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Method of purification of dihydric phenols

A dihydric phenol, purification process technology, applied in the field of purification of methyl hydroquinone, can solve the problems of increasing color, reducing molecular weight growth, reducing transparency, etc.

Inactive Publication Date: 2013-10-30
SABIC GLOBAL TECH BV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Metal residues present in methylhydroquinone at ppm levels have considerable effects on the properties of the copolymer, for example, reduced molecular weight buildup, reduced transparency and increased color

Method used

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  • Method of purification of dihydric phenols
  • Method of purification of dihydric phenols
  • Method of purification of dihydric phenols

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1-2

[0048] Examples 1-2: These examples provide methods for the purification of methylhydroquinone using activated carbon as an adsorbent.

[0049] Crude MeHQ was purified using activated carbon from Norit corporation using the method described above. The solvent system used in Example 1 is a mixture of methyl isobutyl ketone (MIBK; 150 milliliters) and toluene (150 milliliters); the solvent system used in Example 2 is MIBK (150 milliliters) and petroleum ether (150 milliliters). ml) mixture. Different amounts (weight percent) of activated carbon were used in Examples 1 and 2. The results for metal ion concentrations (expressed in ppb levels) in the purified MeHQ are shown in Table 2 below.

[0050] Table 2

[0051]

Embodiment 3-9

[0052] Examples 3-9: These examples provide methods for the purification of methylhydroquinone using silica as an adsorbent.

[0053] Crude MeHQ was purified using activated carbon from Norit corporation using the method described above. The solvent system used in Example 1 is a mixture of methyl isobutyl ketone (MIBK; 150 milliliters) and toluene (150 milliliters); the solvent system used in Example 2 is MIBK (150 milliliters) and petroleum ether (150 milliliters). ml) mixture.

[0054] The procedure used to purify crude MeHQ using silica in Examples 3-6 was the general procedure described above for purification. The method used in Examples 7-9 involved dissolving MeHQ in toluene at reflux temperature and stirring the silica for 1 hour at the same temperature. The solution was then cooled to 80°C before adding acetone. The silica was then filtered off, and the filtrate was concentrated to obtain MeHQ. Table 3 below lists the different amounts of silica and the mesh size o...

Embodiment 10-13

[0057] Examples 10-13: These examples provide methods for the purification of MeHQ using water-washed silica and acid-washed silica (ie, modified silica) as adsorbent materials.

[0058] Preparation of water-washed silica: reflux silica (100 g) with 500 ml of water for about 30 minutes, filter, and dry in an oven at 120° C. to obtain water-washed silica.

[0059] Preparation of acid-washed silica: reflux silica (100 g) with 500 ml of 1N hydrochloric acid for about 30 minutes, filter, and wash with water until the pH of the filtrate is neutral. The silica was then dried in an oven at 120°C to obtain acid-washed silica.

[0060] The difference in metal ion concentration (expressed in ppb levels) in commercial silica and silica after water or acid washing is shown in Table 4 below.

[0061] Table 4

[0062] source Fe Na Zn mn Ca raw materials for washing 24700 442900 1900 700 273700 Silica after washing 8500 342400 <10

400 148100 p...

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Abstract

A process comprising the steps of dissolving a dihydric phenol in a solvent to form a solution A, contacting the solution A with an adsorbent material selected from the group consisting of metal oxides, modified metal oxides, activated carbons, and clays, filtering the adsorbent material to form a solution B, adding an anti-solvent to the solution B to form a solution C, and distilling the solution C, wherein the dihydric phenol is represented by Formula (I): wherein R is a hydrogen atom or an aliphatic functionality having 1 to 6 carbon atoms and n is an integer having a value of 1 to 4.

Description

Background technique [0001] The present invention generally relates to a process for purifying dihydric phenols. More specifically, the present invention relates to a method of purifying methylhydroquinone. [0002] The current method for preparing dihydric phenols involves oxidation of the corresponding aromatic amines to benzoquinones, followed by reduction of benzoquinones to hydroquinones. For example, a commercial process for the preparation of methylhydroquinone uses o-toluidine as a starting material. The acidic sulfate of o-toluidine is prepared by sulfuric acid treatment, and then the acidic sulfate of o-toluidine is oxidized at a low temperature of about 5-8° C. with manganese dioxide and sulfuric acid. The methylbenzoquinone formed is then steam distilled and reduced in the presence of zinc and / or iron and acid to form methylbenzoquinone. Isolated methylhydroquinone is typically 99% pure and typically contains from about 30 parts per million (ppm) to about 50 ppm...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C37/82C07C39/08
CPCC07C37/685C07C37/82C07C39/08
Inventor 苏尼尔·阿什特卡马赫什·马鲁萨雷格拉姆·基尚普什帕·纳拉亚南拉马纳拉亚南·格夫阿朗·迪克西特普拉迪普·纳德卡尼简-普卢恩·伦斯
Owner SABIC GLOBAL TECH BV