JPH1112223A - High-purity terephthalic acid and its recovery - Google Patents

High-purity terephthalic acid and its recovery

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Publication number
JPH1112223A
JPH1112223A JP16860597A JP16860597A JPH1112223A JP H1112223 A JPH1112223 A JP H1112223A JP 16860597 A JP16860597 A JP 16860597A JP 16860597 A JP16860597 A JP 16860597A JP H1112223 A JPH1112223 A JP H1112223A
Authority
JP
Japan
Prior art keywords
terephthalic acid
purity
acid
resin waste
aqueous solution
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.)
Pending
Application number
JP16860597A
Other languages
Japanese (ja)
Inventor
Hirotaka Amimoto
博孝 網本
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.)
Unitika Ltd
Original Assignee
Unitika 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 Unitika Ltd filed Critical Unitika Ltd
Priority to JP16860597A priority Critical patent/JPH1112223A/en
Publication of JPH1112223A publication Critical patent/JPH1112223A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide terephthalic acid of high purity that is obtained from PET resin waste and can be used at the equal level to the virgin terephthalic acid. SOLUTION: Resin waste mainly comprising polyethylene terephthalate and contains foreign contaminants is hydrolyzed in the presence of an alkali. An acid is added to the resultant hydrolyze aqueous solution to adjust its pH to 3.5-9 to precipitate foreign substances, further the pH is lowered less than 3 to precipitate terephthalic acid whereby high-purity terephthalic acid is obtained that has 97% or higher purity according to high-performance liquid chromatography.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、異物混合されたポ
リエチレンテレフタレートを主成分とする樹脂廃棄物
(以下「PET樹脂廃棄物」という。)、中でも分別収
集されたPETボトルを再生処理して得られた高純度テ
レフタル酸及びその回収法に関する。
[0001] The present invention relates to a resin waste containing polyethylene terephthalate as a main component mixed with foreign substances (hereinafter referred to as "PET resin waste"), in particular, a PET bottle collected and sorted by recycling. And a method for recovering the same.

【0002】[0002]

【従来の技術】PET樹脂廃棄物、中でも分別収集され
たPETボトルに代表される産業廃棄物の再生方法とし
ては、主にフレーク状で種々の用途に加工するマテリア
ルリサイクルと、化学処理を行ってモノマーにして再使
用するケミカルリサイクルとがある。
2. Description of the Related Art As a method of regenerating PET resin waste, especially industrial waste represented by separately collected PET bottles, a material recycling process mainly for flakes for various uses and a chemical treatment are carried out. There is chemical recycling to reuse as monomers.

【0003】ケミカルリサイクルは、水、メタノール、
エチレングリコール等の溶媒を用いてモノマーに加溶媒
分解する方法である。この方法は、PET樹脂のエステ
ル基を分解させてモノマーを生成させ、溶媒に溶解させ
て分離するものであるが、異物を含有している場合に
は、異物の種類によっては溶媒と反応したり、溶媒に溶
解したりして、必ずしもモノマーと分離できない場合が
ある。
[0003] Chemical recycling consists of water, methanol,
This is a method of solvolysis to a monomer using a solvent such as ethylene glycol. In this method, the ester group of the PET resin is decomposed to generate a monomer, which is then dissolved in a solvent and separated. However, when a foreign substance is contained, it reacts with the solvent depending on the type of the foreign substance. Or it may not always be separated from the monomer by dissolution in a solvent.

【0004】また、水を溶媒として、PET樹脂廃棄物
をアルカリの存在下に加水分解する場合も同様である。
この際、PET樹脂はテレフタル酸ナトリウムとエチレ
ングリコールとに分解されて水に溶解するが、異物とし
て混入されたものは、水にそのまま溶解したり、アルカ
リと反応して水に溶解したり、あるいは加水分解時の熱
で分解して水に溶解したりする。このため、回収しよう
とするモノマーと異物とが混在することになり、モノマ
ーを分離分離できない場合がある。
The same applies to the case where PET resin waste is hydrolyzed in the presence of an alkali using water as a solvent.
At this time, the PET resin is decomposed into sodium terephthalate and ethylene glycol and dissolved in water, but the one mixed as a foreign substance is directly dissolved in water, or dissolved in water by reacting with an alkali, or It decomposes with the heat of hydrolysis and dissolves in water. For this reason, the monomer to be recovered and the foreign matter are mixed, and the monomer cannot be separated and separated in some cases.

