JPS6025523B2 - How to clean spinning equipment - Google Patents
How to clean spinning equipmentInfo
- Publication number
- JPS6025523B2 JPS6025523B2 JP12863777A JP12863777A JPS6025523B2 JP S6025523 B2 JPS6025523 B2 JP S6025523B2 JP 12863777 A JP12863777 A JP 12863777A JP 12863777 A JP12863777 A JP 12863777A JP S6025523 B2 JPS6025523 B2 JP S6025523B2
- Authority
- JP
- Japan
- Prior art keywords
- cleaning
- sulfamic acid
- aqueous solution
- spinning
- alkali metal
- 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.)
- Expired
Links
Landscapes
- Moulds For Moulding Plastics Or The Like (AREA)
- Detergent Compositions (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
Description
【発明の詳細な説明】
本発明は熱可塑性合成繊維を溶融紡糸するに用いた級糸
装置を洗浄して再生する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for cleaning and regenerating a yarn machine used for melt spinning thermoplastic synthetic fibers.
一般に熱可塑性合成重合体を溶融紡糸するに従って紡糸
装置特にパック内の圧力が上昇したり、紡糸工程が不調
になったりするため、紡糸装置を取替える必要が生じる
。取替えられた使用済みの紡糸装置は洗浄して再使用す
ることが行なわれている。この洗浄方法として、工業的
には、通常ナトリウム又はカリウムの硝酸塩と亜硝酸塩
の混合物の高温(300〜600oo)の溶融液に浸薄
処理する所謂ソルト洗浄が行なわれている。Generally, as thermoplastic synthetic polymers are melt-spun, the pressure inside the spinning device, especially the pack, increases, or the spinning process becomes malfunctioning, making it necessary to replace the spinning device. The used spinning equipment that has been replaced is cleaned and reused. As this cleaning method, so-called salt cleaning is usually carried out industrially, which involves immersion in a high-temperature (300 to 600 oo) molten solution of a mixture of sodium or potassium nitrate and nitrite.
しかしながら、かかるソルト洗浄は、硝酸塩による有機
物の酸化反応であるため、反応が激しく、火炎や爆発の
危険が常に存在する。However, since such salt cleaning is an oxidation reaction of organic matter by nitrate, the reaction is violent and there is always a danger of flame or explosion.
また、この洗浄に際しては高融点の炭酸塩が生じ、これ
を定期的に除去する作業が必要である。この炭酸塩の除
去は極めて危険であり、しかも除去された炭酸塩には硝
酸塩や亜硝酸塩が共存し、公害対策上安易に廃棄できな
い。また、かかるソルト洗浄では、級糸装置に、重合体
の炭化物や重合体中に含まれる種々の金属塩の反応によ
って生じた固着物等が固着し、充分に洗浄することは極
めて困難であった。Further, during this washing, carbonates with a high melting point are generated, and it is necessary to periodically remove them. Removal of this carbonate is extremely dangerous, and the removed carbonate coexists with nitrates and nitrites, so it cannot be easily disposed of as a pollution control measure. In addition, in such salt cleaning, it was extremely difficult to thoroughly clean the threads because the carbides of the polymer and solid matter generated by reactions of various metal salts contained in the polymer stuck to the threading device. .
そのため、ソルト洗浄を繰返し行ない、更に洗浄後顧微
鏡で観察しながら欧質金属針で固着物を除去する必要が
あった。Therefore, it was necessary to repeatedly perform salt cleaning, and after cleaning, remove the stuck substances with a metal needle while observing with a microscope.
かようにソルト洗浄を繰返し行ない、更に顕微鏡によっ
て固着物を除去することは、労力、資源、エネルギーの
点から極めて不経済であるばかりか、労働衛生上におい
ても好ましくない。本発明者は、ソルト洗浄や顕微鏡に
よる金属針清掃を行なわずに、完全に洗浄再生する方法
について鋭意研究した結果、本発明に到達したものであ
る。Repeating salt washing in this way and then removing adhered substances using a microscope is not only extremely uneconomical in terms of labor, resources, and energy, but also undesirable in terms of occupational health. The present inventor has arrived at the present invention as a result of intensive research into a method for completely cleaning and regenerating the metal needle without salt cleaning or cleaning the metal needle using a microscope.
