JPH0674525B2 - Method for circulating cleaning liquid of polymerization equipment - Google Patents

Method for circulating cleaning liquid of polymerization equipment

Info

Publication number
JPH0674525B2
JPH0674525B2 JP59026975A JP2697584A JPH0674525B2 JP H0674525 B2 JPH0674525 B2 JP H0674525B2 JP 59026975 A JP59026975 A JP 59026975A JP 2697584 A JP2697584 A JP 2697584A JP H0674525 B2 JPH0674525 B2 JP H0674525B2
Authority
JP
Japan
Prior art keywords
cleaning liquid
cleaning
polymerization
storage tank
spinning device
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 - Lifetime
Application number
JP59026975A
Other languages
Japanese (ja)
Other versions
JPS60173109A (en
Inventor
芳信 外池
壽 田沢
和彦 斉藤
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP59026975A priority Critical patent/JPH0674525B2/en
Publication of JPS60173109A publication Critical patent/JPS60173109A/en
Publication of JPH0674525B2 publication Critical patent/JPH0674525B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Cleaning In General (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)

Description

【発明の詳細な説明】 〔本発明の技術分野〕 本発明は重合装置内部を洗浄するための洗浄液循環によ
る洗浄方法に関する。
Description: TECHNICAL FIELD OF THE INVENTION The present invention relates to a cleaning method by circulating a cleaning liquid for cleaning the inside of a polymerization apparatus.

〔従来技術とその問題点〕[Prior art and its problems]

従来、重合を行う装置や重合と紡糸とを行う装置の内面
の洗浄はスケール除去の目的で行なうものが多く、主と
して酸、アルカリ、あるいは溶剤による溶解、分解作用
を利用した洗浄方法が使用されている。
Conventionally, cleaning of the inner surface of an apparatus for performing polymerization or an apparatus for performing polymerization and spinning is often performed for the purpose of removing scale, and a cleaning method utilizing dissolution or decomposition action mainly with an acid, an alkali, or a solvent is used. There is.

ところが酸洗浄、アルカリ洗浄では装置材質の腐食とい
う問題が避けられず、又溶剤洗浄も単に溶剤を送入、排
出を繰返すだけではなかなか目的とする清浄レベルに達
しなかった。
However, acid cleaning and alkali cleaning cannot avoid the problem of corrosion of the equipment material, and solvent cleaning does not reach the target cleaning level simply by repeatedly feeding and discharging the solvent.

一方半導体分野等で多く行なわれている精密洗浄として
蒸気洗浄、あるいは超音波洗浄等があるがそれぞれ不満
足な面が多く十分なものでなかった。
On the other hand, as precision cleaning often performed in the semiconductor field and the like, there are steam cleaning, ultrasonic cleaning and the like, but there are many unsatisfactory aspects and they are not sufficient.

例えば蒸気洗浄においては加熱により蒸発させ降温によ
り凝縮させるという方式をとるため、有機物の溶解力も
小さく、蒸発に要する時間、エネルギー等からみてきわ
めて洗浄効率が悪いものであった。
For example, in vapor cleaning, since a method of evaporating by heating and condensing by lowering the temperature is adopted, the dissolving power of organic substances is small, and the cleaning efficiency is extremely poor in view of the time and energy required for evaporation.

又超音波洗浄方法は振動子を内部に挿入する必要がある
という問題があるうえ仮に内部に挿入できたとしても装
置内面を均一に洗浄することは振動子の性質上きわめて
困難である。さらに装置外壁に振動子を接触させて行な
う方法も考えられるが、これも共振、接触面形状、取付
方法等数多くの困難な問題があった。
In addition, the ultrasonic cleaning method has a problem that the vibrator needs to be inserted inside, and even if the vibrator can be inserted inside, it is extremely difficult to uniformly clean the inner surface of the device due to the property of the vibrator. Further, a method in which a vibrator is brought into contact with the outer wall of the device is conceivable, but this also has many difficult problems such as resonance, contact surface shape, and mounting method.