【0005】分別収集されたPETボトルを例にとる
と、付着している内容物のように水にそのまま溶解する
もの、アルミキャップのようにアルカリと反応して水に
溶解するもの、ラベルの染料や顔料のように水に溶解し
たり微粉で分散したりするもの、さらには一部の接着剤
のように熱分解を起こして水に溶解するもの等がある。
したがって、これら異物の除去の程度によって、モノマ
ーの純度や回収率等が大きく影響を受けることになる。
Taking PET bottles collected separately, for example, those which dissolve in water as they are attached, those which dissolve in water by reacting with alkali such as aluminum caps, dyes for labels Examples thereof include those that dissolve in water or disperse in fine powder like pigments and pigments, and those that dissolve in water by causing thermal decomposition such as some adhesives.
Therefore, the degree of removal of these foreign substances greatly affects the purity and recovery rate of the monomer.

【0006】上記した加水分解によるPET樹脂廃棄物
のケミカルリサイクルにおいては、加水分解により水に
溶解するような異物を前もって除去してから、加水分解
を行うことが一般的に行われているが、この異物を除去
する分離操作は、非常に繁雑になるという問題があっ
た。
[0006] In the chemical recycling of PET resin waste by the above-mentioned hydrolysis, it is common practice to carry out hydrolysis after removing foreign substances which are soluble in water by hydrolysis in advance. There is a problem that the separation operation for removing the foreign matter becomes very complicated.

【0007】[0007]

【発明が解決しようとする課題】本発明は、このような
問題点を解決するためになされたもので、PET樹脂廃
棄物より得られ、パージンのテレフタル酸と同等レベル
で使用できる高純度テレフタル酸及びその回収法を提供
するものである。
DISCLOSURE OF THE INVENTION The present invention has been made to solve such problems, and it is intended to obtain high-purity terephthalic acid obtained from PET resin waste and usable at the same level as terephthalic acid of pergin. And a method for recovering the same.

【0008】[0008]

【課題を解決するための手段】本発明者は、そこで鋭意
研究を重ねた結果、PET樹脂廃棄物をアルカリの存在
下に加水分解して得られたテレフタル酸ナトリウム水溶
液に、酸を加えてテレフタル酸として析出させるとき
に、予め前記水溶液のpHを弱酸性〜中性域に調整して
異物除去をした後、前記水溶液のpHを酸性域にすると
高純度のテレフタル酸を回収できることを見い出した。
Means for Solving the Problems The inventor of the present invention has conducted intensive studies, and as a result, obtained by adding an acid to an aqueous solution of sodium terephthalate obtained by hydrolyzing PET resin waste in the presence of an alkali, adding terephthalate. It has been found that when precipitating as an acid, the pH of the aqueous solution is adjusted in advance to a weakly acidic to neutral range to remove foreign substances, and then, when the pH of the aqueous solution is adjusted to an acidic range, terephthalic acid of high purity can be recovered.

【0009】すなわち、本発明の要旨は次の通りであ
る。 (1) PET樹脂廃棄物から回収されたテレフタル酸であ
って、高速液体クロマトグラフィーより求めた純度が97
%以上であることを特徴とする高純度テレフタル酸。 (2) PET樹脂廃棄物をアルカリ存在下に加水分解して
得られた水溶液に、酸を加えてpHを 3.5〜9に調整し
て異物を析出させて分離した後、さらにpHを3以下に
調整してテレフタル酸を析出させることを特徴とする上
記(1) に記載の高純度テレフタル酸の回収法。
That is, the gist of the present invention is as follows. (1) Terephthalic acid recovered from PET resin waste and having a purity determined by high performance liquid chromatography of 97
% Of high-purity terephthalic acid. (2) Acid is added to an aqueous solution obtained by hydrolyzing PET resin waste in the presence of alkali to adjust the pH to 3.5 to 9 to precipitate and separate foreign substances, and the pH is further reduced to 3 or less. The method for recovering high-purity terephthalic acid according to the above (1), characterized in that terephthalic acid is precipitated by adjustment.

