JP4928092B2 - Method for purifying aromatic dihydroxy compounds - Google Patents
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- JP4928092B2 JP4928092B2 JP2005131485A JP2005131485A JP4928092B2 JP 4928092 B2 JP4928092 B2 JP 4928092B2 JP 2005131485 A JP2005131485 A JP 2005131485A JP 2005131485 A JP2005131485 A JP 2005131485A JP 4928092 B2 JP4928092 B2 JP 4928092B2
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Description
本発明は、芳香族ジヒドロキシ化合物を精製する方法に関し、より詳しくは、芳香族ジヒドロキシ化合物を超臨界水または亜臨界水に溶解せしめ、次いで超臨界状態を解除して晶析させることを特徴とする、全く新規な芳香族ジヒドロキシ化合物の精製方法に関する。 The present invention relates to a method for purifying an aromatic dihydroxy compound. More specifically, the present invention is characterized by dissolving an aromatic dihydroxy compound in supercritical water or subcritical water and then releasing the supercritical state to cause crystallization. The present invention relates to a completely new method for purifying aromatic dihydroxy compounds.
芳香族ジヒドロキシ化合物は、ポリカーボネート樹脂、エポキシ系樹脂、ポリエステル樹脂、あるいはフェノール樹脂原料として広く用いられている。なかでも2,2−ビス(4−ヒドロキシフェニル)プロパン、すなわち、ビスフェノールA(以後BPAと表記する。)はポリカーボネート樹脂やエポキシ系樹脂の原料として有用な化学品であり、通常フェノールとアセトンとを酸性触媒の存在下で反応させることにより製造されている。しかしながら、この方法で得たBPA結晶の中にはフェノール、BPA異性体のほか、反応時などに生成した不純物が含有されており、この影響で結晶が着色する傾向がある。BPA結晶の着色度が大きい場合にはこれを原料として製造したポリカーボネート樹脂又はエポキシ樹脂の品質までが低下するので、BPA結晶の着色度はできるだけ低く、純度はできるだけ高いことが望ましい。 Aromatic dihydroxy compounds are widely used as raw materials for polycarbonate resins, epoxy resins, polyester resins, or phenol resins. Among them, 2,2-bis (4-hydroxyphenyl) propane, that is, bisphenol A (hereinafter referred to as BPA) is a chemical product useful as a raw material for polycarbonate resins and epoxy resins, and usually contains phenol and acetone. It is produced by reacting in the presence of an acidic catalyst. However, the BPA crystals obtained by this method contain phenol and BPA isomers, as well as impurities generated during the reaction, etc., and this influence tends to color the crystals. When the coloration degree of the BPA crystal is large, the quality of the polycarbonate resin or epoxy resin produced using this as a raw material is lowered. Therefore, it is desirable that the coloration degree of the BPA crystal is as low as possible and the purity is as high as possible.
また、近年ポリカーボネート樹脂やエポキシ樹脂のケミカルリサイクルにより芳香族ジヒドロキシ化合物を回収する方法が広く検討されているが、これにおいても上記不純物や樹脂中に含まれている無機物などの除去が解決すべき重要な課題となっている。 In recent years, methods for recovering aromatic dihydroxy compounds by chemical recycling of polycarbonate resins and epoxy resins have been widely studied, but even in this case, it is important to remove the impurities and inorganic substances contained in the resins. It is a difficult issue.
