JP2004123600A - Method for removing impurity in dihydroxybenzene - Google Patents

Method for removing impurity in dihydroxybenzene Download PDF

Info

Publication number
JP2004123600A
JP2004123600A JP2002289623A JP2002289623A JP2004123600A JP 2004123600 A JP2004123600 A JP 2004123600A JP 2002289623 A JP2002289623 A JP 2002289623A JP 2002289623 A JP2002289623 A JP 2002289623A JP 2004123600 A JP2004123600 A JP 2004123600A
Authority
JP
Japan
Prior art keywords
dihydroxybenzene
boiling side
extraction
removing impurities
section
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2002289623A
Other languages
Japanese (ja)
Other versions
JP4225027B2 (en
Inventor
Mamoru Kiyono
清野 守
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo Chemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP2002289623A priority Critical patent/JP4225027B2/en
Publication of JP2004123600A publication Critical patent/JP2004123600A/en
Application granted granted Critical
Publication of JP4225027B2 publication Critical patent/JP4225027B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To improve effect on removal of impurities in dihydroxybenzene. <P>SOLUTION: The subject method for removing the impurities in the dihydroxybenzene comprises a first process for distilling crude dihydroxybenzene to obtain an acetone-containing fraction from a low-boiling side and a dihydroxybenzene-containing fraction from a high-boiling side, a second process for distilling the dihydroxybenzene-containing fraction to obtain the dihydroxybenzene-containing fraction from a low-boiling side and a heavy component-containing fraction from a high-boiling side, a third process for adding water to the dihydroxybenzene-containing fraction, bringing an extraction solvent into contact with the fraction and separating the fraction into a dihydroxybenzene-containing water layer and an impurity-containing oil layer, and a fourth process for distilling the dihydroxybenzene-containing water layer to obtain the dihydroxybenzene-containing fraction and a water-containing fraction. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
