JPH06100893A - Method for cleaning polymerization apparatus - Google Patents

Method for cleaning polymerization apparatus

Info

Publication number
JPH06100893A
JPH06100893A JP27348492A JP27348492A JPH06100893A JP H06100893 A JPH06100893 A JP H06100893A JP 27348492 A JP27348492 A JP 27348492A JP 27348492 A JP27348492 A JP 27348492A JP H06100893 A JPH06100893 A JP H06100893A
Authority
JP
Japan
Prior art keywords
cleaning
polymer
weight
alkaline earth
washing
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.)
Withdrawn
Application number
JP27348492A
Other languages
Japanese (ja)
Inventor
Hiroji Itaya
博治 板谷
Masashi Sakamoto
正史 坂本
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.)
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry 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 Asahi Chemical Industry Co Ltd filed Critical Asahi Chemical Industry Co Ltd
Priority to JP27348492A priority Critical patent/JPH06100893A/en
Publication of JPH06100893A publication Critical patent/JPH06100893A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D7/00Compositions of detergents based essentially on non-surface-active compounds
    • C11D7/02Inorganic compounds
    • C11D7/04Water-soluble compounds
    • C11D7/08Acids
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D7/00Compositions of detergents based essentially on non-surface-active compounds
    • C11D7/02Inorganic compounds
    • C11D7/04Water-soluble compounds
    • C11D7/06Hydroxides
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D7/00Compositions of detergents based essentially on non-surface-active compounds
    • C11D7/22Organic compounds
    • C11D7/26Organic compounds containing oxygen
    • C11D7/261Alcohols; Phenols

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Emergency Medicine (AREA)
  • Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
  • Detergent Compositions (AREA)

Abstract

PURPOSE:To remove by washing a condensation polymer deposited on an apparatus without impairing it and dispense with the nertralization step in the disposal of the cleaning fluid by using a cleaning fluid consisting of a polyhydric alcohol, an alkali (alkaline earth) metal hydroxide or a mineral acid, and water each in a specified amount for washing at a specified temperature an apparatus having a condensation polymer deposited thereon. CONSTITUTION:An apparatus (e.g. one made of stainless steel) having a condensation polymer (e.g. nylon 6) deposited thereon is washed at a temperature above the softening point of the polymer by using a cleaning fluid consisting of 69-99.89wt.% polyhydric alcohol (e.g. diethylene glycol), 0.1 to blow 1wt.% alkali (alkaline earth) metal hydroxide or mineral acid (e.g. NaOH), and 0.01-30wt.% water.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は縮合系のポリマーの付着
した装置類を繰り返し使用するために、付着している縮
合系のポリマーを洗浄力が高く、装置への悪影響がな
く、しかも使用後の処理が容易である洗浄液によって除
去する洗浄方法に関する。
BACKGROUND OF THE INVENTION The present invention repeatedly uses equipments to which condensation-type polymers are attached. Therefore, the adhesion-type condensation-type polymers have high detergency and have no adverse effect on the equipments. The present invention relates to a cleaning method of removing with a cleaning liquid that is easy to process.

【0002】[0002]

【従来の技術】縮合系ポリマーを製造する際、品種を変
更する場合や付着したポリマーが長期間の運転により変
性し異物として製品に混入する場合などに装置の洗浄が
必要となる。その際、縮合系ポリマーであるポリアミド
の製造装置に付着しているポリアミドを洗浄除去するに
は、アルカリ金属類の硝酸塩等を高温で溶解させた液中
に装置類を浸漬して洗浄する方法や高温の希燐酸溶液に
接触させる方法等が採用されてきた。しかしこれらの方
法には、複雑で精密化しているポリアミドの装置類を変
性させたり、腐食させたりするという欠点があり、さら
に可燃性ガスが発生するので後処理が必要になり安全性
にも問題があった。
2. Description of the Related Art When a condensation type polymer is manufactured, it is necessary to clean the apparatus when the type of product is changed or when the adhered polymer is modified by a long-term operation and mixed into a product as a foreign substance. At that time, in order to wash and remove the polyamide adhering to the production apparatus for the condensation type polymer polyamide, a method of immersing the apparatus in a liquid in which a nitrate of an alkali metal or the like is dissolved at a high temperature and washing the same are used. A method of contacting with a dilute phosphoric acid solution at a high temperature has been adopted. However, these methods have the drawbacks that they modify and corrode the complicated and refined polyamide equipment, and they also generate postflammable gas, which requires post-treatment and poses a safety problem. was there.