そこで、上記芳香族ジヒドロキシ化合物については種々の精製方法が検討されてきた。BPAの精製方法としては例えば溶融BPAをフラッシュ蒸留装置に供給し、フェノールを含む軽沸物を蒸発除去する方法が知られている(特許文献1:特開2004−67617号公報)。しかし上記方法はフラッシュ蒸発装置の他に薄膜蒸発装置や気液分離装置などが必要であり、プロセスが非常に複雑であった。また、一方でBPAとフェノールとのアダクトを形成する工程を含むBPAの精製方法(特許文献2:特開昭59−231033号公報)、およびBPAを有機溶媒に溶解させ、貧溶媒を加えて再結晶させる方法などが広く知られている(特許文献3:特開平2−229126号公報)。しかし上記方法はいずれも有機溶媒を使用するため、環境への悪影響が懸念され、かつ経済性において問題を有していた。さらに、上記精製方法は特に電子材料用途において嫌われる無機塩の除去を目的とするものではなかった。 Thus, various purification methods have been studied for the aromatic dihydroxy compounds. As a method for purifying BPA, for example, a method of supplying molten BPA to a flash distillation apparatus and evaporating and removing light-boiling substances containing phenol is known (Patent Document 1: Japanese Patent Application Laid-Open No. 2004-67617). However, the above method requires a thin film evaporator and a gas-liquid separator in addition to the flash evaporator, and the process is very complicated. On the other hand, a BPA purification method including a step of forming an adduct of BPA and phenol (Patent Document 2: Japanese Patent Application Laid-Open No. 59-233103), and BPA is dissolved in an organic solvent, and a poor solvent is added to perform re-treatment. A method of crystallizing is widely known (Patent Document 3: Japanese Patent Laid-Open No. 2-229126). However, since any of the above methods uses an organic solvent, there is a concern about an adverse effect on the environment, and there is a problem in economical efficiency. Further, the above purification method is not intended to remove inorganic salts which are hated particularly in electronic materials.
上記のように、第一に工程が簡便で低コストであり、かつ環境に負荷をかけずに有機不純物および無機不純物を効率的に除去できる芳香族ジヒドロキシ化合物の精製方法が強く要望されていた。 As described above, firstly, there has been a strong demand for a method for purifying an aromatic dihydroxy compound that is simple in process and low in cost, and that can efficiently remove organic impurities and inorganic impurities without burdening the environment.
本発明は、上記の問題点に鑑み、有機溶媒を用いず、短時間かつ簡易的なプロセスで、芳香族ジヒドロキシ化合物を精製する方法の提供を目的とするものである。 In view of the above problems, an object of the present invention is to provide a method for purifying an aromatic dihydroxy compound in a short time and with a simple process without using an organic solvent.
本発明者らは、上記問題を解決するべく鋭意検討を重ねた結果、特定の条件下において超臨界水または亜臨界水に芳香族ジヒドロキシ化合物が溶解することに着目し、有機溶媒を使用しない効率的かつ経済的な芳香族ジヒドロキシ化合物の精製を達成するにいたった。 As a result of intensive studies to solve the above problems, the present inventors have paid attention to the fact that aromatic dihydroxy compounds are dissolved in supercritical water or subcritical water under specific conditions. To achieve an effective and economical purification of aromatic dihydroxy compounds.
すなわち、本発明は以下のとおりである。
1.超臨界水または亜臨界水に芳香族ジヒドロキシ化合物を、前記超臨界水または亜臨界水の誘電率が5以下となる範囲で溶解せしめ、次いで超臨界または亜臨界状態を解除して晶析させることを特徴とする芳香族ジヒドロキシ化合物の精製方法。
2.超臨界水または亜臨界水に芳香族ジヒドロキシ化合物が溶解した芳香族ジヒドロキシ化合物水溶液をろ過手段にすることを特徴とする芳香族ジヒドロキシ化合物の精製方法。
3.前記芳香族ジヒドロキシ化合物が下記式(1)
で表される芳香族ジヒドロキシ化合物である請求項1または2に記載の芳香族ジヒドロキシ化合物の精製方法。
4.前記芳香族ジヒドロキシ化合物が2,2−ビス(4−ヒドロキシフェニル)プロパンである芳香族ジヒドロキシ化合物の精製方法。
5.前記超臨界水または亜臨界水への芳香族ジヒドロキシ化合物の溶解を374℃以上500℃以下の温度範囲および18MPa以上40MPa以下の圧力範囲内で行なう芳香族ジヒドロキシ化合物の精製方法。
That is, the present invention is as follows.
