

[0109] Distillation of the reaction liquid started at around 144°C, and the distillate was condensed and separated into three layers in a water separation tube. The upper layer was a solvent layer, the middle layer was a water layer, and the bottom layer was a phenol layer. The upper solvent layer was continuously returned to the reaction system, and the bottom phenol layer was extracted every 15 minutes and returned to the reaction system. The temperature of the reaction system reached 167° C. in about 7 hours from the start of the temperature rise, the generation of water stopped, and the amount of water separated in the water separation tube was 21.2 g. The total amount of phenol returned to th...

Embodiment 3

[0113] 117.5 g (1.25 moles) of phenol and 100 ml of AISOPA-G were charged into a 500 ml four-necked flask equipped with a stirrer, a thermometer, a water separation tube, and a Wedman-type rectification column, and the mixture was added to the mixture at 50 ° C under stirring conditions. After adding dropwise 51.6 g (0.50 mol) of 95% sulfuric acid in the mixture, the temperature was raised.

[0114] Distillation of the reaction liquid started around 144°C, and the distillate was condensed and separated into three layers in the water separation tube, the upper layer being a solvent layer, the middle layer being a water layer, and the bottom layer being a phenol layer. The upper solvent layer was continuously returned to the reaction system, and the bottom phenol layer was reacted without returning to the reaction system. The temperature of the reaction system reached 167° C. in about 10 hours from the start of the temperature rise, and the generation of water stopped. The amoun...

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Abstract

Production of 4,4'-biphenofone is carried out by dewater reacting in mixed solvent of fatty saturated hydrocarbon and mesitylene at boiling-point 175degree or above, distilling, removing mesitylene or reacting in solvent containing fatty saturated hydrocarbon, adding alcohol with carbon1-3 into reactant, separating and re-crystallizing to obtain the final product. It has high purity and better operating performance.

Description

[0001] This application is a divisional application of a Chinese patent application with an application date of March 20, 2002 and an application number of 02828560.3 (international application number is PCT / JP02 / 02702; divisional application number 200610003377.8). technical field [0002] The present invention relates to a method for producing 4,4'-bisphenol sulfone (or 4,4'-dihydroxydiphenylsulfone, hereinafter referred to as 4,4'-BPS) by reacting phenol and sulfuric acid. Background technique [0003] 4,4'-BPS is a useful compound generally used as a raw material for engineering plastics such as polysulfone (PSF) and polyethersulfone (PES). In order to produce this 4,4'-BPS, although the method of reacting phenol and sulfuric acid has been frequently studied, the main problems of this technology are how to efficiently remove water and how to reduce the by-product isomer 2,4 '-BPS to increase the yield of 4,4'-BPS in both ways. [0004] A kind of 4, the manufacture metho...

Claims

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Application Information

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IPC IPC(8): C07C317/22C07C315/00
CPCC07C315/00
Inventor 肥高友也
Owner NIPPON SODA CO LTD
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