しかしながら一方では高純度ポリマー、透明性ポリマー
の製造においては装置内面の精密洗浄に関し強い要望が
あった。
On the other hand, however, in the production of high-purity polymers and transparent polymers, there has been a strong demand for precision cleaning of the inner surface of the device.

例えば透明性を特長とするポリマーには、耐熱性で優れ
ているポリカーボネート、汎用性の高いポリスチレン、
又透明性、耐候性の点でポリメチルメタアクリレート、
及びその共重合体等があるが、その中でも透明性が最も
重要要素となる光ファイバーの場合においては、光導通
路となる芯ポリマーに混在する塵埃の除去がきわめて重
要となる。
For example, polymers that are characterized by transparency include polycarbonate with excellent heat resistance, polystyrene with high versatility,
Also, in terms of transparency and weather resistance, polymethylmethacrylate,
In the case of an optical fiber, of which transparency is the most important factor, the removal of dust mixed in the core polymer to be the optical path is extremely important.

第1図は従来の重合紡糸装置の洗浄装置を説明するもの
で、1は重合紡糸装置、2は洗浄液貯槽、3はミクロフ
ィルターを備えた洗浄液濾過装置である。重合紡糸装置
1と洗浄液貯槽2とはパイプ4により三方コック切替え
コック5を介して接続されており三方コック5の切替え
操作により洗浄ラインからモノマー供給ラインに切替え
可能となされている。
FIG. 1 illustrates a conventional washing device for a polymerization spinning device. Reference numeral 1 is a polymerization spinning device, 2 is a washing liquid storage tank, and 3 is a washing liquid filtering device equipped with a microfilter. The polymerization spinning device 1 and the cleaning liquid storage tank 2 are connected by a pipe 4 via a three-way cock switching cock 5, and the cleaning line can be switched to a monomer supply line by a switching operation of the three-way cock 5.

洗浄液貯槽2の上部にはN2ガス供給ライン6と真空ライ
ン7が接続されており、洗浄液貯槽2を真空ライン7に
より減圧にした後、洗浄液をミクロフィルターにより減
圧濾過することにより濾液が洗浄液貯槽2に貯められ
る。
A N 2 gas supply line 6 and a vacuum line 7 are connected to the upper part of the cleaning liquid storage tank 2, and after the cleaning liquid storage tank 2 is depressurized by the vacuum line 7, the cleaning liquid is filtered under reduced pressure by a microfilter to obtain a filtrate. Can be stored in 2.

重合紡糸装置1の上部にはパイプ8および加・減圧調整
用の三方コック圧力調整弁9を介して減圧ライン10およ
び加圧ライン11が接続されている。なお13はパイプジョ
イントである。
A decompression line 10 and a pressurization line 11 are connected to the upper part of the polymerization spinning device 1 via a pipe 8 and a three-way cock pressure adjustment valve 9 for adjusting pressurization / decompression. Note that 13 is a pipe joint.

洗浄液貯槽に貯められた洗浄液を重合紡糸装置1に送る
には重合紡糸装置の下部に設けたバルブ12を閉じ、次い
で重合紡糸装置内部を真空ライン10により減圧にした
後、洗浄液貯槽2をN2ガスライン6により加圧にするこ
とにより行なわれる。
To send the cleaning liquid stored in the cleaning liquid storage tank to the polymerization spinning device 1, the valve 12 provided at the lower part of the polymerization spinning device is closed, and then the inside of the polymerization spinning device is depressurized by the vacuum line 10, and then the cleaning liquid storage tank 2 is filled with N 2 It is performed by applying pressure through the gas line 6.

移送終了後、切替えコック5と圧力調整弁9をそれぞれ
閉じて重合紡糸装置内部を密閉し、続いて装置本体を加
熱することにより装置内部の加熱洗浄が行なわれる。
After the transfer is completed, the switching cock 5 and the pressure adjusting valve 9 are closed to seal the inside of the polymerization spinning device, and then the device main body is heated to heat and wash the inside of the device.