本発明は、ジイソプロピルベンゼンを酸化する工程とジ(2−ジヒドロペルオキシ−2−プロピル)ベンゼンを分解する工程を含むプロセスから得られた粗ジヒドロキシベンゼンの精製方法において、不純物の少ない精製されたジヒドロキシベンゼンを得ることができるという優れた特徴を有するジヒドロキシベンゼン中の不純物除去方法に関するものである。
【0002】
【従来の技術】
ジイソプロピルベンゼンを酸化する工程とジ(2−ジヒドロペルオキシ−2−プロピル)ベンゼンを分解する工程を含むプロセスから得られた粗ジヒドロキシベンゼンから精製されたジヒドロキシベンゼンを得る方法については、例えば抽出操作の際に分液改善のための添加物を用いることなく、優れた効果が得られる方法(特許文献1参照。)が提出され、また、アセトンを留去して得た脱アセトン缶残中に一価フェノール類などの分液改善のための添加物を用いて抽出操作を行う方法(特許文献2参照。)が開示されている。しかし、ジヒドロキシベンゼン中の微量の不純物としてはイソプロペニルフェノール、オキシアセトフェノン等があるが、主として最終製品中に残る微量不純物として問題になるのはイソプロペニルフェノールであり、従来の方法においては、この微量不純物の除去が必ずしも充分に行なわれない場合があるという問題があった。
【0003】
【特許文献1】
特願2001−173726号(第2頁−第3頁)
【特許文献2】
特開昭64−38号公報(第1頁−第4頁)
【0004】
【発明が解決しようとする課題】
かかる状況において、本発明が解決しようとする課題は、ジイソプロピルベンゼンを酸化する工程とジ(2−ジヒドロペルオキシ−2−プロピル)ベンゼンを分解する工程を含むプロセスから得られた粗ジヒドロキシベンゼンの精製方法であって、抽出操作の際に不純物除去のために添加物を用いることにより、不純物の少ない精製されたジヒドロキシベンゼンを得ることができるという優れた特徴を有するジヒドロキシベンゼン中の不純物除去方法を提供する点にある。
【0005】
【課題を解決するための手段】
すなわち、本発明は、ジイソプロピルベンゼンを酸化する工程とジ(2−ジヒドロペルオキシ−2−プロピル)ベンゼンを分解する工程を含むプロセスから得られた粗ジヒドロキシベンゼンの精製方法であって、下記の第一工程から第三工程を含み、かつ第三工程の抽出操作で使用される抽出溶剤に第3成分を添加することにより、ジヒドロキシベンゼン中の不純物除去効果を向上させる事を特徴とするジヒドロキシベンゼン中の不純物除去方法に係るものである。
第一工程:粗ジヒドロキシベンゼンを蒸留に付し、低沸側からアセトンを含む区分を得、高沸側からジヒドロキシベンゼンを含む区分を得る工程;
第二工程:第一工程で得たジヒドロキシベンゼンを含む区分を蒸留に付し、低沸側からジヒドロキシベンゼンを含む区分を得、高沸側から重質分を含む区分を得る工程;
第三工程:第二工程で得たジヒドロキシベンゼンを含む区分に水を追加した後、抽出溶剤に接触させて抽出に付し、ジヒドロキシベンゼンを含む水層と、不純物を含む油層に分離する工程;
第四工程:第三工程で得たジヒドロキシベンゼンを含む水層を蒸留に付し、ジヒドロキシベンゼンを含む区分と水を含む区分を得る工程;
【0006】
【発明の実施の形態】
本発明において用いられる原料は、ジイソプロピルベンゼンを酸化する工程とジ(2−ジヒドロペルオキシ−2−プロピル)ベンゼンを分解する工程を含むプロセスから得られた粗ジヒドロキシベンゼンである。また、粗ジヒドロキシベンゼンの主な成分は、アセトンの含有量は、通常2〜40重量%、イソプロペニルフェノール含有量は、通常0.01〜5重量%、ジヒドロキシベンゼン含有量は、通常2〜40重量%であり、その他の成分がメチルイソブチルケトンである。
【0007】
以下、本発明の不純物除去方法を、その一実施態様を示す図1を参照しながら詳細に説明する。
【0008】