即ち、本発明は熱可塑性合成重合体の溶融欲糸に使用し
た紡糸装置を加熱して該装置の付着物を炭化せしめた後
スルフアミン酸水溶液に浸贋処理し、次いでアルカリ金
属の炭酸塩及び/又はアルカリ金属の重炭酸塩の水溶液
に浸漬処理することを特徴とする薮糸装置の洗浄方法で
ある。That is, in the present invention, a spinning device used for melting a thermoplastic synthetic polymer is heated to carbonize the deposits on the device, and then immersed in an aqueous sulfamic acid solution, and then alkali metal carbonate and/or Alternatively, there is a method for cleaning a bush thread device, which is characterized by immersion treatment in an aqueous solution of bicarbonate of an alkali metal.
本発明において言う級糸装置とは、熱可塑性合成重合体
の溶融紡糸に使用した紡糸口金及びパック部品全てを言
い、分解して洗浄に供するのが好ましい。In the present invention, the term "grading device" refers to all the spinnerets and pack parts used for melt-spinning thermoplastic synthetic polymers, and it is preferable to disassemble them and use them for cleaning.
また、ここで言う熱可塑性合成重合体は、溶融級糸に供
する重合体であり、特にポリエチレンテレフタレートの
如き線状ポリエステル系重合体、ポリアミド系重合体、
ポリオレフィン系重合体を主たる対象とする。第1の処
理である加熱は、級糸装置に付着している重合体成分を
炭化させるためのものであり、加熱温度は付着重合体の
種類、量等によって異なるが、通常350oo以上、好
ましくは400oo以上である。In addition, the thermoplastic synthetic polymer referred to herein refers to a polymer that is used to make melt-grade yarn, and in particular, linear polyester polymers such as polyethylene terephthalate, polyamide polymers,
The main target is polyolefin polymers. The first treatment, heating, is to carbonize the polymer component adhering to the grader, and the heating temperature varies depending on the type and amount of the adhering polymer, but is usually 350 oo or higher, preferably It is 400oo or more.
具体的には、電気炉で加熱しても、金属球等の媒体を用
いて流動床で加熱しても、焼却炉内で重油の如き可燃物
の燃焼によって加熱しても、また重合体成分自体を燃焼
させてもよい。第2の処理に使用するスルフアミン酸水
溶液の濃度は、通常1重量%以上、好ましくは5重量%
以上であり、その上限は特になく飽和状態を越えても差
支えない。Specifically, the polymer component It may also burn itself. The concentration of the sulfamic acid aqueous solution used in the second treatment is usually 1% by weight or more, preferably 5% by weight.
This is the above, and there is no particular upper limit, and there is no problem even if the saturation state is exceeded.
処理時間は約1■ご以上が望ましく、60〜200分行
なうのが好ましい。また処理液の温度は、スルフアミン
酸の分解温度以下であればよく、通常5〜5000、好
ましくは20〜40qoの範囲であり、室温で充分であ
る。従って、前記加熱処理後50oo程度以下に冷却し
た後スルフアミン酸水溶液に浸債するのが好ましく、第
1の処理後一旦水洗してこの第2の処理に供してもよい
。この浸薄に際して櫨梓機、ェアレーション又は口金パ
ックの移動によって液を凝拝してもよい。第3の処理に
使用するアルカリ金属の炭酸塩又は重炭酸塩としては、
具体的には炭酸ナトリウム、炭酸カリウ」と丁、炭酸リ
チウム、炭酸水素ナトリウム、炭酸水素カリウム、炭酸
水素リチウムであり、これらは1種のみ単独でも、2種
以上併用してもよい。The treatment time is preferably about 1 inch or more, and preferably 60 to 200 minutes. The temperature of the treatment liquid may be lower than the decomposition temperature of sulfamic acid, and is usually in the range of 5 to 5,000 qo, preferably 20 to 40 qo, and room temperature is sufficient. Therefore, after the heat treatment, it is preferable to cool down to about 50 oo or less and then immerse it in an aqueous sulfamic acid solution.After the first treatment, it may be washed with water and then subjected to the second treatment. During this immersion, the liquid may be immersed by using a dipping machine, aeration, or moving the cap pack. The alkali metal carbonate or bicarbonate used in the third treatment includes:
Specifically, they include sodium carbonate, potassium carbonate, lithium carbonate, sodium hydrogen carbonate, potassium hydrogen carbonate, and lithium hydrogen carbonate, and these may be used alone or in combination of two or more.
