JPH10158309A - Purification of monomer - Google Patents

Purification of monomer

Info

Publication number
JPH10158309A
JPH10158309A JP33506396A JP33506396A JPH10158309A JP H10158309 A JPH10158309 A JP H10158309A JP 33506396 A JP33506396 A JP 33506396A JP 33506396 A JP33506396 A JP 33506396A JP H10158309 A JPH10158309 A JP H10158309A
Authority
JP
Japan
Prior art keywords
monomer
solution
purifying
sulfur compound
styrene
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
JP33506396A
Other languages
Japanese (ja)
Other versions
JP3730346B2 (en
Inventor
Rensuke Igarashi
錬典 五十嵐
Shinichi Tadokoro
愼一 田所
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.)
Kuraray Co Ltd
Original Assignee
Kuraray 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 Kuraray Co Ltd filed Critical Kuraray Co Ltd
Priority to JP33506396A priority Critical patent/JP3730346B2/en
Publication of JPH10158309A publication Critical patent/JPH10158309A/en
Application granted granted Critical
Publication of JP3730346B2 publication Critical patent/JP3730346B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Landscapes

  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Polymerisation Methods In General (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

PROBLEM TO BE SOLVED: To purify a monomer by bringing a monomer solution containing sulfur compounds into contact with an aqueous solution of an alkali(ne earth) metal hypochlorite, then extracting the monomer thereby obtaining the monomer of high quality having no foreign smell. SOLUTION: A plastic waste that contains sulfur compounds and a resin containing more than 50wt.% of methyl methacrylate units or styrene units is thermally decomposed to prepare a monomer solution. This monomer solution is treated with an aqueous solution of an alkali(ne earth) metal hypochlorite and extracted or distilled thereby purifying the monomer.

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、イオウ化合物を含
むモノマー溶液の精製方法に関し、特に廃プラスチック
を熱分解して得た分解液中に微量含まれるイオウ化合物
を効率よく且つ経済的に有利に除去することを主眼とし
たモノマーの精製に好適な方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for purifying a monomer solution containing a sulfur compound, and more particularly, to efficiently and economically advantageously use a small amount of a sulfur compound contained in a decomposition solution obtained by thermally decomposing waste plastic. The present invention relates to a method suitable for purifying a monomer with an emphasis on removal.

【0002】[0002]

【従米の技術】従来からメチルメタクリレート(以下、
これをMMΛと略記する場合がある)またはスチレンを
主成分とするモノマーを重合して得られるメタクリル樹
脂、スチレン樹脂、MS樹脂等は家電製品、自動車部
品、光学素材として広く使用されている。これらの樹脂
は熱分解によって容易にモノマーに解重合することが知
られている。しかしながら、これらの樹脂を熱分解した
場合、樹脂化の段階などで添加されたイオウ化合物を主
とした不純物が残存して蒸留操作でも除くことができず
異臭が残るため、単に蒸留精製のみでは製品モノマーと
することができなかった。また分解液中に含まれる微量
のイオウ化合物は、不純物の除去剤として用いられる活
性炭、モレキュラーシーブでは十分に除去することがで
きなかった。このため、従来これら廃プラスチックは焼
却するか、埋立処分することを余儀なくされているのが
実情である。
[Technology of the United States] Methyl methacrylate (hereinafter, referred to as
This may be abbreviated as MMΛ) or methacrylic resin, styrene resin, MS resin, and the like obtained by polymerizing a monomer containing styrene as a main component are widely used as home electric appliances, automobile parts, and optical materials. It is known that these resins are easily depolymerized into monomers by thermal decomposition. However, when these resins are thermally decomposed, impurities mainly composed of sulfur compounds added at the stage of resinification remain and cannot be removed by the distillation operation, so that an unpleasant odor remains. Could not be monomer. Also, trace amounts of sulfur compounds contained in the decomposition solution could not be sufficiently removed with activated carbon or molecular sieve used as an impurity remover. For this reason, these waste plastics have conventionally been incinerated or landfilled.

【0003】[0003]

【発明が解決しようとする課題】したがって、本発明
は、イオウ化合物を含むモノマー溶液、特に廃プラスチ
ックを熱分解して得た微量のイオウ化合物を含有する分
解液を精製し、イオウ臭気のないモノマーを得る方法を
提供することを目的とする。
SUMMARY OF THE INVENTION Accordingly, the present invention provides a monomer solution containing a sulfur compound, in particular, a decomposition solution containing a trace amount of a sulfur compound obtained by thermally decomposing waste plastic to purify a monomer solution having no sulfur odor. The purpose is to provide a method of obtaining.