洗浄が終了した後、直ちにバルブ12を開けると重合紡糸
装置内部に密封された洗浄液のベーパー圧により洗浄液
が排出される。そしてこの操作は所定回数繰返される。
When the valve 12 is opened immediately after the washing is completed, the washing liquid is discharged by the vapor pressure of the washing liquid sealed inside the polymerization spinning device. Then, this operation is repeated a predetermined number of times.

しかしながら、従来方法により繰返し洗浄を行なう場
合、移送した洗浄剤は重合紡糸装置が加熱された状態に
あると、瞬時に蒸発し、その蒸気圧により逆圧がかかり
逆流を起して移送が停止することがあるのみならず、極
端な場合は、逆圧が貯槽まで達して危険な状態を引き起
すことも予想される。このため洗浄を繰返すことに重合
紡糸装置の加熱・冷却を繰返す必要が生じるという問題
があり、洗浄効率が甚だ悪い。
However, in the case where the cleaning is repeatedly performed by the conventional method, the transferred cleaning agent is instantly evaporated when the polymerization spinning device is in a heated state, and a reverse pressure is generated by the vapor pressure of the cleaning agent to stop the transfer. Not only that, but in extreme cases, it is expected that the back pressure will reach the storage tank and cause a dangerous condition. For this reason, there is a problem in that heating and cooling of the polymer spinning device must be repeated in repeating washing, and the washing efficiency is extremely poor.

さらに従来の洗浄装置の場合、重合紡糸装置に連通する
ライン、例えば加・減圧ラインの洗浄がきわめて困難で
あるという問題があった。つまり連通しているラインの
配管内部には前回の重合時に重合紡糸装置より拡酸され
る低分子量成分が薄く堆積することが多く、これがその
後の熱的変化等により細かくヒビ割れ破壊し、微粉末状
の異物として発現し、N2ガス送入時、装置内に送入され
てしまうという問題があった。
Further, in the case of the conventional cleaning device, there is a problem that it is extremely difficult to clean the line communicating with the polymerization spinning device, for example, the pressurizing / depressurizing line. In other words, the low molecular weight components that spread out from the polymerization spinning device during the previous polymerization are often deposited thinly inside the piping of the communicating line, which is finely cracked and broken due to subsequent thermal changes, etc. There is a problem that the foreign matter appears as a foreign substance and is fed into the apparatus when N 2 gas is fed.

〔本発明の目的〕[Purpose of the present invention]

本発明の目的は、かかる従来技術の諸欠点を改良し、重
合装置の内面を精密洗浄することが可能な洗浄方法を提
供することにある。
It is an object of the present invention to provide a cleaning method capable of improving various drawbacks of the prior art and capable of precisely cleaning the inner surface of a polymerization apparatus.

〔本発明の構成〕[Configuration of the present invention]

即ち、本発明は次の構成を有する。 That is, the present invention has the following configurations.

(1)加・減圧調整ラインを備えた重合装置と洗浄液貯
槽との間に洗浄液を循環させる配管が配設され、前記洗
浄液貯槽から前記重合装置へと洗浄液を供給する洗浄液
供給ラインに洗浄液濾過用の孔径0.5μm以下のミクロ
フィルターが配設され、かつ、前記重合装置から前記洗
浄液貯槽へと洗浄液を回収する洗浄液回収ラインにルッ
キンググラスが配設されてなる洗浄液循環洗浄装置によ
り、前記重合装置内部を有機溶媒からなる洗浄液で加熱
循環洗浄することを特徴とする重合装置の洗浄液循環洗
浄方法。
(1) A pipe for circulating a cleaning liquid is provided between a polymerization device equipped with a pressurization / decompression adjusting line and a cleaning liquid storage tank, and a cleaning liquid is supplied to a cleaning liquid supply line for supplying the cleaning liquid from the cleaning liquid storage tank to the polymerization device. Of the inside of the polymerization apparatus by a cleaning solution circulation cleaning apparatus in which a microfilter having a pore size of 0.5 μm or less is installed, and a looking glass is installed in a cleaning solution recovery line for recovering the cleaning solution from the polymerization apparatus to the cleaning solution storage tank. A cleaning liquid circulating cleaning method for a polymerization apparatus, wherein the cleaning liquid is heated and circulated with a cleaning liquid made of an organic solvent.