【0003】また、溶剤単独の洗浄液やこれに添加剤を
加えた洗浄液等も提案されているが、洗浄剤としてはい
づれも不十分であり、又洗浄力は満足するが、添加剤の
中和が必要であったりするという欠点のため実用上問題
があった。例えば、ドイツ特許第1133212号およ
び同第1143375号の明細書では、一価あるいは多
価のアルコールを洗浄剤とする方法が提案されている。
この方法は常圧の場合、ポリアミドを溶解する能力が低
く、十分に洗浄するためには長時間を要するという問題
点があり、また、沸点以上の加圧にした場合でも常圧よ
り時間は短くなるが、洗浄力はまだ十分でないという欠
点があった。
Further, a cleaning solution containing only a solvent or a cleaning solution containing an additive has been proposed. However, none of them is sufficient as a cleaning agent, and the cleaning power is satisfactory, but the additive is neutralized. However, there was a problem in practical use due to the drawback that it was necessary. For example, in the specifications of German Patent Nos. 1,133,212 and 1,143,375, a method using a monohydric or polyhydric alcohol as a detergent is proposed.
This method has a problem that the ability to dissolve polyamide is low in the case of normal pressure, and it takes a long time to sufficiently wash, and the time is shorter than normal pressure even when the pressure is higher than the boiling point. However, there is a drawback that the detergency is not yet sufficient.

【0004】また、特公昭51−47447号公報で
は、多価アルコール類にアルカリ金属もしくはアルカリ
土類金属の化合物または鉱産を添加した組成物を洗浄剤
とする方法を提案しているが、この方法は使用後の洗浄
液を廃棄する際に、酸やアルカリで中和しなけらばなら
ないという問題点がある。さらに、鉱酸を使用する場合
は、装置材質の腐食を生じ、一方、アルカリ金属やアル
カリ土類金属の化合物を使用する場合は装置材質の腐食
割れを生じるという欠点があった。
Further, Japanese Patent Publication No. 51-47447 proposes a method of using a composition obtained by adding a compound of an alkali metal or an alkaline earth metal or a mining product to a polyhydric alcohol as a cleaning agent. Has a problem that when the cleaning liquid after use is discarded, it must be neutralized with an acid or an alkali. Further, there is a drawback that when the mineral acid is used, the equipment material is corroded, while when the compound of the alkali metal or the alkaline earth metal is used, the equipment material is corroded and cracked.

【0005】[0005]

【発明が解決しようとする課題】本発明は、洗浄能力が
十分に高く、しかも洗浄液を廃棄する場合、従来法のよ
うに中和を必要とせず、装置材質に対しても腐食の恐れ
がない縮合系ポリマーの付着した装置類を洗浄する方法
を提供することを目的とするものである。
The present invention has a sufficiently high cleaning ability, and when the cleaning liquid is discarded, it does not require neutralization as in the conventional method, and there is no fear of corrosion of the material of the apparatus. It is an object of the present invention to provide a method for cleaning devices having a condensation polymer attached thereto.