本発明の第一工程1は、上記の粗ジヒドロキシベンゼン6を蒸留に付し、低沸側からアセトンを含む区分8を得、高沸側からジヒドロキシベンゼンを含む区分9を得る工程である。第一工程の条件及び具体的な方法としては、次のものを例示することができる。蒸留は、通常、精留塔を用い、−95〜1000KpaGでの条件で行なうことができる。低沸側にアセトン2〜80重量%を含み、高沸側にイソプロペニルフェノール0.1〜20重量%、重質分1〜30重量%及びジヒドロキシベンゼン70〜99重量%を含む組成をあげることができる。
【0009】
本発明の第二工程2は、第一工程で得たジヒドロキシベンゼンを含む区分9を蒸留に付し、低沸側からジヒドロキシベンゼンを含む区分11を得、高沸側から重質分を含む区分10を得る工程である。第二工程の条件及び具体的な方法としては、次のものを例示することができる。蒸留は、通常、単蒸留あるいは精留塔を用い、−100〜0KpaGの条件で行なうことができる。低沸側にイソプロペニルフェノール0.1〜20重量%及びジヒドロキシベンゼン80〜99.9重量%を含み、高沸側に重質分を含む区分を得ることができる。
【0010】
本発明の第三工程3は、第二工程で重質分を含む区分を除去して得たジヒドロキシベンゼンを含む区分11に第四工程からリサイクルされる水を含む区分12とジヒドロキシベンゼンを含む区分16を追加した後、抽出溶剤13に接触させて抽出に付し、ジヒドロキシベンゼンを含む水層14と、不純物としてイソプロペニルフェノールを含む油層15に分離する工程である。第三工程の条件及び具体的な方法としては、次のものを例示することができる。抽出は、通常抽出塔および/またはミキサーセトラーを用いて、向流抽出を行なうことができる。第二工程で得た重質分の除去されたイソプロペニルフェノール及びジヒドロキシベンゼンを含む区分に水を追加し、5〜70重量%にジヒドロキシベンゼン濃度を調製した後、抽出溶剤に接触させて不純物を油分側に抽出し、ジヒドロキシベンゼンを含む水層と、イソプロペニルフェノール0.05〜20重量%を含む油層に分離することができる。抽出溶剤としては、トルエン、キシレン、シメン、トリイソプロピルベンゼン、ジイソプロピルベンゼン等を用いることができるが、抽出効率および分液性等の観点からトルエンが好適に用いられる。該トルエン中に第3成分を添加することにより、不純物抽出効率の一層の向上を図ることができる。第3成分としてはケトン類が用いられるが、中でもメチルイソブチルケトンを使用することが好適である。第3成分は、少なくともトルエン中に2wt%添加される。
【0011】
本発明の第四工程4は第三工程で得たジヒドロキシベンゼンを含む水層14を蒸留に付し、精製ジヒドロキシベンゼン7を得るとともに、ジヒドロキシベンゼンと不純物を含む区分16と主として水を含む区分12を得る工程である。第四工程の条件及び具体的な方法としては、次のものを例示することができる。蒸留は、通常、精留塔を用い、−99〜1000KpaGでの条件で行なうことができる。まず主として水を含む区分を留出除去後、精製ジヒドロキシベンゼンを留出させて、ジヒドロキシベンゼンと不純物を含む区分を取得することができる。また、この工程で発生する低沸分と高沸分を含むジヒドロキシベンゼンを前工程にリサイクルすることもできる。
【0012】
【実施例】
本発明を実施例に基づいて、より具体的に説明するが、もとより本発明はこれら実施例に限定されるものではない。
実施例1、2、3;比較例1
第二工程で得たm−イソプロペニルフェノール(以下OSTと略す)1.5重量%及びレゾルシン98重量%を含む区分2.3重量部と第四工程から一部リサイクルされるレゾルシンを主として含む区分0.2重量部に水を追加し、50重量%レゾルシン濃度のレゾルシン水溶液を調製した。このレゾルシン水溶液5重量部に対して、トルエンに第3成分としてメチルイソブチルケトン(以下MIBKと略す)をそれぞれ2.4wt%(実施例1)、5wt%(実施例2)、8wt%(実施例3)を添加した抽出溶剤3重量部およびMIBKを添加しないトルエン(比較例1)3重量部を用いて、抽出塔とミキサーセトラーを組み合わせた装置により向流液々抽出を行った。
尚、OST除去率は下記の如くにして求めた。
OST除去率=(抽出前OST量−抽出後OST量)/抽出前OST量
実験結果を、表1に示す。
【0013】
【表1】