(2)一端が加・減圧調整ラインに連通され、かつ、他
端が洗浄液回収ラインに連通するバイパス回路が設けら
れたことを特徴とする特許請求の範囲第1項記載の重合
装置の洗浄液循環洗浄方法。
(2) A cleaning liquid circulation in a polymerization apparatus according to claim 1, wherein a bypass circuit is provided, one end of which is connected to the pressurization / decompression adjustment line and the other end of which is connected to the cleaning liquid recovery line. Cleaning method.

本発明法に用いる循環洗浄装置は、重合反応が行われる
装置いわゆる重合装置、の内面洗浄用に用いられる。こ
の重合装置は、重合反応により得られたポリマを溶融紡
糸することも兼ねた装置、いわゆる重合紡糸装置であっ
てもよい。
The circulation cleaning device used in the method of the present invention is used for cleaning the inner surface of a device in which a polymerization reaction is carried out, a so-called polymerization device. This polymerization apparatus may be an apparatus that also serves as melt spinning of the polymer obtained by the polymerization reaction, that is, a so-called polymerization spinning apparatus.

以下、本発明法を重合紡糸装置の洗浄に適用した場合の
装置の1実施態様を示す第2図を参照して説明する。第
2図は、重合紡糸装置内を密閉系で洗浄液循環洗浄する
際に好ましいもので、符号は同一又は相当部材を示す。
第2図において、14は重合紡糸装置の上端と洗浄液貯槽
2を結ぶ洗浄液供給ライン、15は重合紡糸装置1の下部
と洗浄液貯槽2とを結ぶ洗浄液回収ラインであり、上記
供給ラインは洗浄液貯槽2と重合紡糸装置1との間に順
次配設された液送ポンプ16、フィルター17、三方コック
5およびこれらを互いに連結するパイプ4並びにパイプ
ジョイント13とから構成され、上記回収ライン15は重合
紡糸装置1と洗浄液貯槽2との間に順次配設されたバル
ブ12、ルッキンググラス18、パイプジョイント13′、三
方バルブ19およびパイプ4′から構成されている。
Hereinafter, description will be given with reference to FIG. 2 showing one embodiment of the apparatus when the method of the present invention is applied to washing of a polymer spinning apparatus. FIG. 2 is preferable when the cleaning liquid circulation cleaning is performed in a closed system in the polymerization spinning device, and the reference numerals indicate the same or corresponding members.
In FIG. 2, 14 is a cleaning liquid supply line connecting the upper end of the polymerization spinning device and the cleaning liquid storage tank 2, 15 is a cleaning liquid recovery line connecting the lower part of the polymerization spinning device 1 and the cleaning liquid storage tank 2, and the supply line is the cleaning liquid storage tank 2 And a polymerization spinning device 1, which are sequentially arranged between the liquid delivery pump 16, the filter 17, the three-way cock 5, and the pipe 4 and the pipe joint 13 that connect these components to each other. The recovery line 15 is a polymerization spinning device. 1 and a cleaning liquid storage tank 2 are sequentially provided with a valve 12, a looking glass 18, a pipe joint 13 ', a three-way valve 19 and a pipe 4'.