【0010】[0010]

【発明の実施の形態】以下、本発明について詳細に説明
する。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail.

【0011】本発明におけるPET樹脂廃棄物には、自
治体等により分別収集されたPETボトル、オーディオ
テープやプリペイドカード等のようなPET樹脂と異物
との複合物、あるいは産業廃棄物としてのPET樹脂廃
棄物等が挙げられるが、分別収集されたPETボトルを
用いると、より高純度のテレフタル酸が得られる点で好
ましい。
The PET resin waste according to the present invention includes PET bottles collected separately by local governments, composites of PET resin and foreign matter such as audio tapes and prepaid cards, or PET resin waste as industrial waste. Although it is preferable to use a separately collected PET bottle, terephthalic acid with higher purity can be obtained.

【0012】次に、高純度テレフタル酸の回収法につい
て説明する。本発明の方法においては、まず初めに、P
ET樹脂廃棄物をアルカリ存在下に加水分解して水溶液
とする。ここで、アルカリ存在下に加水分解するとは、
アルカリ剤として苛性ソーダや水酸化カリウムを用いて
加水分解を行うものである。そして、得られた水溶液中
には、テレフタル酸ナトリウムやエチレングリコール、
反応残余の水やアルカリの他に、通常は異物の溶解物等
が含まれており、場合によっては、顔料等の微粉化され
たろ過が困難である懸濁物が含まれていることもある。
Next, a method for recovering high-purity terephthalic acid will be described. In the method of the present invention, first, P
ET resin waste is hydrolyzed in the presence of an alkali to form an aqueous solution. Here, the hydrolysis in the presence of an alkali means
The hydrolysis is carried out using caustic soda or potassium hydroxide as an alkaline agent. And in the obtained aqueous solution, sodium terephthalate, ethylene glycol,
In addition to the residual water and alkali remaining in the reaction, they usually contain dissolved substances of foreign substances, and in some cases, may contain finely divided suspensions such as pigments that are difficult to filter. .

【0013】次に、上記の水溶液に、酸を加えてpHを
3.5〜9、好ましくはpHを 4.5〜7に調整して異物を
析出させる。この際、酸としては、硫酸、塩酸、硝酸等
の鉱酸の他に、酢酸等の有機酸が好適に使用できる。ま
た、酸を加えるに先立って、水溶液に高分子凝集剤を少
量添加することで、水溶液中に含有されているアルミの
溶解物や懸濁状の微粉や有機性の異物等を効率よく除去
できる。
Next, an acid is added to the above aqueous solution to adjust the pH.
The pH is adjusted to 3.5 to 9, preferably 4.5 to 7, to deposit foreign matter. In this case, as the acid, an organic acid such as acetic acid can be suitably used in addition to a mineral acid such as sulfuric acid, hydrochloric acid, and nitric acid. In addition, prior to the addition of the acid, by adding a small amount of a polymer flocculant to the aqueous solution, it is possible to efficiently remove aluminum dissolved substances, suspended fine powder, organic foreign substances, and the like contained in the aqueous solution. .

【0014】そして最後に、上記の異物が析出分離され
た水溶液に、さらに酸を加えてpHを3以下、好ましく
はpHを2〜2.5 に調整してテレフタル酸を析出させ
る。この際、酸としては、異物を析出分離させるのに用
いた酸と同一の酸もしくは異種の酸のいずれをも好適に
使用することができる。さらに、数種の酸の混合物も用
いてもよい。
Finally, an acid is further added to the aqueous solution from which the foreign substances have been separated and separated to adjust the pH to 3 or less, preferably to 2 to 2.5 to precipitate terephthalic acid. At this time, as the acid, either the same acid as the acid used for separating and separating the foreign substance or a different acid can be suitably used. Furthermore, mixtures of several acids may be used.

【0015】また、上記した回収工程において、PET
樹脂廃棄物をアルカリ存在下に加水分解して得られた水
溶液を活性炭処理した後、この処理液に酸を加えてpH
を 3.5〜9に調整して異物を析出させると、より着色の
少ないテレフタル酸を得ることができる。
In the above-mentioned recovery step, PET is used.
After an aqueous solution obtained by hydrolyzing resin waste in the presence of alkali is treated with activated carbon, an acid is added to the treated solution to adjust the pH.
Is adjusted to 3.5 to 9 to deposit foreign matter, terephthalic acid with less coloring can be obtained.