【0006】[0006]

【課題を解決するための手段】即ち、本発明は多価アル
コール類69〜99.89重量%及びアルカリ金属もし
くはアルカリ土類金属の水酸化物または鉱酸0.1〜1
重量%及び0.01〜30重量%からなる洗浄液を、装
置に付着した縮合系ポリマーの軟化点以上の温度で、縮
合系ポリマーの付着した装置に用いることにより、前記
縮合系ポリマーを装置類から分離除去させる方法からな
る洗浄方法であって、装置類の変形、損傷、付着がな
く、洗浄液もpHが中性もしくは中性に近いので洗浄液
の処理が容易であるという優れた効果を有する洗浄方法
である。
That is, the present invention comprises 69 to 99.89% by weight of polyhydric alcohols and 0.1 to 1 of alkali metal or alkaline earth metal hydroxides or mineral acids.
By using a cleaning liquid composed of 0.01% by weight and 0.01% by weight at a temperature equal to or higher than the softening point of the condensation-type polymer attached to the apparatus, the condensation-type polymer is removed from the apparatuses. A cleaning method consisting of a method of separating and removing, which has an excellent effect that the cleaning solution is easy to process because the cleaning solution does not have deformation, damage or adhesion and the pH of the cleaning solution is neutral or close to neutral. Is.

【0007】本発明で使用する多価アルコール類として
は、メチレングリコール系、エチレングリコール系、プ
ロピレングリコール類、グリセリン等のジオール、トリ
オール等があげられるが、特に好ましいのはエチレング
リコール、トリエチレングリコールである。
Examples of the polyhydric alcohols used in the present invention include methylene glycol-based, ethylene glycol-based, propylene glycols, diols such as glycerin, triols, and the like, with ethylene glycol and triethylene glycol being particularly preferred. is there.

【0008】アルカリ金属もしくはアルカリ土類金属の
水酸化物としては、Li、Na、K、Mg、Ca、Ba
の水酸化物等が挙げられ、鉱酸としては塩酸、硫酸、硝
酸、燐酸等が挙げられる。アルカリ金属もしくはアルカ
リ土類金属の水酸化物の添加量は、洗浄液に対して0.
1重量%〜1.0重量%であり、特に0.1重量%〜
0.5重量%が好ましい。0.1重量%未満では、ポリ
マーが装置類に残留することがあるので好ましくない。
また、1.0重量%を越えると溶液のpHが中性ではな
くなり廃棄の際に中和する作業が必要となる。
Examples of hydroxides of alkali metals or alkaline earth metals include Li, Na, K, Mg, Ca and Ba.
And the like, and examples of the mineral acid include hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid and the like. The amount of the alkali metal or alkaline earth metal hydroxide added was 0.
1% by weight to 1.0% by weight, especially 0.1% by weight to
0.5% by weight is preferred. If it is less than 0.1% by weight, the polymer may remain in the devices, which is not preferable.
If it exceeds 1.0% by weight, the pH of the solution becomes non-neutral, and it is necessary to neutralize the solution at the time of disposal.

【0009】水の添加量は、0.01重量%〜30重量
%であり、特に0.01重量%〜5重量%が好ましい。
0.01重量%未満または30重量%以上では、ポリマ
ーが装置類に残留することがあるので好ましくない。
The amount of water added is 0.01% by weight to 30% by weight, and particularly preferably 0.01% by weight to 5% by weight.
If it is less than 0.01% by weight or 30% by weight or more, the polymer may remain in the devices, which is not preferable.

【0010】本発明で用いる洗浄液は、前記多価アルコ
ール類と前記アルカリ金属もしくはアルカリ土類金属の
水酸化物又は鉱酸と水からなるが、上記成分の他に洗浄
効果を阻害しない範囲で他の成分を加えててもよい。洗
浄温度は、装置に付着したポリマーの軟化点以上の温度
であり、その温度で前記洗浄液にそのポリマーの付着し
た装置類を接触させればよい。その際、洗浄液を撹拌し
たり、ポンプで循環させたり、不活性ガスでバブリング
させることにより洗浄時間を速めることもできる。
The cleaning solution used in the present invention comprises the above-mentioned polyhydric alcohols and the above-mentioned alkali metal or alkaline earth metal hydroxides or mineral acids and water. May be added. The cleaning temperature is a temperature equal to or higher than the softening point of the polymer attached to the apparatus, and the apparatus attached with the polymer may be brought into contact with the cleaning liquid at that temperature. At this time, the cleaning time can be shortened by stirring the cleaning liquid, circulating it with a pump, or bubbling with an inert gas.