Figure 2004123600
【0014】
【発明の効果】
本発明により、ジイソプロピルベンゼンを酸化する工程とジ(2−ジヒドロペルオキシ−2−プロピル)ベンゼンを分解する工程を含むプロセスから得られた粗ジヒドロキシベンゼンの精製方法であって、抽出操作の際に不純物除去のために添加物を用いることにより、不純物の少ない精製されたジヒドロキシベンゼンを得ることができるという優れた特徴を有するジヒドロキシベンゼンの精製方法を提供することができた。
【図面の簡単な説明】
【図1】本発明における不純物除去方法の流れの一例を示す図である。
【符号の説明】
1 第一工程
2 第二工程
3 第三工程
4 第四工程
5 抽出溶剤回収工程
6 粗ジヒドロキシベンゼン
7 精製ジヒドロキシベンゼン
8 アセトンを含む区分
9 ジヒドロキシベンゼンを含む区分
10 重質分を含む区分
11 ジヒドロキシベンゼンを含む区分
12 水を含む区分
13 抽出溶剤
14 ジヒドロキシベンゼンを含む水層
15 イソプロペニルフェノールを含む油層(抽出溶剤層)
16 ジヒドロキシベンゼンを含む区分
17 イソプロペニルフェノールを含む区分[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a method for purifying crude dihydroxybenzene obtained from a process comprising a step of oxidizing diisopropylbenzene and a step of decomposing di (2-dihydroperoxy-2-propyl) benzene, wherein purified dihydroxybenzene having a small amount of impurities is provided. The present invention relates to a method for removing impurities in dihydroxybenzene, which has an excellent feature that it can obtain
[0002]
[Prior art]
A method for obtaining purified dihydroxybenzene from crude dihydroxybenzene obtained from a process including a step of oxidizing diisopropylbenzene and a step of decomposing di (2-dihydroperoxy-2-propyl) benzene is described, for example, in an extraction operation. (See Patent Document 1), which provides excellent effects without using additives for improving liquid separation, and monovalent is contained in the deacetone bottom obtained by distilling acetone. A method of performing an extraction operation using an additive for improving liquid separation such as phenols (see Patent Document 2) is disclosed. However, trace amounts of impurities in dihydroxybenzene include isopropenylphenol and oxyacetophenone, but isopropenylphenol is a problem mainly as a trace impurity remaining in the final product. There has been a problem that impurities may not always be sufficiently removed.
[0003]
[Patent Document 1]
Japanese Patent Application No. 2001-173726 (Pages 2 to 3)
[Patent Document 2]
JP-A-64-38 (pages 1 to 4)
[0004]
[Problems to be solved by the invention]
In such circumstances, the problem to be solved by the present invention is to provide a method for purifying crude dihydroxybenzene obtained from a process comprising a step of oxidizing diisopropylbenzene and a step of decomposing di (2-dihydroperoxy-2-propyl) benzene. And a method for removing impurities in dihydroxybenzene, which has an excellent feature that purified dihydroxybenzene with less impurities can be obtained by using an additive for removing impurities during the extraction operation. On the point.
[0005]
[Means for Solving the Problems]
That is, the present invention relates to a method for purifying crude dihydroxybenzene obtained from a process comprising a step of oxidizing diisopropylbenzene and a step of decomposing di (2-dihydroperoxy-2-propyl) benzene, comprising: The method includes the third step from the step, and the effect of removing impurities in dihydroxybenzene is improved by adding the third component to the extraction solvent used in the extraction operation of the third step. It relates to a method for removing impurities.
First step: a step of subjecting crude dihydroxybenzene to distillation to obtain a fraction containing acetone from the low boiling side and to obtain a fraction containing dihydroxybenzene from the high boiling side;
Second step: a step of subjecting the section containing dihydroxybenzene obtained in the first step to distillation to obtain a section containing dihydroxybenzene from the low boiling side and obtaining a section containing heavy components from the high boiling side;
Third step: a step of adding water to the section containing dihydroxybenzene obtained in the second step, and then contacting it with an extraction solvent and subjecting it to extraction to separate into an aqueous layer containing dihydroxybenzene and an oil layer containing impurities;
Fourth step: a step of subjecting the aqueous layer containing dihydroxybenzene obtained in the third step to distillation to obtain a section containing dihydroxybenzene and a section containing water;
[0006]
BEST MODE FOR CARRYING OUT THE INVENTION
The raw material used in the present invention is crude dihydroxybenzene obtained from a process including a step of oxidizing diisopropylbenzene and a step of decomposing di (2-dihydroperoxy-2-propyl) benzene. The main components of the crude dihydroxybenzene are usually 2 to 40% by weight of acetone, usually 0.01 to 5% by weight of isopropenylphenol, and usually 2 to 40% by weight of dihydroxybenzene. % By weight, and the other component is methyl isobutyl ketone.
[0007]
Hereinafter, the impurity removing method of the present invention will be described in detail with reference to FIG.
[0008]
The first step 1 of the present invention is a step of subjecting the above crude dihydroxybenzene 6 to distillation to obtain a section 8 containing acetone from the low boiling side and a section 9 containing dihydroxybenzene from the high boiling side. The following can be exemplified as the conditions and the specific method of the first step. The distillation can be usually performed using a rectification column under the conditions of -95 to 1000 KpaG. A composition containing 2-80% by weight of acetone on the low boiling side, 0.1-20% by weight of isopropenylphenol, 1-30% by weight of heavy components and 70-99% by weight of dihydroxybenzene on the high boiling side. Can be.
[0009]