重合紡糸装置1の上端に連結された加・減圧用パイプ8
は4方分岐管20に接続され、一方の分岐管は三方コック
21を介して減圧ライン10に接続され、第二の分岐管はバ
ルブ22を介して加圧ライン11に接続され、第三の分岐管
はバルブ23およびパイプ24を介してバルブ12とルッキン
ググラス18との間の回収ラインに接続されている。つま
りパイプ8、4方分岐管20、バルブ23、パイプ24とはバ
イパス回路25を構成している。
A pressurizing / depressurizing pipe 8 connected to the upper end of the polymer spinning device 1.
Is connected to a 4-way branch pipe 20, one branch pipe is a 3-way cock
The second branch pipe is connected to the depressurization line 11 via the valve 21, the second branch pipe is connected to the pressurization line 11 via the valve 22, and the third branch pipe is connected to the valve 12 and the looking glass 18 via the valve 23 and the pipe 24. Is connected to the recovery line between. That is, the pipe 8, the 4-way branch pipe 20, the valve 23, and the pipe 24 form a bypass circuit 25.

次にこの装置により洗浄液による循環洗浄を行なうに
は、まず化学的に十分精錬された洗浄液を貯槽2に入
れ、液送ポンプ16によりミクロフィルターを備えた濾過
装置17に送り加圧濾過を行なう。
Next, in order to carry out the circulation cleaning with the cleaning liquid by this apparatus, first, the cleaning liquid which has been sufficiently refined chemically is put into the storage tank 2 and is fed by the liquid feed pump 16 to the filtration device 17 equipped with a micro filter for pressure filtration.

洗浄液はさらに、三方コック5を通過させ重合紡糸装置
1に送られる。
The cleaning liquid is further passed through the three-way cock 5 and sent to the polymerization spinning device 1.

この場合、重合紡糸装置に洗浄液を一杯に充填させるた
め、バルブ12、22、23は閉にしてバルブ21を大気に解放
にし洗浄液があふれるまで送液を続行する。
In this case, in order to fully fill the polymerization spinning device with the cleaning liquid, the valves 12, 22, 23 are closed and the valve 21 is opened to the atmosphere, and the liquid feeding is continued until the cleaning liquid overflows.

大気解放口より洗浄液があふれたところでバルブ21を閉
にし、バルブ12を開に、3方バルブ19を循環回路側に設
定することにより循環洗浄を開始することができる。
When the cleaning liquid overflows from the atmosphere opening port, the valve 21 is closed, the valve 12 is opened, and the three-way valve 19 is set on the circulation circuit side, whereby the circulation cleaning can be started.

バイパス回路25のみの洗浄を行なう場合はバルブ12を
閉、バルブ23を開にすることにより容易に行なうことが
できる。
When only the bypass circuit 25 is washed, it can be easily performed by closing the valve 12 and opening the valve 23.

もちろん、重合紡糸装置とバイパス回路とを同時に洗浄
することも可能である。
Of course, it is also possible to wash the polymerization spinning device and the bypass circuit at the same time.

循環洗浄の開始と共に重合紡糸装置の加熱装置26を徐々
に昇温し、所定の温度まで上げることにより加熱循環洗
浄が開始される。
When the circulation cleaning is started, the heating device 26 of the polymerization spinning device is gradually heated to a predetermined temperature to start the heating circulation cleaning.

なお、本装置においてはパイプ8に接続する4方分岐管
の分岐点からバルブ21又は22の間は盲孔となり洗浄不良
となる懸念があるので、ポリメチルメタクリレート、ポ
リスチレン、ポリカーボネート等いずれのポリマ用の場
合も、その条件下で沸点以下になるよう重合紡糸装置か
ら4方分岐点の間に冷却部を設けるか、あるいはこれら
の間隔を十分に大きくとり、自然放熱させることにより
4方分岐点以後で低分子量成分が付着しないように配慮
することが望ましい。
In addition, in this device, there is a concern that a blind hole is formed between the branch point of the 4-way branch pipe connected to the pipe 8 and the valve 21 or 22 to cause poor cleaning. Therefore, for any polymer such as polymethylmethacrylate, polystyrene, or polycarbonate. In the case of, the cooling part is provided between the polymerization spinning device and the four-way branch points so that the boiling point is not more than the boiling point under these conditions, or the space between them is set to a sufficiently large value to allow natural heat dissipation, and then Therefore, it is desirable to consider that low molecular weight components do not adhere.