【0016】上記のようにして析出されたテレフタル酸
は、ろ過操作によって分離し、水洗、乾燥工程等を経
て、異物の少ない高純度のテレフタル酸が得られる。
The terephthalic acid thus precipitated is separated by a filtration operation, washed with water, dried, and the like to obtain high-purity terephthalic acid with few foreign substances.

【0017】このようにして得られたテレフタル酸は、
高速液体クロマトグラフィー(HPLC)より求めた純
度が97%以上、通常は98%以上であり、パージンのテレ
フタル酸と同等レベルで使用できるものである。
The terephthalic acid thus obtained is
The purity determined by high performance liquid chromatography (HPLC) is 97% or more, usually 98% or more, and it can be used at the same level as terephthalic acid of pergin.

【0018】[0018]

【実施例】以下、実施例により本発明をさらに具体的に
説明する。なお、実施例及び比較例で用いた測定法は次
の通りである。 1.測定法 (a) テレフタル酸の純度(%) 高速液体クロマトグラフ(ウォーターズ社製、600E)を
用いてテレフタル酸の純度を算定した。なお、高速液体
クロマトグラフ測定は、次の条件で行い、式より算定
した。 検出器:PDA(フォト・ダイオード・アレイ) カラム:Waters μ Bondasphere 5μ C18−100A カラム温度:40℃ 対象リテンションタイム:0〜1.9 分 テレフタル酸対象ピーク:リテンションタイム 0.9分
近傍の単一ピーク 不純物:対象リテンションタイムの間のピーク(ただ
し、マイナスピークについては除外した。) 純度(%)=(の面積)/(の面積+の面積)
×100 (b) テレフタル酸の回収率(%) 下記表1の組成分析例のPET比率から算定した。
The present invention will be described more specifically with reference to the following examples. The measuring methods used in Examples and Comparative Examples are as follows. 1. Measurement method (a) Purity of terephthalic acid (%) The purity of terephthalic acid was calculated using a high performance liquid chromatograph (600E, manufactured by Waters). The high-performance liquid chromatograph measurement was performed under the following conditions, and was calculated from the equation. Detector: PDA (photodiode array) Column: Waters μ Bondasphere 5μ C18-100A Column temperature: 40 ° C Target retention time: 0 to 1.9 minutes Terephthalic acid Target peak: Retention time Single peak near 0.9 minutes Impurity: Target Peak during the retention time (excluding negative peaks) Purity (%) = (area of) / (area of + area of)
× 100 (b) Recovery rate of terephthalic acid (%) Calculated from the PET ratio of the composition analysis example in Table 1 below.

【0019】参考例1(PET樹脂廃棄物の組成分析
例) 自治体により分別収集されたPETボトルを、9mmスク
リーンを通過するように湿式破砕したものの組成分析例
を表1に示す。
Reference Example 1 (Example of composition analysis of PET resin waste) Table 1 shows an example of composition analysis of PET bottles collected and sorted by a local government and wet-crushed so as to pass through a 9 mm screen.

【0020】[0020]

【表1】 [Table 1]