1. Aromatic dihydroxy compound is dissolved in supercritical water or subcritical water in a range where the dielectric constant of the supercritical water or subcritical water is 5 or less, and then the supercritical or subcritical state is released and crystallized. A method for purifying an aromatic dihydroxy compound characterized by the following.
2. A method for purifying an aromatic dihydroxy compound, comprising using an aqueous solution of an aromatic dihydroxy compound in which an aromatic dihydroxy compound is dissolved in supercritical water or subcritical water as a filtering means.
3. The aromatic dihydroxy compound is represented by the following formula (1):
The method for purifying an aromatic dihydroxy compound according to claim 1, wherein the aromatic dihydroxy compound is represented by the formula:
4). A method for purifying an aromatic dihydroxy compound, wherein the aromatic dihydroxy compound is 2,2-bis (4-hydroxyphenyl) propane.
5 . Purification method of the preceding Symbol supercritical water or sub aromatic dihydroxy compound dissolved aromatic dihydroxy compound performing within the following pressure range 374 ° C. or higher 500 ° C. or less of the temperature range and 18MPa or 40MPa of the critical water.
上述のごとく、本発明によれば、環境に優しくかつ簡易的なプロセスで芳香族ジヒドロキシ化合物を精製し、樹脂原料として最適な高純度の芳香族ジヒドロキシ化合物を得ることができる。 As described above, according to the present invention, an aromatic dihydroxy compound can be purified by an environmentally friendly and simple process to obtain an aromatic dihydroxy compound having a high purity that is optimal as a resin raw material.
本発明は上記のとおりの特徴をもつ全く新規な芳香族ジヒドロキシ化合物の精製方法に関するものであるが、以下にその実施の形態を説明する。 The present invention relates to a completely novel method for purifying an aromatic dihydroxy compound having the characteristics as described above, and an embodiment thereof will be described below.
本発明はいかなる製法で得られた芳香族ジヒドロキシ化合物にも適用可能であるが、その製法としては、例えばヒドロキシ化合物とアセトンとの酸性触媒存在下における反応が挙げられる。また、本発明は原料からの合成ではなく樹脂の分解により得られた芳香族ジヒドロキシ化合物にも広く適用可能である。上記芳香族ジヒドロキシ化合物はいかなる不純物を含有していてもよいが、含有される不純物としては例えばフェノールを主とするヒドロキシ化合物、アセトン、高縮合度の縮合物を含む種々の副生物、無機塩、金属などが挙げられる。さらに、本発明に供する芳香族ジヒドロキシ化合物の形態は、プリルやフレーク、粉体など公知の形態のいずれでもよい。 The present invention can be applied to an aromatic dihydroxy compound obtained by any production method. Examples of the production method include a reaction of a hydroxy compound and acetone in the presence of an acidic catalyst. Further, the present invention can be widely applied to aromatic dihydroxy compounds obtained not by synthesis from raw materials but by decomposition of resins. The aromatic dihydroxy compound may contain any impurities. Examples of the impurities contained include hydroxy compounds mainly composed of phenol, acetone, various by-products including highly condensed condensates, inorganic salts, A metal etc. are mentioned. Furthermore, the form of the aromatic dihydroxy compound used in the present invention may be any of known forms such as prills, flakes, and powders.
