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Methods of purification of 2-aryl-3,3-bis(4-hydroxyaryl)phthalimidines, and polymers derived therefrom

A technology of benzopyrrolone and hydroxyaryl, applied in the field of purification of 2-aryl-3,3-bis(4-hydroxyaryl)benzopyrrolone and polymers derived therefrom, can solve the problem of phenolphthalein Derivatives are lengthy resources, phenolphthalein derivatives are difficult to prepare and separate, dense and other issues

Inactive Publication Date: 2020-02-04
SHPP GLOBAL TECH BV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Phenolphthalein derivatives pure enough for polymer synthesis can be difficult to prepare and isolate
Currently available methods for preparing and isolating phenolphthalein derivatives are lengthy and resource intensive

Method used

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  • Methods of purification of 2-aryl-3,3-bis(4-hydroxyaryl)phthalimidines, and polymers derived therefrom
  • Methods of purification of 2-aryl-3,3-bis(4-hydroxyaryl)phthalimidines, and polymers derived therefrom
  • Methods of purification of 2-aryl-3,3-bis(4-hydroxyaryl)phthalimidines, and polymers derived therefrom

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1A

[0087] 70 kilograms (kg) of phenolphthalein containing 10 wt% water, 98.75 kg aniline, and 22 kg HCl (32 wt% in water) were combined in a 200 liter (L) glass-lined reactor equipped with an overhead condenser. The reaction mixture was heated at 100 to 120 °C and passed through a wiped film evaporator to remove water as an aniline-water azeotrope. The reaction mixture was then heated at 170°C (internal temperature) and continued until the measured concentration of phenolphthalein in the reaction mass was about 1 wt%. The reaction mass was then cooled to 150 to 160°C. The reaction mixture was added to another reactor containing about 650 kg of NaOH (7 wt% to 10 wt% in water). Once the reaction mixture was mixed with aqueous NaOH, it was cooled to about 100°C. The resulting alkaline solution was continuously treated with aniline at a flow rate of about 40 kg / hr at a rate of about 70 kg / hour (hr) in a structured packing extraction column to remove aminophenol impurities. Traces ...

Embodiment 1B

[0093] 70.0 kg of phenolphthalein containing 10 wt% water, 98.75 kg of aniline and 22 kg of HCl (32 wt% in water) were combined in a 200 L glass lined reactor equipped with an overhead condenser. The reaction mixture was heated at 100 to 120 °C and passed through a wiped film evaporator to remove water as an aniline-water azeotrope. The reaction mixture was then heated at 170°C (internal temperature). The reaction was continued until phenolphthalein was about 1 wt% in the reaction mass as measured by HPLC. A portion of this reaction mixture was withdrawn and named Sample 1-1.

[0094] The reaction mass was then cooled to 150 to 160°C. The reaction mixture was added to another reactor containing about 600 kg of NaOH (7 wt% to 10 wt% in water). Once the reaction mixture was mixed with aqueous NaOH, it was cooled to about 100°C. The obtained alkaline solution was continuously treated with aniline at a flow rate of 53 kg / hr at a rate of 67 kg / hr in a structured packing extract...

Embodiment 2

[0102] Mix 300 mL of methanol and 29 mL of HCl in a 1 L glass reactor with an anchor stirrer. 150 mL of the carbon-treated base solution from Example 1A was slowly added to the reactor. The reaction mixture was heated at reflux (about 63°C) for 1 hour, then cooled and maintained at 25°C for 1 hour. The temperature was maintained for a further 30 minutes and then cooled to 10°C. The obtained crystalline solid was filtered and washed with 100 mL of hot water. The isolated product was dried and weighed to 9.2 g.

[0103] The HPLC analysis of the isolated products is given in Table 3.

[0104] table 3

[0105]

[0106] is not detected.

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Abstract

The invention relates to methods of purification of 2-aryl-3,3-bis(4-hydroxyaryl)phthalimidines, and polymers derived therefrom, the method comprising heating a reaction mixture comprising a phenolphthalein compound of formula (II) and a primary arylamine of formula (III) in the presence of an acid catalyst to form a reaction mixture; removing water from the reaction mixture; quenching the reaction mixture with an aqueous alkali solution to form a quenched reaction mixture; extracting the quenched reaction mixture with an aminoaryl compound of formula (IV) to form an organic layer and an extracted aqueous layer comprising a crude 2-aryl-3,3-bis(hydroxyaryl)phthalimidine compound; contacting the extracted aqueous layer with carbon to form a semi-purified 2-aryl-3,3-bis(hydroxyaryl)phthalimidine compound; and mixing the semi-purified 2-aryl-3,3-bis(hydroxyaryl)phthalimidine compound with a solution comprising an alcohol and an acid to form a purified 2-aryl-3,3-bis(hydroxyaryl)phthalimidine of formula (I).

Description

technical field [0001] The present invention relates to a purification method of 2-aryl-3,3-bis(4-hydroxyaryl)benzopyrrolone and a polymer derived therefrom. Background technique [0002] Phenolphthalein derivatives such as 2-phenyl-3,3-bis(4-hydroxyphenyl)benzopyrrolone (also known as N-phenylphenolphthalein bisphenol (PPPBP) or 3,3-bis(4-hydroxyphenyl base)-2-phenylisoindolin-1-one) have been used as aromatic dihydroxy compound monomers to prepare polycarbonate resins as well as polyarylate resins. Phenolphthalein derivatives of sufficient purity for polymer synthesis can be difficult to prepare and isolate. Currently available methods for preparing and isolating phenolphthalein derivatives are lengthy and resource intensive. Purification of crude PPPBP is also typically performed in a batch process, such as described in US Patent 7,135,577, US Patent 7,563,817 and US Patent 7,884,220. The entire process can include eight, ten or more manual interventions. [0003] The...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07D209/46C08G64/24C08G64/30
CPCC07D209/46C08G64/307C08G64/24C08G64/12
Inventor 德希穆克·桑德什·希瓦吉奥什瓦库马尔·孔达西瓦库马尔·斯雷拉马吉里斯瓦库马尔·佩里亚萨米拉维·高塔姆斯里尼瓦桑·纳马拉加内桑·巴拉克里什南
Owner SHPP GLOBAL TECH BV
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