【0021】実施例1 参考例1のPET樹脂廃棄物 500gと30重量%苛性ソー
ダ水溶液 700gとを内容積2リットルのオートクレーブ
に入れ、窒素置換後加熱し、150 ℃に6時間保持した
後、自然冷却させ、内温が40℃以下になってから内容物
を払い出した。この内容物をろ紙でろ別後、残渣をろ過
により除去したところ、1130gの水溶液が得られた。こ
の水溶液 200gを取り、攪拌しながら5重量%の硫酸を
少しずつ添加してpHを6.5 に調整した。このときに灰
褐色の沈殿が析出したのでこれをろ別し、さらにこの水
溶液に5重量%の硫酸を少しずつ添加してpHを 2.5に
調整したところ、白色のテレフタル酸が析出した。次い
で、ろ過、水洗、乾燥の工程を経てテレフタル酸66.3g
を単離した。このテレフタル酸の純度をHPLCより測
定した結果、純度97.8%であった。また、テレフタル酸
の回収率は97.5%であった。さらに、このテレフタル酸
を用いて、常法により重縮合したところ、バージンのテ
レフタル酸を用いた場合と同等レベルのPETが得られ
た。
Example 1 500 g of the PET resin waste of Reference Example 1 and 700 g of a 30% by weight aqueous solution of caustic soda were placed in an autoclave having an internal volume of 2 liters, replaced with nitrogen, heated, kept at 150 ° C. for 6 hours, and then naturally cooled. The contents were discharged when the internal temperature became 40 ° C. or less. After the content was filtered off with a filter paper, the residue was removed by filtration, whereby 1130 g of an aqueous solution was obtained. 200 g of this aqueous solution was taken, and 5% by weight of sulfuric acid was added little by little with stirring to adjust the pH to 6.5. At this time, a grey-brown precipitate was deposited. This was filtered off, and 5% by weight of sulfuric acid was gradually added to the aqueous solution to adjust the pH to 2.5, whereby white terephthalic acid was deposited. Next, terephthalic acid 66.3 g through the steps of filtration, washing and drying
Was isolated. As a result of measuring the purity of this terephthalic acid by HPLC, the purity was 97.8%. The recovery of terephthalic acid was 97.5%. Furthermore, when polycondensation was carried out using this terephthalic acid by a conventional method, PET at a level equivalent to that obtained when virgin terephthalic acid was used was obtained.

【0022】実施例2 実施例1で用いた水溶液 200gを取り、攪拌しながら高
分子凝集剤ユニフロッカーUF 105(ユニチカ社製)を
4mg/lとなるように添加してから、5重量%の硫酸を少
しずつ添加してpHを 5.0に調整した。このときに析出
した灰褐色の成分を分離除去後の残存液に、5重量%の
硫酸/酢酸の等量混合液を少しずつ添加てpHを 2.5に
調整したところ、白色のテレフタル酸が析出した。次い
で、ろ過、水洗、乾燥の工程を経てテレフタル酸66.0g
を単離した。このテレフタル酸の純度をHPLCより測
定した結果、純度98.8%であった。また、テレフタル酸
の回収率は97.0%であった。さらに、このテレフタル酸
を用いて、常法により重縮合したところ、バージンのテ
レフタル酸を用いた場合と同等レベルのPETが得られ
た。
Example 2 200 g of the aqueous solution used in Example 1 was taken, and a polymer flocculant Uniflocker UF 105 (manufactured by Unitika) was added thereto with stirring at a concentration of 4 mg / l. The pH was adjusted to 5.0 by adding sulfuric acid little by little. A 5% by weight mixture of sulfuric acid / acetic acid was added little by little to the remaining liquid after separation and removal of the grey-brown components precipitated at this time, and the pH was adjusted to 2.5 by little. As a result, white terephthalic acid was precipitated. . Then, through the steps of filtration, washing and drying, 66.0 g of terephthalic acid
Was isolated. As a result of measuring the purity of this terephthalic acid by HPLC, the purity was 98.8%. The recovery of terephthalic acid was 97.0%. Furthermore, when polycondensation was carried out using this terephthalic acid by a conventional method, PET at a level equivalent to that obtained when virgin terephthalic acid was used was obtained.

【0023】比較例1 実施例1で用いた水溶液 200gを取り、攪拌しながら5
重量%の硫酸を少しずつ添加してpHを 2.5に調整した
ところ、灰色のテレフタル酸が析出した。次いで、ろ
過、水洗、乾燥の工程を経てテレフタル酸62.8gを単離
した。このテレフタル酸の純度をHPLCより測定した
結果、純度96.6%であり、異物を 3.4%含むものであっ
た。また、異物の成分にはケイ素をはじめアルミ、鉄等
の無機成分が検出された。また、テレフタル酸の回収率
は、92.4%であった。さらに、このテレフタル酸を用い
て、常法により重縮合したところ、バージンのテレフタ
ル酸を用いた場合と同等レベルのPETは得られなかっ
た。
Comparative Example 1 200 g of the aqueous solution used in Example 1 was taken, and stirred for 5 minutes.
When the pH was adjusted to 2.5 by gradually adding wt% sulfuric acid, gray terephthalic acid was precipitated. Next, 62.8 g of terephthalic acid was isolated through the steps of filtration, washing and drying. The purity of this terephthalic acid was measured by HPLC. As a result, the purity was 96.6%, and it contained 3.4% of foreign substances. In addition, inorganic components such as aluminum, iron, etc., including silicon, were detected as components of the foreign matter. The recovery of terephthalic acid was 92.4%. Further, when polycondensation was performed using this terephthalic acid by a conventional method, PET at the same level as when virgin terephthalic acid was used was not obtained.