In the second step 2 of the present invention, the section 9 containing dihydroxybenzene obtained in the first step is subjected to distillation to obtain a section 11 containing dihydroxybenzene from the low boiling side and a section containing heavy components from the high boiling side. This is the step of obtaining No. 10. The following can be exemplified as the conditions and the specific method of the second step. The distillation can be usually performed using a simple distillation or a rectification column under the conditions of -100 to 0 KpaG. A fraction containing 0.1 to 20% by weight of isopropenylphenol and 80 to 99.9% by weight of dihydroxybenzene on the low boiling side and heavy components on the high boiling side can be obtained.
[0010]
In the third step 3 of the present invention, the section 11 containing dihydroxybenzene obtained by removing the section containing heavy components in the second step is divided into the section 12 containing water recycled from the fourth step and the section containing dihydroxybenzene. After adding 16, it is a step of contacting with an extraction solvent 13 for extraction to separate into an aqueous layer 14 containing dihydroxybenzene and an oil layer 15 containing isopropenylphenol as an impurity. The following can be exemplified as conditions and specific methods of the third step. The extraction can be usually carried out by countercurrent extraction using an extraction column and / or a mixer settler. Water is added to the section containing isopropenylphenol and dihydroxybenzene from which the heavy components obtained in the second step have been removed, and the concentration of dihydroxybenzene is adjusted to 5 to 70% by weight. It can be extracted on the oil side and separated into an aqueous layer containing dihydroxybenzene and an oil layer containing 0.05 to 20% by weight of isopropenylphenol. As the extraction solvent, toluene, xylene, cymene, triisopropylbenzene, diisopropylbenzene and the like can be used, but toluene is preferably used from the viewpoint of extraction efficiency and liquid separation. By adding the third component to the toluene, the impurity extraction efficiency can be further improved. Ketones are used as the third component, and among them, methyl isobutyl ketone is preferably used. The third component is added at least 2 wt% in toluene.
[0011]
In the fourth step 4 of the present invention, the aqueous layer 14 containing dihydroxybenzene obtained in the third step is subjected to distillation to obtain a purified dihydroxybenzene 7, and a section 16 containing dihydroxybenzene and impurities and a section 12 mainly containing water This is the step of obtaining The following can be exemplified as the conditions and specific method of the fourth step. The distillation can be usually performed using a rectification column under the conditions of -99 to 1000 KpaG. First, after distilling and removing a section mainly containing water, purified dihydroxybenzene is distilled to obtain a section containing dihydroxybenzene and impurities. Further, dihydroxybenzene containing a low-boiling component and a high-boiling component generated in this step can be recycled to the preceding step.
[0012]
【Example】
The present invention will be described more specifically based on examples, but the present invention is not limited to these examples.
Examples 1, 2, 3; Comparative Example 1
2.3 parts by weight containing 1.5% by weight of m-isopropenylphenol (hereinafter abbreviated as OST) obtained in the second step and 98% by weight of resorcinol, and a section mainly containing resorcinol partially recycled from the fourth step Water was added to 0.2 parts by weight to prepare a resorcinol aqueous solution having a resorcinol concentration of 50% by weight. With respect to 5 parts by weight of this resorcinol aqueous solution, 2.4 wt% (Example 1), 5 wt% (Example 2), and 8 wt% (Example 1) of methyl isobutyl ketone (hereinafter abbreviated as MIBK) as a third component in toluene Using 3 parts by weight of the extraction solvent to which 3) was added and 3 parts by weight of toluene to which MIBK was not added (Comparative Example 1), countercurrent liquid extraction was performed by an apparatus combining an extraction column and a mixer settler.
The OST removal rate was determined as follows.
OST removal rate = (OST amount before extraction−OST amount after extraction) / OST amount before extraction Experimental results are shown in Table 1.
[0013]
[Table 1]
Figure 2004123600
[0014]
【The invention's effect】
According to the present invention, there is provided a method for purifying crude dihydroxybenzene obtained from a process comprising a step of oxidizing diisopropylbenzene and a step of decomposing di (2-dihydroperoxy-2-propyl) benzene. By using an additive for removal, it was possible to provide a method for purifying dihydroxybenzene having an excellent feature that purified dihydroxybenzene having few impurities can be obtained.
[Brief description of the drawings]
FIG. 1 is a diagram showing an example of a flow of an impurity removing method according to the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 1st process 2 2nd process 3 3rd process 4 4th process 5 Extraction solvent collection process 6 Crude dihydroxybenzene 7 Purified dihydroxybenzene 8 Category 9 containing acetone Category 10 containing dihydroxybenzene Category 11 containing heavy matter 11 Dihydroxybenzene Category 12 containing water Category 13 containing water Extraction solvent 14 Water layer containing dihydroxybenzene 15 Oil layer containing isopropenylphenol (extraction solvent layer)
16 Category containing dihydroxybenzene 17 Category containing isopropenylphenol