本発明に供する芳香族ジヒドロキシ化合物は特に限定されるものではないが、下記式(1)
(ここで、R1、R2、R3およびR4は互いに独立に水素原子、炭素数1〜10のアルキル基、炭素数6〜10のアリール基または炭素数7〜10のアラルキル基またはハロゲン原子であり、そしてWは単結合、炭素数1〜10のアルキレン基、炭素数2〜10のアルキリデン基、炭素数6〜10のシクロアルキレン基、炭素数6〜10のシクロアルキリデン基、炭素数8〜15のアルキレン−アリーレン−アルキレン基、酸素原子、硫黄原子、スルホキシド基またはスルホン基である。)、
で表される繰り返し単位からなるものを好ましいものとして挙げることができる。
The aromatic dihydroxy compound used in the present invention is not particularly limited, but the following formula (1)
(Wherein R 1 , R 2 , R 3 and R 4 are each independently a hydrogen atom, an alkyl group having 1 to 10 carbon atoms, an aryl group having 6 to 10 carbon atoms, an aralkyl group having 7 to 10 carbon atoms, or a halogen atom) And W is a single bond, an alkylene group having 1 to 10 carbon atoms, an alkylidene group having 2 to 10 carbon atoms, a cycloalkylene group having 6 to 10 carbon atoms, a cycloalkylidene group having 6 to 10 carbon atoms, or a carbon number. 8 to 15 alkylene-arylene-alkylene group, oxygen atom, sulfur atom, sulfoxide group or sulfone group).
What consists of a repeating unit represented by these can be mentioned as a preferable thing.
炭素数1〜10のアルキル基は直鎖状であっても分岐鎖状であってもよい。その例としては、メチル、エチル、プロピル、ブチル、オクチル、デシル等を挙げることができる。炭素数6〜10のアリール基としては、例えばフェニル、トリル、クミル、ナフチル等を挙げることができる。炭素数7〜10のアラルキル基としては、例えばベンジル、2−フェネチル、2−メチル、2−フェニルエチル等を挙げることができる。
R1、R2、R3およびR4としては、互いに独立に、水素原子、メチル基およびt−ブチル基が好ましく、水素原子が特に好ましい。
The alkyl group having 1 to 10 carbon atoms may be linear or branched. Examples thereof include methyl, ethyl, propyl, butyl, octyl, decyl and the like. Examples of the aryl group having 6 to 10 carbon atoms include phenyl, tolyl, cumyl, naphthyl and the like. Examples of the aralkyl group having 7 to 10 carbon atoms include benzyl, 2-phenethyl, 2-methyl, 2-phenylethyl and the like.
As R 1 , R 2 , R 3 and R 4 , independently of each other, a hydrogen atom, a methyl group and a t-butyl group are preferable, and a hydrogen atom is particularly preferable.
また、Wの定義も下記のとおりである。
炭素数1〜10のアルキレン基は直鎖状であっても分岐鎖状であってもよい。その例としては、メチレン、1,2−エチレン、2,2−プロピレン、2,2−ブチレン、1,1−デシレン等を挙げることができる。
炭素数2〜10のアルキリデン基としては、例えばエチリデン、プロピリデン、ブチリデン、ヘキシリデン等を挙げることができる。
炭素数6〜10のシクロアルキレン基としては、例えば1,4−シクロヘキシレン、2−イソプロピル−1,4−シクロヘキシレン等を挙げることができる。
炭素数6〜10のシクロアルキリデン基としては、例えばシクロヘキシリデン、イソプロピルシクロヘキシリデン等を挙げることができる。
炭素数8〜15のアルキレン−アリーレン−アルキレン基としては、例えばm−ジイソプロピルフェニレン基などが挙げられる。
Wとしては、シクロヘキシリデン基、2,2−プロピリデン基が好ましく、2,2−プロピリデン基が特に好ましい。
The definition of W is also as follows.
The alkylene group having 1 to 10 carbon atoms may be linear or branched. Examples thereof include methylene, 1,2-ethylene, 2,2-propylene, 2,2-butylene, 1,1-decylene and the like.
Examples of the alkylidene group having 2 to 10 carbon atoms include ethylidene, propylidene, butylidene, and hexylidene.
Examples of the cycloalkylene group having 6 to 10 carbon atoms include 1,4-cyclohexylene and 2-isopropyl-1,4-cyclohexylene.
Examples of the cycloalkylidene group having 6 to 10 carbon atoms include cyclohexylidene and isopropylcyclohexylidene.
Examples of the alkylene-arylene-alkylene group having 8 to 15 carbon atoms include m-diisopropylphenylene group.