【0024】[0024]

【発明の効果】本発明によれば、パージンのテレフタル
酸と同等レベルで使用できる高純度テレフタル酸をPE
T樹脂廃棄物より得ることができ、これらはボトル用原
料、繊維用原料、フィルム用原料、原料中間体等として
好適に利用できるものである。
According to the present invention, high-purity terephthalic acid which can be used at the same level as terephthalic acid of perzine is made of PE
It can be obtained from T resin waste, and these can be suitably used as bottle raw materials, fiber raw materials, film raw materials, raw material intermediates, and the like.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 異物混合されたポリエチレンテレフタレ
ートを主成分とする樹脂廃棄物から回収されたテレフタ
ル酸であって、高速液体クロマトグラフィーより求めた
純度が97%以上であることを特徴とする高純度テレフタ
ル酸。
1. High-purity terephthalic acid recovered from resin waste containing polyethylene terephthalate as a main component and having a foreign substance content of 97% or more, as determined by high performance liquid chromatography. Terephthalic acid.
【請求項2】 前記異物混合されたポリエチレンテレフ
タレートを主成分とする樹脂廃棄物が、分別収集された
PETボトルであることを特徴とする請求項1に記載の
高純度テレフタル酸。
2. The high-purity terephthalic acid according to claim 1, wherein the resin waste mainly composed of polyethylene terephthalate mixed with foreign substances is a separately collected PET bottle.
【請求項3】 異物混合されたポリエチレンテレフタレ
ートを主成分とする樹脂廃棄物をアルカリ存在下に加水
分解して得られた水溶液に、酸を加えてpHを 3.5〜9
に調整して異物を析出させて分離した後、さらにpHを
3以下に調整してテレフタル酸を析出させることを特徴
とする請求項1又は2に記載の高純度テレフタル酸の回
収法。
3. An aqueous solution obtained by hydrolyzing a resin waste mainly composed of polyethylene terephthalate mixed with foreign substances in the presence of an alkali is added with an acid to adjust the pH to 3.5 to 9;
The method for recovering high-purity terephthalic acid according to claim 1 or 2, wherein the terephthalic acid is precipitated by further adjusting the pH to 3 or less after precipitating and separating foreign matter by adjusting the pH.
JP16860597A 1997-06-25 1997-06-25 High-purity terephthalic acid and its recovery Pending JPH1112223A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16860597A JPH1112223A (en) 1997-06-25 1997-06-25 High-purity terephthalic acid and its recovery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16860597A JPH1112223A (en) 1997-06-25 1997-06-25 High-purity terephthalic acid and its recovery

Publications (1)

Publication Number Publication Date
JPH1112223A true JPH1112223A (en) 1999-01-19

Family

ID=15871165

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16860597A Pending JPH1112223A (en) 1997-06-25 1997-06-25 High-purity terephthalic acid and its recovery

Country Status (1)

Country Link
JP (1) JPH1112223A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100429385B1 (en) * 2001-04-09 2004-04-29 한국화학연구원 Process for preparing high purified terephthalic acid from PET
JP2020050653A (en) * 2018-09-26 2020-04-02 遠東新世紀股▲分▼有限公司 Method of producing terephthalic acid and system thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100429385B1 (en) * 2001-04-09 2004-04-29 한국화학연구원 Process for preparing high purified terephthalic acid from PET
JP2020050653A (en) * 2018-09-26 2020-04-02 遠東新世紀股▲分▼有限公司 Method of producing terephthalic acid and system thereof

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