【0004】[0004]

【課題を解決するための手段】本発明者らは、熱分解液
中に含まれるイオウ化合物の除去法について鋭意検討し
た結果、酸化剤で処理することでイオウ化合物が反応し
て水溶性化合物または高沸点化合物に変換するため、抽
出および蒸留操作で容易に除去できるようになることを
見出した。更に酸化剤の中でも特に次亜塩素酸のアルカ
リ金属塩またはアルカリ土類金属塩の水溶液が低分子イ
オウ化合物との反応性が高いことを見出し、本発明を完
成させるに至った。
Means for Solving the Problems The present inventors have intensively studied a method for removing a sulfur compound contained in a pyrolysis solution, and as a result, the sulfur compound reacts with an oxidizing agent to react with the water-soluble compound. It has been found that since the compound is converted into a high-boiling compound, it can be easily removed by extraction and distillation. Furthermore, among the oxidizing agents, it has been found that an aqueous solution of an alkali metal salt or an alkaline earth metal salt of hypochlorous acid has high reactivity with a low-molecular-weight sulfur compound, thereby completing the present invention.

【0005】すなわち、本発明は、イオウ化合物を含む
モノマー溶液、特に廃プラスチックを熱分解して得たイ
オウ化合物を含有するモノマー溶液を精製するに際し、
モノマー溶液を、次亜塩素酸のアルカリ金属塩またはア
ルカリ土類金属塩の水溶液と接触処理した後、抽出およ
び/または蒸留することを特徴とするモノマーの精製方
法である。
That is, the present invention provides a method for purifying a monomer solution containing a sulfur compound, particularly a monomer solution containing a sulfur compound obtained by thermally decomposing waste plastic.
A method for purifying a monomer, comprising subjecting a monomer solution to a contact treatment with an aqueous solution of an alkali metal salt or an alkaline earth metal salt of hypochlorous acid, followed by extraction and / or distillation.

【0006】[0006]

【発明の実施の形態】以下に本発明の方法について詳細
に説明する。本発明は、イオウ化合物を含むモノマー溶
液、特に廃プラスチックを熱分解して得た微量のイオウ
化合物を含有するモノマー溶液の精製方法である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The method of the present invention will be described below in detail. The present invention is a method for purifying a monomer solution containing a sulfur compound, particularly a monomer solution containing a trace amount of a sulfur compound obtained by thermally decomposing waste plastic.

【0007】本発明の方法に用いるモノマー溶液として
は、イオウ化合物を含む単量体成分を主体成分とするモ
ノマー溶液であれば特に限定はないが、廃プラスチック
を熱分解して得たイオウ化合物を含有する分解液である
ことが好ましい。
[0007] The monomer solution used in the method of the present invention is not particularly limited as long as it is a monomer solution containing a monomer component containing a sulfur compound as a main component, but a sulfur compound obtained by thermally decomposing waste plastic is used. It is preferable that the decomposition solution is contained.

【0008】また、廃プラスチックとしては特に限定さ
れないが、メタクリル樹脂、スチレン樹脂またはMMA
単位またはスチレン単位を50重量%以上含む他の共重
合樹脂の廃プラスチックが好ましく用いられる。本発明
は、これらを熱分解して得た分解液をモノマー溶液とし
て用い、このモノマー溶液からMMAおよび/またはス
チレンモノマ一を精製する方法として有効である。分解
液中には、通常MMA、スチレンなどの単量体を主体と
し、これに1〜100ppm程度の種々の形態の有機イ
オウ化合物などからなるイオウ化合物(メチルメルカプ
タン、硫化ジメチル、二硫化ジメチルなど)、可塑剤な
どの他の種々の不純物が含まれる。
The waste plastic is not particularly limited, but may be methacrylic resin, styrene resin or MMA.
A waste plastic of another copolymer resin containing 50% by weight or more of a styrene unit or a styrene unit is preferably used. The present invention is effective as a method for using a decomposition solution obtained by thermally decomposing these as a monomer solution and purifying MMA and / or styrene monomer from the monomer solution. The decomposition solution usually contains a monomer such as MMA or styrene as a main component, and a sulfur compound (eg, methyl mercaptan, dimethyl sulfide, dimethyl disulfide, etc.) composed of various forms of organic sulfur compounds of about 1 to 100 ppm. And various other impurities such as plasticizers.