さらに、本発明では洗浄効率を上げる手段として、洗浄
系内を解放系で行なうこともできる。
Further, in the present invention, as a means for improving the cleaning efficiency, the inside of the cleaning system may be an open system.

即ち、重合紡糸装置に付設した加熱装置の温度を洗浄液
の大気下での沸点以上にし、系内の一部、例えば洗浄液
貯槽を開放系にすることにより重合紡糸装置内部で洗浄
液の沸騰を起し、そのバブリング効果により重合紡糸装
置内面をより効率的に洗浄することができる。
That is, the temperature of the heating device attached to the polymerization spinning device is made equal to or higher than the boiling point of the cleaning liquid in the atmosphere, and a part of the system, for example, the cleaning liquid storage tank is opened to cause boiling of the cleaning liquid inside the polymerization spinning device. The bubbling effect makes it possible to wash the inner surface of the polymerization spinning device more efficiently.

第3図は開放系の洗浄液貯槽を例示したもので、イは貯
槽上部を閉塞するとともに側面に水平に伸びる開放部
2′を設けたもので、洗浄液の沸騰により生ずるベーパ
ーの排出流によって大気中の塵埃の侵入を防止可能であ
る。
FIG. 3 shows an example of an open type cleaning liquid storage tank, in which (a) is provided with an opening 2'that horizontally closes the storage tank and extends horizontally to the atmosphere due to the vapor discharge of the cleaning liquid. It is possible to prevent dust from entering.

第3図ロは外からの塵埃の混入をより完全に防止するた
め側面に下向きの開口部分2″を設けたものである。
In FIG. 3B, a downward opening portion 2 ″ is provided on the side surface in order to more completely prevent the entry of dust from the outside.

本発明においては洗浄装置各要素を連結するパイプジョ
イントも気密性、発塵の問題からきわめて重要であり、
気密性が悪いと系外から確実に塵埃の取り込みが発生
し、逆に気密性を主に考えると材質上の問題(発塵)を
生じるので注意の必要がある。
In the present invention, the pipe joint connecting the respective elements of the cleaning device is also very important from the problems of airtightness and dust generation,
If airtightness is poor, dust will be reliably taken in from the outside of the system, and conversely, if airtightness is mainly considered, problems with the material (dust generation) will occur, so caution is required.

本発明で使用するミクロフィルターとはメンブラン状の
絶対濾過型フィルターであり、水銀ポロシメーターによ
る孔径値が0.5μm以下、好ましくは0.2μm以下のもの
であり、該当するものとしてセルロースエステル、ポリ
オレフィン、ポリテトラフロロエチレン、ポリカーボネ
ート、ポリアミド等があるが耐薬品性、耐熱性の点から
ポリテトラフロロエチレンが最も好ましい。
The microfilter used in the present invention is a membrane type absolute filtration type filter having a pore size value by mercury porosimeter of 0.5 μm or less, preferably 0.2 μm or less. Applicable ones are cellulose ester, polyolefin and polytetrahydrofuran. Although there are fluoroethylene, polycarbonate, polyamide and the like, polytetrafluoroethylene is most preferable from the viewpoint of chemical resistance and heat resistance.

又、洗浄液の循環方向は、重合紡糸装置の下から上への
上方向(図示なし)、あるいは、上から下への下方向
(第2図)のどちらでも行なえる。
Further, the circulation direction of the washing liquid can be either from the bottom to the top of the polymerization spinning device (not shown) or from the top to the bottom (FIG. 2).