W is preferably a cyclohexylidene group or a 2,2-propylidene group, and particularly preferably a 2,2-propylidene group.
かかる芳香族ジヒドロキシ化合物の具体例としては、2,2−ビス(4−ヒドロキシフェニル)プロパン(すなわちBPA)、ビス(4−ヒドロキシフェニル)メタン、1,1−ビス(4’−ヒドロキシフェニル)エタン、1,2−ビス(4’−ヒドロキシフェニル)エタン、ビス(4−ヒドロキシフェニル)フェニルメタン、1,1−ビス(4’−ヒドロキシフェニル)−1−フェニルエタン、2−(4’−ヒドロキシフェニル)−2−(3’−ヒドロキシフェニル)プロパン、2,2−ビス(4’−ヒドロキシフェニル)ブタン、1,1−ビス(4’−ヒドロキシフェニル)イソブタンおよび4,4’−ジヒドロキシジフェニル等が挙げられる。 Specific examples of such aromatic dihydroxy compounds include 2,2-bis (4-hydroxyphenyl) propane (ie BPA), bis (4-hydroxyphenyl) methane, 1,1-bis (4′-hydroxyphenyl) ethane. 1,2-bis (4′-hydroxyphenyl) ethane, bis (4-hydroxyphenyl) phenylmethane, 1,1-bis (4′-hydroxyphenyl) -1-phenylethane, 2- (4′-hydroxy) Phenyl) -2- (3′-hydroxyphenyl) propane, 2,2-bis (4′-hydroxyphenyl) butane, 1,1-bis (4′-hydroxyphenyl) isobutane, 4,4′-dihydroxydiphenyl, etc. Is mentioned.
次に、本発明において使用する超臨界水または亜臨界水について説明する。超臨界流体とは臨界温度、臨界圧力を超えた状態の物質を示し、超臨界水とは臨界温度374℃以上、臨界圧力22MPa以上の水を示す。また、本発明において亜臨界水とは温度350℃以上かつ圧力18MPa以上であって、超臨界状態ではない水を示す。超臨界または亜臨界状態の水は、その温度・圧力に対応して密度、イオン積、イオン濃度、誘電率等の諸物性値が幅広く変動することが知られており、これらを容易に制御することが可能である。この結果、超臨界水または亜臨界水の物質の溶解力が極めて大きな範囲で変化し、溶質分子にとっては溶媒を交換したのに匹敵する効果をもたらす。さらに、超臨界水または亜臨界水は粘度が液体に比べて小さいため物質の拡散が速く、超臨界水または亜臨界水中での反応は通常の液体中の反応に比べて拡散律速になりにくいという利点もある。また、実用的な側面から見ると、水は最も安価である上、無毒、難燃性であり環境への負荷が少なく、熱安定性に富み、酸化もされない、理想的な溶媒であるといえる。 Next, the supercritical water or subcritical water used in the present invention will be described. The supercritical fluid indicates a substance in a state exceeding the critical temperature and the critical pressure, and the supercritical water indicates water having a critical temperature of 374 ° C. or higher and a critical pressure of 22 MPa or higher. In the present invention, subcritical water refers to water that is at a temperature of 350 ° C. or higher and a pressure of 18 MPa or higher and is not in a supercritical state. Supercritical or subcritical water is known to vary widely in physical properties such as density, ion product, ion concentration, dielectric constant, etc., depending on its temperature and pressure, and these are easily controlled. It is possible. As a result, the dissolving power of the substance of supercritical water or subcritical water changes within a very large range, and the solute molecules have an effect comparable to that of exchanging the solvent. Furthermore, supercritical water or subcritical water has a lower viscosity than liquid, so the diffusion of substances is faster, and the reaction in supercritical water or subcritical water is less likely to be diffusion-controlled than the reaction in normal liquid. There are also advantages. From a practical point of view, water is the cheapest, non-toxic, flame retardant, less burden on the environment, excellent in thermal stability, and is not ideally oxidized. .