【0009】本発明は、抽出、蒸留に先立ち、酸化剤水
溶液で接触処理することにより、モノマーを損失するこ
となくイオウ化合物などの着臭成分のみを水溶性化合物
に、または沸点の大きく異なる物質に変換せしめ、通常
の抽出および蒸留操作で容易に分離可能なものとし、実
質的に異臭の無いモノマー、特にMMAおよび/または
スチレンモノマーを得る方法である。
According to the present invention, by subjecting a odorant such as a sulfur compound to a water-soluble compound or a substance having a greatly different boiling point without losing monomers, the present invention provides a contact treatment with an aqueous oxidizing agent prior to extraction and distillation. In this method, a monomer which can be easily separated by ordinary extraction and distillation operations to obtain a monomer having substantially no off-flavor, particularly, a MMA and / or styrene monomer is obtained.

【0010】本発明の方法においては、酸化剤として次
亜塩素酸のアルカリ金属塩またはアルカリ土類金属塩が
使用されるが、それらの中でも特にナトリウム、カリウ
ム、カルシウムの塩が好ましい。これらの次亜塩素酸塩
は水溶液で用いられる。例えば、10%次亜塩素酸ナト
リウム水溶液の場合の使用量は、熱分解液などのモノマ
ー溶液100重量部に対して通常0.1〜4重量部であ
り、好ましくは0.3〜2重量部である。
In the method of the present invention, an alkali metal salt or an alkaline earth metal salt of hypochlorous acid is used as an oxidizing agent, and among them, sodium, potassium and calcium salts are particularly preferable. These hypochlorites are used in aqueous solution. For example, the amount of 10% aqueous sodium hypochlorite used is generally 0.1 to 4 parts by weight, preferably 0.3 to 2 parts by weight, per 100 parts by weight of a monomer solution such as a pyrolysis solution. It is.

【0011】接触処理方法、反応装置としては、特に限
定されることは無く、例えば攪拌機の付いた釜内で上記
モノマー溶液および水溶液を攪拌・接触させるだけで十
分である。接触時間は、通常0.1分〜30分であり、
温度も特に制限は無く、室温で実施するのが有利であ
る。
The contact treatment method and the reaction apparatus are not particularly limited, and it is sufficient to stir and contact the monomer solution and the aqueous solution in a kettle equipped with a stirrer, for example. The contact time is usually 0.1 to 30 minutes,
The temperature is not particularly limited, and it is advantageous to carry out the reaction at room temperature.

【0012】また、本発明の方法は、接触処理の後、抽
出工程および/または蒸留工程が適用されるが、特別な
抽出設備、蒸留設備は必要なく、例えば、当該処理液を
従来のモノマー製造用精製設備の抽出および/または蒸
留プロセスにフィードして、目的とするモノマーを精製
・回収することができる。これらのうち蒸留工程の採用
が工程減少の点で好ましく、例えば製造された粗モノマ
ーと混合して蒸留・精製することも可能である。
In the method of the present invention, an extraction step and / or a distillation step is applied after the contact treatment. However, no special extraction equipment or distillation equipment is required. It can be fed to an extraction and / or distillation process in a purification facility for purification and recovery of the target monomer. Of these, the use of a distillation step is preferred from the viewpoint of reducing the number of steps. For example, distillation and purification can be performed by mixing with a produced crude monomer.

【0013】[0013]

【実施例】以下に本発明について実施例および比較例で
もって具体的に詳しく説明するが、本発明はこれらの実
施例によりその範囲を限定されるものではない。なお、
以下の実施例および比較例において、モノマーの純度は
ガスクロマトグラフィ[(株)島津製作所製、GC−1
4A型]により測定された値(%)である。
EXAMPLES The present invention will be described in detail below with reference to examples and comparative examples, but the scope of the present invention is not limited by these examples. In addition,
In the following Examples and Comparative Examples, the purity of the monomer was determined by gas chromatography [GC-1 manufactured by Shimadzu Corporation].
4A].