Claims (5)

ジイソプロピルベンゼンを酸化する工程とジ(2−ジヒドロペルオキシ−2−プロピル)ベンゼンを分解する工程を含むプロセスから得られた粗ジヒドロキシベンゼンの精製方法であって、下記の第一工程から第三工程を含み、かつ第三工程の抽出操作で使用される抽出溶剤に第3成分を添加することにより、ジヒドロキシベンゼン中の不純物除去効果を向上させることを特徴とするジヒドロキシベンゼン中の不純物除去方法。
第一工程:粗ジヒドロキシベンゼンを蒸留に付し、低沸側からアセトンを含む区分を得、高沸側からジヒドロキシベンゼンを含む区分を得る工程;
第二工程:第一工程で得たジヒドロキシベンゼンを含む区分を蒸留に付し、低沸側からジヒドロキシベンゼンを含む区分を得、高沸側から重質分を含む区分を得る工程;
第三工程:第二工程で得たジヒドロキシベンゼンを含む区分に水を追加した後、抽出溶剤に接触させて抽出に付し、ジヒドロキシベンゼンを含む水層と、不純物を含む油層に分離する工程;
第四工程:第三工程で得たジヒドロキシベンゼンを含む水層を蒸留に付し、ジヒドロキシベンゼンを含む区分と水を含む区分を得る工程;
A method for purifying crude dihydroxybenzene obtained from a process comprising a step of oxidizing diisopropylbenzene and a step of decomposing di (2-dihydroperoxy-2-propyl) benzene, comprising the following first to third steps: A method for removing impurities in dihydroxybenzene, wherein the third component is added to an extraction solvent used in the extraction operation of the third step, thereby improving the effect of removing impurities in dihydroxybenzene.
First step: a step of subjecting crude dihydroxybenzene to distillation to obtain a fraction containing acetone from the low boiling side and to obtain a fraction containing dihydroxybenzene from the high boiling side;
Second step: a step of subjecting the section containing dihydroxybenzene obtained in the first step to distillation to obtain a section containing dihydroxybenzene from the low boiling side and obtaining a section containing heavy components from the high boiling side;
Third step: a step of adding water to the section containing dihydroxybenzene obtained in the second step, and then contacting it with an extraction solvent and subjecting it to extraction to separate into an aqueous layer containing dihydroxybenzene and an oil layer containing impurities;
Fourth step: a step of subjecting the aqueous layer containing dihydroxybenzene obtained in the third step to distillation to obtain a section containing dihydroxybenzene and a section containing water;
第三工程の抽出溶剤がトルエンであり、添加する第3成分がケトン類である請求項1記載のジヒドロキシベンゼン中の不純物除去方法。The method for removing impurities in dihydroxybenzene according to claim 1, wherein the extraction solvent in the third step is toluene, and the third component to be added is a ketone. 第3成分のケトン類がメチルイソブチルケトンである請求項2記載のジヒドロキシベンゼン中の不純物除去方法。3. The method for removing impurities in dihydroxybenzene according to claim 2, wherein the ketone as the third component is methyl isobutyl ketone. ジイソプロピルベンゼンが、m−ジイソプロピルベンゼンであって、ジヒドロキシベンゼンがレゾルシンである請求項1から3のずれかに記載のジヒドロキシベンゼン中の不純物除去方法。4. The method for removing impurities in dihydroxybenzene according to claim 1, wherein the diisopropylbenzene is m-diisopropylbenzene, and the dihydroxybenzene is resorcin. 粗ジヒドロキシベンゼンが、アセトン、イソプロペニルフェノール、メチルイソブチルケトン及び重質分を含有する粗レゾルシンである請求項1から4のいずれかに記載のジヒドロキシベンゼン中の不純物除去方法。5. The method for removing impurities from dihydroxybenzene according to claim 1, wherein the crude dihydroxybenzene is crude resorcinol containing acetone, isopropenylphenol, methyl isobutyl ketone and heavy components.
JP2002289623A 2002-10-02 2002-10-02 Method for removing impurities in dihydroxybenzene Expired - Fee Related JP4225027B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002289623A JP4225027B2 (en) 2002-10-02 2002-10-02 Method for removing impurities in dihydroxybenzene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002289623A JP4225027B2 (en) 2002-10-02 2002-10-02 Method for removing impurities in dihydroxybenzene