かかる(重)炭酸塩の濃度は、浸薄する口金パックに付
着しているスルフアミン酸と反応して発泡する程度であ
ればよく、極めて広い範囲をとることができる。例えば
2〜1の重量%で充分に目的を達成することができる。
処理温度は任意でよく、室温で充分である。第1の加熱
処理した級糸装置には、炭化物、その他の固着物が相当
量付着しており、特に口金の細孔内には多量付着してい
る。The concentration of the (bi)carbonate may be within a very wide range as long as it reacts with the sulfamic acid attached to the die pack to be diluted and foams. For example, a content of 2 to 1% by weight can sufficiently achieve the purpose.
The treatment temperature may be arbitrary, and room temperature is sufficient. A considerable amount of carbide and other fixed substances are attached to the first heat-treated yarn device, and a large amount is especially attached to the inside of the pores of the spinneret.
これを第2のスルフアミン酸水溶液に浸漬処理すること
により、固着物と器壁の間にスルフアミン酸が浸透して
固着物はほぼ脱離する。しかし紬孔内や複雑な構造の部
分には固着物が残留しているが、この残留物はスルフア
ミン酸により極めて脱離し易い状態になっている。この
ようにスルフアミン酸水溶液によって処理した紙糸装置
は、残留している固着物と器壁との間にスルフアミン酸
が浸透しており、また紬孔部や複雑な構造の部分等には
スルフアミン酸水溶液が保持されている。従って、かか
る筋糸装置を第3のアルカリ金属の(重)炭酸塩水溶液
に浸債すると、酸−塩基の中和反応によって瞬時に炭酸
ガスの発泡が起り、紡糸装置に残留している固着物は完
全に脱離される。このように第1〜第3の処理を順次行
なうことによって、紡糸装置の洗浄は完全に行なわれる
。By immersing this in a second sulfamic acid aqueous solution, the sulfamic acid penetrates between the stuck material and the vessel wall, and most of the stuck material is removed. However, there are some fixed substances left inside the pongee holes and in parts with complicated structures, but these residues are in a state where they are extremely easy to be removed by sulfamic acid. In paper yarn devices treated with an aqueous sulfamic acid solution, the sulfamic acid has penetrated between the remaining adherents and the vessel wall, and the sulfamic acid has penetrated into the holes and parts with complicated structures. Aqueous solution is retained. Therefore, when such a yarn device is immersed in a third alkali metal (bi)carbonate aqueous solution, carbon dioxide gas is instantly foamed due to the acid-base neutralization reaction, and the stuck substances remaining in the spinning device are removed. is completely removed. By sequentially performing the first to third treatments in this manner, the spinning apparatus is completely cleaned.
第3の処理後の綾糸装置は水洗、乾燥すればそのまま再
使用できる。この水洗には任意の方法が採用される。紡
糸装置を水中に浸潰してもよく、この際灘畔装置やェア
レーション等によって損拝を行なってもよい。また水を
噴出せしめても、水にかえてスチームを噴射してもよい
。特にスチームを噴射することは、万一残留物があって
もこの噴射によって除去されるので、好ましい。また、
乾燥についても任意の方法、例えば熱による乾燥、自然
乾燥、圧空吹付による乾燥等によって行われる。本発明
の方法によれば、ソルト洗浄や顕微鏡観察による金属針
清掃を行なうことなく、紡糸口金パックを完全に洗浄再
生でき、再生に要する作業能率を大中に向上させること
ができ、更に、洗浄不良による製糸工程における不良、
例えば口金面における糸条の曲り、織糸工程や延伸工程
におけるラップや断糸の発生、毛羽の発生等を改善する
ことができる。The twill yarn device after the third treatment can be reused as is by washing with water and drying. Any method can be used for this water washing. The spinning device may be submerged in water, and at this time, worship may be performed using a nada device, aeration, or the like. Furthermore, water may be ejected, or steam may be ejected instead of water. In particular, it is preferable to inject steam because even if there is any residue, it will be removed by this injection. Also,
Drying can also be carried out by any method, such as drying by heat, natural drying, drying by compressed air spraying, etc. According to the method of the present invention, the spinneret pack can be completely cleaned and regenerated without salt cleaning or metal needle cleaning by microscopic observation, and the work efficiency required for regeneration can be greatly improved. Defects in the spinning process due to defects,
For example, it is possible to improve the bending of the yarn on the spinneret surface, the occurrence of wrapping or yarn breakage in the weaving process or the stretching process, the occurrence of fuzz, etc.