【0014】実施例1 廃アクリル樹脂1kgを反応釜中500℃に加熱して留
出した1リットルの分解液(比重0.98;MMA9
0.7重量%、メチルメルカプタン56ppm、硫化ジ
メチル15ppm、二硫化ジメチル35ppm等を含
む)を攪拌機の付いた2リットルのフラスコに仕込ん
だ。このフラスコに試薬10%次亜塩素酸ナトリウム水
溶液10mlおよび蒸留水90mlを添加し、室温下で
5分間攪拌する。攪拌終了後静置して下相の水相を分離
し、さらに水100mlを添加して5分間攪拌した後、
下相の水相を分離した。得られた粗モノマー液を棚段2
0段のオールダーショー精留塔を組込んだ蒸留装置に仕
込み、常圧下、還流比1.1で蒸留し、沸点99.8〜
100.6℃の留分750mlを得た。得られた精製M
MAモノマーの純度は99.8%であり、臭いはMMA
特有のもので異臭はなかった。またFPD−ガスクロマ
トグラフィ(イオウ用フィルターを装着した炎光光度検
出器付きガスクロマトグラフィ)でもピークは検出され
ず、イオウ化合物は0.01ppm以下であった。
Example 1 1 kg of waste acrylic resin was heated to 500 ° C. in a reaction vessel and distilled to obtain 1 liter of a decomposed liquid (specific gravity 0.98; MMA 9
0.7% by weight, containing 56 ppm of methyl mercaptan, 15 ppm of dimethyl sulfide, 35 ppm of dimethyl disulfide, etc.) were charged into a 2 liter flask equipped with a stirrer. 10 ml of a 10% aqueous solution of sodium hypochlorite and 90 ml of distilled water are added to the flask, and the mixture is stirred at room temperature for 5 minutes. After completion of the stirring, the mixture was allowed to stand and the lower aqueous phase was separated, and 100 ml of water was further added and stirred for 5 minutes.
The lower aqueous phase was separated. The obtained crude monomer liquid is transferred to a tray 2
A distillation apparatus incorporating a 0-stage Oldershaw rectification column was charged, and distilled under a normal pressure at a reflux ratio of 1.1.
750 ml of a 100.6 ° C. fraction were obtained. Purified M obtained
The purity of the MA monomer is 99.8%, and the odor is MMA.
No peculiar smell. No peak was detected by FPD-gas chromatography (gas chromatography with a flame photometric detector equipped with a sulfur filter), and the content of sulfur compounds was 0.01 ppm or less.

【0015】比較例1 実施例1において、廃アクリル樹脂の熱分解液1リット
ルを次亜塩素酸ナトリウム水溶液による処理をせずにそ
のまま蒸留装置に仕込み、99.8〜100.6℃の留
分750mlを得た。得られたMMAモノマーの純度は
99.8%であったがMMAモノマーとは異なる臭気が
感じられた。FPD−ガスクロマトグラフィによる測定
では二硫化ジメチルのリテンションタイムの位置に28
ppm相当量のピークが測定された。
Comparative Example 1 In Example 1, 1 liter of the pyrolysis liquid of waste acrylic resin was charged into a distillation apparatus without treatment with an aqueous solution of sodium hypochlorite, and a fraction at 99.8 to 100.6 ° C. 750 ml were obtained. Although the purity of the obtained MMA monomer was 99.8%, an odor different from that of the MMA monomer was felt. According to the measurement by FPD-gas chromatography, 28
A peak corresponding to ppm was measured.

【0016】実施例2 MMAを65%、スチレンを35%含むMS樹脂1kg
を反応釜中500℃に加熱して留出した950mlの分
解液(比重0.95;MMA55.3重量%、スチレン
22.9重量%、メチルメルカプタン89ppm、硫化
ジメチル12ppm、二硫化ジメチル21ppm等を含
む)を攪拌機の付いた2リットルのフラスコに仕込ん
だ。このフラスコに試薬10%の次亜塩素酸ナトリウム
水溶液6mlと蒸留水100mlを添加して5分間攪拌
した。攪拌終了後下相の水相を分離し、さらに水100
mlを添加して5分間攪拌した後、下相の水相を分離し
た。得られた粗モノマー液を実施例1と同じ蒸留装置に
仕込み、常圧下還流比1.7で蒸留し、沸点99.8〜
100.6℃、留分520mlを得た。得られた精製M
MAモノマーの純度は99.8%であり、異臭は無かっ
た。FPD−ガスクロマトグラフィでもイオウ化合物の
存在は認められなかった。
Example 2 1 kg of MS resin containing 65% of MMA and 35% of styrene
Was heated to 500 ° C. in a reaction vessel to distill 950 ml of a decomposition solution (specific gravity 0.95; MMA 55.3% by weight, styrene 22.9% by weight, methyl mercaptan 89 ppm, dimethyl sulfide 12 ppm, dimethyl disulfide 21 ppm, etc.). Was charged into a 2 liter flask equipped with a stirrer. 6 ml of a 10% aqueous solution of sodium hypochlorite and 100 ml of distilled water were added to the flask and stirred for 5 minutes. After completion of the stirring, the lower aqueous phase was separated, and 100
After addition of ml and stirring for 5 minutes, the lower aqueous phase was separated. The obtained crude monomer liquid was charged into the same distillation apparatus as in Example 1, and distilled under a normal pressure and a reflux ratio of 1.7, and the boiling point was 99.8 to 99.8.
At 100.6 ° C., a fraction of 520 ml was obtained. Purified M obtained
The purity of the MA monomer was 99.8%, and there was no off-odor. The presence of the sulfur compound was not recognized by FPD-gas chromatography.