本発明における超臨界水または亜臨界水への芳香族ジヒドロキシ化合物の溶解は、超臨界水または亜臨界水の誘電率が10以下である範囲内で行うことが好ましく、より好ましくは5以下であることが好ましい。誘電率は物質内で電荷とそれによって与えられる力との関係を示す係数であり、溶媒の極性の指標となる。室温での水の誘電率は約80と非常に大きいため、電解質等の無機物はよく溶けるが、有機物はほとんど溶解しない。しかし温度を上げると誘電率は徐々に低下し、374℃以上の超臨界水または亜臨界水では10程度と極性の小さな有機溶媒並の値になる。その結果、有機物はよく溶けるが無機物はほとんど溶けないという、通常の水とは逆の現象が起こる。本発明においては、誘電率を10以下とすることで芳香族ジヒドロキシ化合物の超臨界水への溶解度を向上させることができる。誘電率が10以上であると、芳香族ジヒドロキシ化合物の溶解度が低下し熱分解が進行してしまうため好ましくない。 The dissolution of the aromatic dihydroxy compound in the supercritical water or subcritical water in the present invention is preferably performed within the range where the dielectric constant of the supercritical water or subcritical water is 10 or less, more preferably 5 or less. It is preferable. The dielectric constant is a coefficient indicating the relationship between the electric charge in the substance and the force applied thereby, and is an index of the polarity of the solvent. Since the dielectric constant of water at room temperature is as large as about 80, inorganic substances such as electrolytes dissolve well, but organic substances hardly dissolve. However, when the temperature is raised, the dielectric constant gradually decreases, and in the case of supercritical water or subcritical water at 374 ° C. or higher, the value is about 10 and the value of an organic solvent having a small polarity. As a result, a phenomenon opposite to that of normal water occurs in which organic matter dissolves well but inorganic matter hardly dissolves. In the present invention, the solubility of the aromatic dihydroxy compound in supercritical water can be improved by setting the dielectric constant to 10 or less. A dielectric constant of 10 or more is not preferable because the solubility of the aromatic dihydroxy compound decreases and thermal decomposition proceeds.
さらに本発明における超臨界水または亜臨界水への芳香族ジヒドロキシ化合物の溶解は、超臨界水または亜臨界水の温度が前記臨界温度である374℃以上500℃以下で行うことが好ましく、より好ましくは430℃以下が好ましい。温度が374℃以下であると、超臨界水の誘電率が急激に上昇し、芳香族ジヒドロキシ化合物の溶解度が減少するため好ましくない。また500℃以上であると、芳香族ジヒドロキシ化合物の熱分解反応が進行して副生成物であるヒドロキシ化合物やその誘導体の生成を併発し、得られる芳香族ジヒドロキシ化合物の純度低下や着色を引き起こす恐れがあるため好ましくない。 Furthermore, the dissolution of the aromatic dihydroxy compound in supercritical water or subcritical water in the present invention is preferably performed at a temperature of supercritical water or subcritical water of 374 ° C. or higher and 500 ° C. or lower, which is the critical temperature. Is preferably 430 ° C. or lower. A temperature of 374 ° C. or lower is not preferable because the dielectric constant of supercritical water increases rapidly and the solubility of the aromatic dihydroxy compound decreases. Further, if the temperature is 500 ° C. or higher, the thermal decomposition reaction of the aromatic dihydroxy compound proceeds and the generation of the by-product hydroxy compound or its derivative is caused, which may cause a decrease in purity or coloring of the obtained aromatic dihydroxy compound. This is not preferable.