以下に実施例をあげて本発明を更に詳述する。The present invention will be explained in further detail by giving examples below.
実施例 1ポリエチレンテレフタレートの溶融紡糸に使
用した紡糸パックを分解した。Example 1 A spinning pack used for melt spinning polyethylene terephthalate was disassembled.
口金はsus316ステンレス製の直径17仇舷、厚さ
1比舷、孔数96川固、孔径0.3肋であり、他のパッ
ク部品はsus304ステンレス製であった。この分解
した口金とパック部品を電気炉に入れて600℃で4時
間加熱した後、取り出して冷却後40℃の1の重量%ス
ルフアミン酸水溶液に3時間浸潰し、スルフアミン酸水
溶液が付着している状態で室温の5重量%炭酸ナトリウ
ム水溶液に1分間浸潰した。浸糟と同時に発泡が生じた
。浸債後取出して水洗し、3k9/嫌Gのスチームを5
分間噴射し、次いで圧空を吹き付けて乾燥した。パック
部品は完全に洗浄されており、固着物は全く残留してい
なかった。また、口金は顕微鏡で観察したところ固着物
が残留している孔は1孔もなく完全に洗浄されていた。
実施例 2
実施例1と同様にして電気炉で加熱処理後冷却した口金
とパック部品を40つCの15重量%スルフアミン酸水
溶液に2時間浸潰し、続いて室温の1の重量%炭酸水素
カリウム水溶液に2分間浸潰した。The cap was made of SUS 316 stainless steel, with a diameter of 17 m, a thickness of 1 m, 96 holes, and a hole diameter of 0.3, and the other pack parts were made of SUS 304 stainless steel. The disassembled cap and pack parts were placed in an electric furnace and heated at 600°C for 4 hours, then taken out, cooled, and immersed in a 1% by weight sulfamic acid aqueous solution at 40°C for 3 hours, so that the sulfamic acid aqueous solution adhered In this state, it was immersed in a 5% by weight aqueous sodium carbonate solution at room temperature for 1 minute. Foaming occurred simultaneously with erosion. After soaking the bond, take it out, wash it with water, and apply 3k9/5g of steam.
It was sprayed for a minute and then dried by blowing with compressed air. The pack parts were thoroughly cleaned and no deposits remained. Furthermore, when the cap was observed under a microscope, it was found that it had been completely cleaned, with no holes in which any solid matter remained.
Example 2 The cap and pack parts, which had been heat-treated in an electric furnace and cooled in the same manner as in Example 1, were immersed in a 15% by weight aqueous solution of sulfamic acid at 40 C for 2 hours, followed by 1% by weight potassium bicarbonate at room temperature. Soaked in aqueous solution for 2 minutes.
取出して水洗した後圧空を吹き付けて乾燥した。口金、
パック部いずれも完全に洗浄されていた。比較例実施例
1と同様の紙糸済みの分解した口金とパック部品を、硝
酸ナトリウム6の重量%、亜硝酸ナトリウム35重量%
及び水酸化ナトリウム5重量%からなる40000の溶
融液に浸潰した。After taking it out and washing it with water, it was dried by blowing compressed air. cap,
All pack parts were thoroughly cleaned. Comparative Example The same disassembled cap and pack parts with paper thread as in Example 1 were mixed with 6% by weight of sodium nitrate and 35% by weight of sodium nitrite.
and 40,000 mol of 5% by weight of sodium hydroxide.
浸簿と同時に猛烈な火炎を生じてソルトが吹き上げ、こ
ぼれそうになった。5ぴ分浸糟後水洗し、圧空によって
乾燥した。As soon as the tank was immersed, a fierce flame erupted and the salt was blown up, almost spilling over. After soaking for 5 minutes, it was washed with water and dried using compressed air.