【0011】洗浄温度が前記ポリマーの軟化点未満の場
合はポリマーが残留し、ポリマーを洗浄除去する目的を
十分に達成することができない。本発明の洗浄液の適用
される縮合系ポリマーは、ナイロン6等のポリアミド類
またはポリエチレンテレフタレート等のポリエステル類
等の主に脱水、脱アルコール反応を利用して製造される
ポリマーでそれらの共重合体であっても良い。
When the washing temperature is lower than the softening point of the polymer, the polymer remains and the purpose of washing and removing the polymer cannot be sufficiently achieved. The condensation polymer to which the cleaning liquid of the present invention is applied is a polymer such as polyamides such as nylon 6 or polyesters such as polyethylene terephthalate produced mainly by dehydration / dealcoholization reaction and copolymers thereof. It may be.

【0012】[0012]

【発明の効果】本発明方法により、縮合系ポリマーの付
着した装置類を洗浄すると、付着しているポリマー(そ
の変性物も含む)を十分に洗浄除去することができ、し
かも、洗浄時に装置類の腐食の恐れがない。また、洗浄
廃液の廃棄時に中和する必要がないという効果もある。
EFFECTS OF THE INVENTION By washing the apparatus to which the condensation polymer is attached by the method of the present invention, the attached polymer (including its modified product) can be sufficiently washed and removed, and the apparatus can be washed at the time of washing. There is no risk of corrosion. Further, there is also an effect that it is not necessary to neutralize the cleaning waste liquid.

【0013】[0013]

【実施例】次に本発明の実施例をあげて具体的に説明す
る。
EXAMPLES Next, examples of the present invention will be specifically described.

【0014】ポリアミドイミドエラストマーの製造例 かきまぜ機、窒素導入口及び留去管を取り付けた500
mlセパラブルフラスコに、カプロラクタム97g、数
平均分子量1470のポイオキシエチレングリコール9
0g、トリメリット酸16.4g、ジフェニルメタンジ
イソシアネート4.52gをN,N−ヘキサメチレン−
ビス(3,5−ジ−t−ブチル−4−ヒドロキシケイ皮
酸アミド)(商品名、イルガノックス 1098:酸化
防止剤)0.3gと共に仕込み、窒素を50ml/mi
nで流しながら、150℃で融解させた後、260℃で
4時間重合した。260℃にしてから1時間、2時間、
4時間後の反応中の水分は0.7、0.5、0.3重量
%であった。
Production Example of Polyamideimide Elastomer 500 equipped with a stirrer, a nitrogen inlet and a distillation tube
In a ml separable flask, 97 g of caprolactam and 9 of polyoxyethylene glycol having a number average molecular weight of 1470.
0 g, trimellitic acid 16.4 g, and diphenylmethane diisocyanate 4.52 g were added to N, N-hexamethylene-
Charge with 0.3 g of bis (3,5-di-t-butyl-4-hydroxycinnamic acid amide) (trade name, Irganox 1098: antioxidant), and add nitrogen at 50 ml / mi.
It was melted at 150 ° C while flowing at n, and then polymerized at 260 ° C for 4 hours. 1 hour, 2 hours after reaching 260 ° C,
The water content in the reaction after 4 hours was 0.7, 0.5, and 0.3% by weight.

【0015】次いで、テトラブチルオルソチタネート
0.3gを添加した後、徐々に1トールまで減圧して未
反応のカプロラクタムを系外に留去した。さらに同温度
で1トール以下の圧力下で2時間重合して、単黄色透明
なエラストマーを得た(ヘイズ46%)。このエラスト
マーは、ポリオキシエチレングリコールセグメント49
重量%を含有し、相対粘度1.93で、融点は190
℃、結晶化温度は121℃分解温度は330℃であっ
た。
Then, after adding 0.3 g of tetrabutyl orthotitanate, the pressure was gradually reduced to 1 Torr and unreacted caprolactam was distilled out of the system. Further, polymerization was carried out at the same temperature under a pressure of 1 Torr or less for 2 hours to obtain a single yellow transparent elastomer (haze 46%). This elastomer has polyoxyethylene glycol segment 49
Wt%, relative viscosity 1.93, melting point 190
The crystallization temperature was 121 ° C and the decomposition temperature was 330 ° C.