【0017】実施例3 廃スチレン樹脂1kgを反応釜中500℃に加熱して留
出した950mlの分解液(比重0.92;スチレン7
2重量%、メチルメルカプタン18ppm、硫化ジメチ
ル21ppm、二硫化ジメチル44ppm等を含む)を
攪拌機の付いた2リットルのフラスコに仕込んだ。この
フラスコに試薬サラシ粉[Ca(OCl)2 ]を使用し
て調製した0.5%次亜塩素酸のサラシ粉水溶液100
mlを添加し、室温下で5分間攪拌した。攪拌終了後静
置し、下相の水相を分離した。さらに水100mlを添
加して5分間攪拌し、下相の水相を分離した。得られた
粗スチレンモノマー液を棚段20段のオールダーショー
精留塔を組み込んだ蒸留装置に仕込み、常圧下還流比
1.4で蒸留し、沸点144.8〜145.5℃の留分
670mlを得た。得られたスチレンモノマーの純度は
99.7%でその臭いはスチレン特有のもので異臭は無
かった。またFPD−ガスクロマトグラフィでもイオウ
化合物の存在は認められなかった。
Example 3 1 kg of waste styrene resin was heated to 500 ° C. in a reaction vessel and distilled out to 950 ml of a decomposition solution (specific gravity 0.92; styrene 7
2 wt%, containing 18 ppm of methyl mercaptan, 21 ppm of dimethyl sulfide, 44 ppm of dimethyl disulfide, etc.) were charged into a 2 liter flask equipped with a stirrer. In this flask, an aqueous solution of 0.5% hypochlorous acid was used, which was prepared by using a reagent powder [Ca (OCl) 2 ].
Then, the mixture was stirred at room temperature for 5 minutes. After completion of the stirring, the mixture was allowed to stand, and the lower aqueous phase was separated. Further, 100 ml of water was added and the mixture was stirred for 5 minutes, and the lower aqueous phase was separated. The obtained crude styrene monomer liquid was charged into a distillation apparatus incorporating an Oldershaw rectification column having 20 trays, and distilled under a normal pressure at a reflux ratio of 1.4 to obtain a fraction having a boiling point of 144.8 to 145.5 ° C. 670 ml were obtained. The purity of the obtained styrene monomer was 99.7%, and the odor was peculiar to styrene, and there was no off-odor. Also, the presence of the sulfur compound was not recognized by FPD-gas chromatography.

【0018】[0018]

【発明の効果】本発明によれば、イオウ化合物などを選
択的に分離可能な物質に変化せしめることにより、異臭
のない高品質のモノマーを廃プラスチックから回収する
ことが可能となり、工業的に有効である。
According to the present invention, it is possible to recover a high-quality monomer having no off-odor from waste plastics by converting sulfur compounds and the like into substances that can be selectively separated, which is industrially effective. It is.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 イオウ化合物を含むモノマー溶液を精製
するに際し、モノマー溶液を、次亜塩素酸のアルカリ金
属塩またはアルカリ土類金属塩の水溶液と接触処理した
後、抽出および/または蒸留することを特徴とするモノ
マーの精製方法。
In purifying a monomer solution containing a sulfur compound, the monomer solution is contacted with an aqueous solution of an alkali metal salt or an alkaline earth metal salt of hypochlorous acid, followed by extraction and / or distillation. A method for purifying a characteristic monomer.
【請求項2】 モノマー溶液が、廃プラスチックを熱分
解して得た分解液であることを特徴とする請求項1記載
のモノマーの精製方法。
2. The method according to claim 1, wherein the monomer solution is a decomposition solution obtained by thermally decomposing waste plastic.
【請求項3】 廃プラスチックが、メチルメタクリレー
ト単位またはスチレン単位を50重量%以上含有する樹
脂であることを特徴とする請求項2記載のモノマーの精
製方法。
3. The method for purifying a monomer according to claim 2, wherein the waste plastic is a resin containing at least 50% by weight of a methyl methacrylate unit or a styrene unit.
JP33506396A 1996-11-29 1996-11-29 Monomer purification method Expired - Fee Related JP3730346B2 (en)

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JP3730346B2 JP3730346B2 (en) 2006-01-05

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