Claims (1)
を加熱して該装置の付着物を炭化せしめた後スルフアミ
ン酸水溶液に浸漬処理し、次いでアルカリ金属の炭酸塩
及び/又はアルカリ金属の重炭酸塩の水溶液に浸漬処理
することを特徴とする紡糸装置の洗浄方法。 2 スルフアミン酸水溶液の濃度が1重量%以上である
特許請求の範囲第1項記載の紡糸装置の洗浄方法。 3 アルカリ金属の炭酸塩及び/又はアルカリ金属の重
炭酸塩の水溶液で処理した後更にスチームで処理する特
許請求の範囲第1項又は第2項記載の紡糸装置の洗浄方
法。 4 熱可塑性合成重合体が線状ポリエステル系重合体、
ポリアミド系重合体及びポリオレフイン系重合体よりな
る群から選ばれた少なくとも一種の熱可塑性合成重合体
である特許請求の範囲第1項〜第3項いずれか1項記載
の紡糸装置の洗浄方法。[Claims] 1. A spinning device used for melt spinning a thermoplastic synthetic polymer is heated to carbonize the deposits on the device, and then immersed in an aqueous sulfamic acid solution, and then treated with an alkali metal carbonate and/or Or, a method for cleaning a spinning device, which comprises immersing it in an aqueous solution of an alkali metal bicarbonate. 2. The method for cleaning a spinning device according to claim 1, wherein the concentration of the sulfamic acid aqueous solution is 1% by weight or more. 3. The method for cleaning a spinning device according to claim 1 or 2, which comprises treating with an aqueous solution of alkali metal carbonate and/or alkali metal bicarbonate and then further treating with steam. 4 The thermoplastic synthetic polymer is a linear polyester polymer,
The method for cleaning a spinning device according to any one of claims 1 to 3, wherein the cleaning method is at least one thermoplastic synthetic polymer selected from the group consisting of polyamide polymers and polyolefin polymers.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12863777A JPS6025523B2 (en) | 1977-10-28 | 1977-10-28 | How to clean spinning equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12863777A JPS6025523B2 (en) | 1977-10-28 | 1977-10-28 | How to clean spinning equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5464120A JPS5464120A (en) | 1979-05-23 |
| JPS6025523B2 true JPS6025523B2 (en) | 1985-06-19 |
Family
ID=14989731
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12863777A Expired JPS6025523B2 (en) | 1977-10-28 | 1977-10-28 | How to clean spinning equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6025523B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6296475U (en) * | 1985-12-10 | 1987-06-19 |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110820054B (en) * | 2019-11-22 | 2021-04-27 | 蓝星(成都)新材料有限公司 | A cleaning method for aramid 1414 spinneret |
-
1977
- 1977-10-28 JP JP12863777A patent/JPS6025523B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6296475U (en) * | 1985-12-10 | 1987-06-19 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5464120A (en) | 1979-05-23 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104532409B (en) | Waste clothing recycling pre-treatment technology | |
| GB2139607A (en) | Production of pure carbonized polyacrylonitrile material | |
| CN107541797B (en) | The high-efficiency washing method of polyacrylonitrile-based carbon fibre dry-jet wet-spinning special spinning jet | |
| US3294489A (en) | Process for preparing carbon fibers | |
| WO2022047843A1 (en) | Technological method for regenerating flame retardant polyester fiber by recycling polyester fiber | |
| CN202666707U (en) | Manufacturing device for porous hollow fiber membrane | |
| JP2001516404A (en) | Method for producing active fabric made of carbon fiber | |
| CN105671652A (en) | Combined cleaning method for spinneret plate | |
| JPS6025523B2 (en) | How to clean spinning equipment | |
| US3485670A (en) | Processes for cleaning apparatus used in processing poly(ethylene-terephthalate) | |
| CN101182648A (en) | Fine-denier filament spinneret ethanediol cleaning process | |
| EP1354082B1 (en) | Method for producing hollow rayon fibers | |
| GB1600640A (en) | Method of removing alkali and alkaline earth impurities from carbonizable polyacrylonitrile material | |
| JP2009155769A (en) | Cleaning method for polyester melt spinneret | |
| JPH0319906A (en) | Cleaning of melt-spinning spinneret | |
| CN109794459A (en) | A kind of polyester fondant filter element cleaning technique | |
| JPS6025522B2 (en) | How to clean the spinneret pack | |
| CN106006638A (en) | Preparation method of high-penetration microporous granular active carbon | |
| CN220758354U (en) | Filter equipment washing system | |
| US3188239A (en) | Spinneret cleaning process | |
| CN110820055A (en) | Efficient cleaning method for mesophase pitch melt spinning spinneret plate | |
| JPS622044B2 (en) | ||
| CN1062773A (en) | Cleaning method of polyester fondant filter core | |
| JPS5812931B2 (en) | How to clean the cap filter | |
| JP2022102186A (en) | Carbon fiber recovery method |