また、圧力条件は18MPa以上40MPa以下で行うことが好ましく、より好ましくは20MPa以上30MPa以下が好ましい。圧力が40MPa以上であると、工業プロセスにおいて多量なエネルギーコストを要し、安全面、経済面において多大な負荷がかかるため、好ましくない。また、18MPa以下であると前述の亜臨界水特有の諸物性が発現しにくくなるため、好ましくない。 The pressure condition is preferably 18 MPa or more and 40 MPa or less, more preferably 20 MPa or more and 30 MPa or less. When the pressure is 40 MPa or more, a large amount of energy cost is required in an industrial process, and a great load is imposed on safety and economy, which is not preferable. On the other hand, if it is 18 MPa or less, the physical properties peculiar to the above-mentioned subcritical water are difficult to be expressed.
本発明における反応時間は特に限定されるものではないが、上記条件において5分以下という非常に短時間で芳香族ジヒドロキシ化合物を溶解することができる。溶解時間を延ばすとジヒドロキシ化合物の分解が進行して純度が低下する上、工業プロセスにおいては単位時間当たりの処理量が少なくなる、または容器の容積が大きくなるため、好ましくない。 The reaction time in the present invention is not particularly limited, but the aromatic dihydroxy compound can be dissolved in a very short time of 5 minutes or less under the above conditions. Prolonging the dissolution time is not preferable because the decomposition of the dihydroxy compound proceeds to lower the purity, and the processing amount per unit time decreases or the volume of the container increases in an industrial process.
本発明の実施の形態は、流通式、半回分式、またはバッチ式反応器の何れでも良いが、流通式を用いると処理量を増やすことができ、好ましい。また、超臨界水または亜臨界水への無機塩の溶解度は非常に低いため、超臨界水または亜臨界水に芳香族ヒドロキシ化合物が溶解した芳香族ジヒドロキシ化合物水溶液をろ過手段に供することにより、無機不純物の除去を行なうことが可能である。ろ過方法は特に限定されないが、例えばメンブランフィルター、ろ紙、焼結フィルターなどのろ材を使用することができる。また、該ろ過処理により、超臨界水に不溶な鉱物等、無機塩以外の異物も除去される。 The embodiment of the present invention may be any of a flow type, a semi-batch type, or a batch type reactor, but the use of the flow type is preferable because the throughput can be increased. In addition, since the solubility of inorganic salts in supercritical water or subcritical water is very low, an inorganic dihydroxy compound aqueous solution in which an aromatic hydroxy compound is dissolved in supercritical water or subcritical water is used as a filtration means. It is possible to remove impurities. Although the filtration method is not particularly limited, for example, a filter medium such as a membrane filter, a filter paper, and a sintered filter can be used. Moreover, foreign substances other than inorganic salts, such as a mineral insoluble in supercritical water, are removed by the filtration treatment.
超臨界水または亜臨界水に溶解した芳香族ジヒドロキシ化合物は、必要に応じて上記ろ過手段を通過させた後、超臨界状態を解除することで容易に晶析、回収することができる。超臨界状態の解除とは温度・圧力をそれぞれ臨界点以下の任意の温度圧力に下げることで行なわれ、例えば常温常圧まで低下させれば良く、良溶媒からの晶析操作として広く用いられる貧溶媒の添加は一切不要である。また、必要に応じて冷却等の公知の晶析操作を併用することも可能である。 The aromatic dihydroxy compound dissolved in supercritical water or subcritical water can be easily crystallized and recovered by releasing the supercritical state after passing through the filtration means as necessary. The release of the supercritical state is performed by lowering the temperature and pressure to any temperature pressure below the critical point. For example, it can be lowered to room temperature and normal pressure, and it is a poorly used crystallization operation from a good solvent. No addition of solvent is necessary. In addition, a known crystallization operation such as cooling can be used in combination as required.
本発明により精製された芳香族ジヒドロキシ化合物は他の方法で精製された芳香族ジヒドロキシ化合物に比べて溶媒残存量が低く、純度が高く、かつ着色度が低いという特長を有し、これをポリカーボネート樹脂、エポキシ樹脂、ポリカーボネートのコンパウンド樹脂、その他樹脂の原料として用いることにより、高品質の樹脂を得ることができる。 The aromatic dihydroxy compound purified by the present invention has the features that the residual solvent amount is low, the purity is high, and the coloring degree is low compared with the aromatic dihydroxy compound purified by other methods. High-quality resins can be obtained by using as raw materials for epoxy resins, polycarbonate compound resins, and other resins.