【0016】実施例1〜4 SUS−304のステンレス鋼ピースにポリアミド、ポ
リアミドイミドエラストマー等を溶融付着させた試料片
を、第1表に示す組成の洗浄液を入れたガラスフラスコ
中に浸し、ガラス製の水冷還流管を付け、マントルヒー
ターで所定の温度及び時間加熱した。冷却後試料片を取
り出し、水で洗浄後、該試料片を目視観察した。試料片
の外観及び色調は、加熱前に比べ変化は認められなかっ
た。それらの結果と使用後の洗浄液のpHを表1に示し
た。なお、pHは試験使用後の洗浄液50mlを取り、
250mlまで希釈した後、通常のpHメーターを用い
て測定した。
Examples 1 to 4 A sample piece prepared by melting and adhering polyamide, polyamideimide elastomer, etc. on a stainless steel piece of SUS-304 was immersed in a glass flask containing a cleaning solution having the composition shown in Table 1, and made of glass. Was attached to the water-cooled reflux tube, and heated with a mantle heater at a predetermined temperature for a predetermined time. After cooling, the sample piece was taken out, washed with water, and then visually observed. The appearance and color tone of the sample piece were not changed as compared with those before heating. The results and the pH of the cleaning liquid after use are shown in Table 1. For the pH, take 50 ml of the washing solution after the test use,
After diluting to 250 ml, it was measured using a normal pH meter.

【0017】比較例1〜3 洗浄組成を表2のとおり変えた以外は、実施例1〜4と
同じ方法で試料を洗浄し、結果を表2に示した。比較例
1は、ポリマーが残留付着していた。また比較例2,3
は、ポリマーの付着は全くなかったが、洗浄液のpHが
強アルカリもしくは強酸性を示したので、洗浄液を廃棄
する際、中和しなくてはならなかった。また、比較例3
は試料片に一部黒点の斑点があり、明らかに腐食されて
いることが認められた。
Comparative Examples 1 to 3 Samples were washed in the same manner as in Examples 1 to 4 except that the cleaning composition was changed as shown in Table 2, and the results are shown in Table 2. In Comparative Example 1, the polymer remained attached. Comparative Examples 2 and 3
No polymer adhered, but the pH of the washing solution showed strong alkali or strong acidity, and therefore the washing solution had to be neutralized when it was discarded. In addition, Comparative Example 3
It was confirmed that the test piece had some black spots and was clearly corroded.

【0018】[0018]

【表1】 [Table 1]

【0019】[0019]

【表2】 [Table 2]

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C11D 7:08) ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Office reference number FI technical display location C11D 7:08)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 多価アルコール類69〜99.89重量
%、及びアルカリ金属もしくはアルカリ土類金属の水酸
化物又は鉱酸0.1〜1重量%未満、及び水0.01〜
30重量%からなる洗浄液を用いて、縮合系のポリマー
の付着した装置類をその付着したポリマーの軟化点以上
の温度で洗浄することを特徴とする重合装置類の洗浄方
法。
1. Polyalcohols 69 to 99.89% by weight, and alkali metal or alkaline earth metal hydroxides or mineral acids 0.1 to less than 1% by weight, and water 0.01 to.
A method for cleaning a polymerization device, comprising: cleaning a device having a condensation-type polymer attached thereto at a temperature equal to or higher than a softening point of the attached polymer using a cleaning liquid of 30% by weight.
JP27348492A 1992-09-18 1992-09-18 Method for cleaning polymerization apparatus Withdrawn JPH06100893A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27348492A JPH06100893A (en) 1992-09-18 1992-09-18 Method for cleaning polymerization apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27348492A JPH06100893A (en) 1992-09-18 1992-09-18 Method for cleaning polymerization apparatus