Publications (2)

Publication Number Publication Date
JP2004123600A true JP2004123600A (en) 2004-04-22
JP4225027B2 JP4225027B2 (en) 2009-02-18

Family

ID=32281734

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002289623A Expired - Fee Related JP4225027B2 (en) 2002-10-02 2002-10-02 Method for removing impurities in dihydroxybenzene

Country Status (1)

Country Link
JP (1) JP4225027B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104529714A (en) * 2015-01-13 2015-04-22 青岛科技大学 Method for extracting resorcinol

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104529714A (en) * 2015-01-13 2015-04-22 青岛科技大学 Method for extracting resorcinol

Also Published As

Publication number Publication date
JP4225027B2 (en) 2009-02-18

Similar Documents

Publication Publication Date Title
JP2609044B2 (en) Extraction method of phenol from phenol tar
JP2009515967A (en) Recovery of cumene hydroperoxide decomposition products by distillation
KR100835323B1 (en) Propylene Oxide Purification
WO2009080339A3 (en) Method and apparatus for removal of hydrocarbons from an aqueous stream
JP4225027B2 (en) Method for removing impurities in dihydroxybenzene
JP3552306B2 (en) Method for producing propylene oxide and styrene monomer
JP2002363118A (en) Method for purifying dihydroxybenzene
GB2122613A (en) Purification of phenol
JP7130885B2 (en) Chemical Recovery Method for Propylene Oxide-Styrene Monomer Process
USH2194H1 (en) Purification of phenols
JP4224877B2 (en) Method for producing purified phenol
JP4276349B2 (en) Inden production method
EP2412695B1 (en) Method of purifying dihydroxybenzene
JP3823721B2 (en) Extraction and recovery method of polymerization inhibitor
JP6655646B2 (en) Method for producing tar acid
JP3455772B2 (en) Method for recovering phenol and its derivatives
JP2004217529A (en) Method for treating phenol tar
JP2004217538A (en) Method for treating phenol tar
JP2568318B2 (en) Recovery method of high boiling tar acid
WO2018198428A1 (en) Method for recovering tar acid salt and method for producing tar acid
KR0169217B1 (en) Method of separating phenol
JP2012072073A (en) Method for purification of dihydroxybenzene, and method for production of dihydroxybenzene
JPS6357413B2 (en)
JPH07330644A (en) Recovery of a phenol from hydrocarbon mixture
JPS6256448A (en) Separation of highly concentrated hydroxyacetone

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20050419

RD05 Notification of revocation of power of attorney

Effective date: 20080129

Free format text: JAPANESE INTERMEDIATE CODE: A7425

RD05 Notification of revocation of power of attorney

Effective date: 20080512

Free format text: JAPANESE INTERMEDIATE CODE: A7425

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20080704

A131 Notification of reasons for refusal

Effective date: 20080715

Free format text: JAPANESE INTERMEDIATE CODE: A131

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20080806

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20080819

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20080905

A911 Transfer of reconsideration by examiner before appeal (zenchi)

Effective date: 20081016

Free format text: JAPANESE INTERMEDIATE CODE: A911

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Effective date: 20081104

Free format text: JAPANESE INTERMEDIATE CODE: A01

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20081117

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 3

Free format text: PAYMENT UNTIL: 20111205

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111205

Year of fee payment: 3

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111205

Year of fee payment: 3

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121205

Year of fee payment: 4

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121205

Year of fee payment: 4

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20131205

Year of fee payment: 5

LAPS Cancellation because of no payment of annual fees