以下、実施例により本発明を更に具体的に説明するが、本発明はこれにより何等限定を受けるものではない。 Hereinafter, the present invention will be described more specifically with reference to examples, but the present invention is not limited thereto.
[実施例1]
全内容積6mLのSUS316製チューブ型反応管に、ポリカーボネートの加水分解により得られた粗BPA0.1gを入れ、圧力が25MPaとなるように水1.1gを仕込み、密閉した。反応管内をアルゴン置換して不活性雰囲気とした後、400℃に予熱したサンドバス中に浸漬させ、3分間保持した。ここで、上記条件における比誘電率=2であった。その後、反応管を水に浸漬させて室温まで急冷し、内容物をガラス瓶に取り出したところ、20℃0.1MPaの温度圧力条件下にて無色のBPA針状結晶の析出が見られた。
上記結晶を回収してジエチルエーテルに溶解し、この溶液をガスクロマトグラフィー(HP5890)により分析したところ、上記BPAの純度は99%であることが確認された。
[Example 1]
In a tube-type reaction tube made of SUS316 having a total internal volume of 6 mL, 0.1 g of crude BPA obtained by hydrolysis of polycarbonate was charged, and 1.1 g of water was charged so that the pressure became 25 MPa, followed by sealing. After the inside of the reaction tube was replaced with argon to make an inert atmosphere, it was immersed in a sand bath preheated to 400 ° C. and held for 3 minutes. Here, the relative dielectric constant in the above condition = 2. Thereafter, the reaction tube was immersed in water and rapidly cooled to room temperature, and the contents were taken out into a glass bottle. As a result, colorless BPA needle crystals were observed under a temperature and pressure condition of 20 ° C. and 0.1 MPa.
The crystals were collected and dissolved in diethyl ether, and this solution was analyzed by gas chromatography (HP5890). As a result, it was confirmed that the purity of the BPA was 99%.
[比較例1]
反応管に、ポリカーボネートの加水分解により得られた粗BPA0.1gを入れ、圧力が30MPaとなるように水4.8gを仕込み、密閉した。反応管内をアルゴン置換して不活性雰囲気とした後、270℃に予熱したサンドバス中に浸漬させ、30分間保持した。ここで、上記条件における比誘電率=25であった。その後、反応管を水に浸漬させて室温まで急冷し、内容物をガラス瓶に取り出したところ、内容物は褐色に着色していた。
内容物を実施例1と同様にジエチルエーテルに溶解し、ガスクロマトグラフィーで分析したところ、BPAの二次分解によるフェノール、イソプロピルフェノールなどの生成が確認され、好ましくないことが分かった。
[Comparative Example 1]
The reaction tube was charged with 0.1 g of crude BPA obtained by hydrolysis of polycarbonate, charged with 4.8 g of water so that the pressure was 30 MPa, and sealed. After the inside of the reaction tube was replaced with argon to make an inert atmosphere, it was immersed in a sand bath preheated to 270 ° C. and held for 30 minutes. Here, the relative dielectric constant under the above conditions was 25. Then, when the reaction tube was immersed in water and rapidly cooled to room temperature, the content was taken out into a glass bottle, and the content was colored brown.
The contents were dissolved in diethyl ether in the same manner as in Example 1 and analyzed by gas chromatography. As a result, formation of phenol, isopropylphenol, and the like due to secondary decomposition of BPA was confirmed, which proved undesirable.
Claims (5)
で表される芳香族ジヒドロキシ化合物である請求項1または2に記載の芳香族ジヒドロキシ化合物の精製方法。 The aromatic dihydroxy compound is represented by the following formula (1):
The method for purifying an aromatic dihydroxy compound according to claim 1, wherein the aromatic dihydroxy compound is represented by the formula:
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