Publications (1)

Publication Number Publication Date
JPH06100893A true JPH06100893A (en) 1994-04-12

Family

ID=17528554

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27348492A Withdrawn JPH06100893A (en) 1992-09-18 1992-09-18 Method for cleaning polymerization apparatus

Country Status (1)

Country Link
JP (1) JPH06100893A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6568406B2 (en) * 1997-10-22 2003-05-27 Basf Aktiengesellschaft Method of cleaning plant parts for the preparation or processing of (meth)acrylic esters
WO2005111187A1 (en) * 2004-05-18 2005-11-24 Lg Chem, Ltd. Facility parts cleaning solution for processing of (meth)acrylic acid and/or (meth)acrylic esters and cleaning method using said cleaning solution

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6568406B2 (en) * 1997-10-22 2003-05-27 Basf Aktiengesellschaft Method of cleaning plant parts for the preparation or processing of (meth)acrylic esters
WO2005111187A1 (en) * 2004-05-18 2005-11-24 Lg Chem, Ltd. Facility parts cleaning solution for processing of (meth)acrylic acid and/or (meth)acrylic esters and cleaning method using said cleaning solution
US7073519B2 (en) 2004-05-18 2006-07-11 Lg Chem, Ltd. Facility parts cleaning solution for processing of (meth)acrylic acid and/or (meth)acrylic esters and cleaning method using said cleaning solution
KR100635284B1 (en) * 2004-05-18 2006-10-17 주식회사 엘지화학 Plant parts cleaning solution for the processing of methacrylic acid and/or methacrylic esters, and cleaning method using said cleaning solution

Similar Documents

Publication Publication Date Title
KR101142562B1 (en) Cleaning agent composition
US5350457A (en) Process for cleaning electronic or precision parts and recycling rinse waste water
EP0030904B1 (en) Copolyester amides pliant at low temperature
JPWO2010024141A1 (en) Cleaning composition for lead-free solder flux removal and lead-free solder flux removal system
EP0196981B1 (en) Process for the preparation of copolyamides based on hexamethylene diamine, apidic acid and dimeric acid
JPH0739372B2 (en) Method to increase the rate of reaction of direct esterification of diacid with glycol
EP0384859A1 (en) Method for the preparation of semi-aromatic polyamides comprising aromatic dicarboxylic acid(s) and alkyl pentamethylene diamine residues
JPH06100893A (en) Method for cleaning polymerization apparatus
JP3203285B2 (en) Method for producing low-corrosion polyarylene sulfide
JPH051840B2 (en)
JPH07197100A (en) Cleaning agent for external window
BR112013019383A2 (en) linear polymer for release of dirt and alkaline detergent liquid
WO1993023436A1 (en) Method for reducing polymer build-up in a polymerization reactor
JPH07102062A (en) Polymer composed of polyether block and polyamide block
JP4038596B2 (en) Composition for removing organic solvent and / or oily substance from substrate surface
JPH10182545A (en) Prevention of fouling in device for producing acrylic acid
JP5132309B2 (en) Method for producing cyclic ester
JPH10505616A (en) Production of aspartic acid polycondensate and use of the polycondensate
JPH09324195A (en) Solvent usable as detergent
KR20110047693A (en) A detergent composition for a glass substrate of flat panel display device
US2525178A (en) Removing silver films from mirrors with phosphoric acid
JPS59102998A (en) Method of cleaning devices adhered with polyamide
SU1744072A1 (en) Method of strengthening phosphate glass products
JP2548964B2 (en) Cleaning method for urethane resin mold
US3679593A (en) Stripping of condensation polymers with an alkoxide

Legal Events

Date Code Title Description
A300 Withdrawal of application because of no request for examination

Free format text: JAPANESE INTERMEDIATE CODE: A300

Effective date: 19991130