洗浄された重合紡糸装置内面の清浄レベルの評価は、サ
ンプリングのため一旦系外に取り出すことなく重合紡糸
装置出口直後に設けられたルッキンググラスにレンズ系
で光源を絞ったハロゲンランプを照射するとにより発現
する輝点を観測することにより行なうことができる。
The evaluation of the cleanliness level of the inner surface of the washed polymerization spinning device was expressed by irradiating a halogen lamp with a light source narrowed with a lens system to the looking glass provided immediately after the exit of the polymerization spinning device for sampling without taking it out of the system. This can be done by observing the bright spots that

本発明によると、清浄レベルの評価は洗浄作業中同時に
行なう事が可能であり、観測される輝点が10cm光路当り
完全に0になるまで行なう方法がとれる。
According to the present invention, the evaluation of the cleaning level can be carried out simultaneously during the cleaning operation, and the method can be carried out until the observed bright spot becomes completely 0 per 10 cm optical path.

洗浄が終った後は、洗浄液を完全に除去するためバルブ
12およびバルブ23のみ開とし、他は全て閉にしバルブ19
を排出側(第2図では下方側)に切り替え洗浄液を蒸気
圧により排出する。次いで直ちにバルブ12、23を閉じ、
バルブ21を真空ライン10側に切り替え1〜10-2Torrの真
空度で真空乾燥を行ない重合紡糸装置内面に有機物およ
び塵埃が完全にない状態にする。
After cleaning, use the valve to completely remove the cleaning solution.
Only valve 12 and valve 23 are open, all others are closed and valve 19
To the discharge side (lower side in FIG. 2) and the cleaning liquid is discharged by vapor pressure. Then immediately close valves 12, 23,
The valve 21 is switched to the vacuum line 10 side, and vacuum drying is performed at a vacuum degree of 1 to 10 -2 Torr to completely remove organic substances and dust from the inner surface of the polymerization spinning device.

本発明において適用される洗浄液としては、メチルメタ
アクリレート、酢酸メチル等のエステル類、アセトン、
メチルエチルケトン等のケトン類、ヘキサン、ヘプタン
等の炭化水素類、ベンゼン、トルエン等の芳香族系炭化
水素類、メチルセロソロブ、エチルエーテル等のエーテ
ル類、メチルアルコール、エチルアルコール等のアルコ
ール類等の有機溶媒が用いられ、ポリマーに対する溶解
性、沸点、蒸発速度等を考慮して選択使用される。
The cleaning liquid applied in the present invention includes methyl methacrylate, esters such as methyl acetate, acetone,
Ketones such as methyl ethyl ketone, hydrocarbons such as hexane and heptane, aromatic hydrocarbons such as benzene and toluene, ethers such as methyl cellosolve and ethyl ether, and organic solvents such as alcohols such as methyl alcohol and ethyl alcohol. It is selected and used in consideration of solubility with respect to polymer, boiling point, evaporation rate and the like.

重合紡糸装置にポリマーや他の有機物が大量に残存して
いる場合は、洗浄液を一旦重合紡糸装置に貯めた後排出
するといった操作を繰り返し、ポリマー及び有機物の濃
度を少なくとも0.1%以下にしてから加熱循環洗浄を行
なうのが装置保全、洗浄効率の面から好ましい。
If a large amount of polymers and other organic substances remain in the polymerization spinning device, repeat the operation of temporarily storing the cleaning liquid in the polymerization spinning device and then discharging it, and heat the mixture until the concentration of the polymer and organic substances is at least 0.1% or less. Circulating cleaning is preferable from the viewpoints of equipment maintenance and cleaning efficiency.

なお、上述説明では重合紡糸装置の循環洗浄装置につい
て説明したが、本発明の循環洗浄装置は、重合のみを行
なう装置にも勿論適用可能であり、特に、高純度ポリマ
や透明ポリマ等を製造する重合装置の内面洗浄用として
有用である。
In the above description, the circulation cleaning device of the polymerization spinning device has been described, but the circulation cleaning device of the present invention can of course be applied to a device that only performs polymerization, and particularly produces a high-purity polymer or a transparent polymer. It is useful for cleaning the inner surface of polymerization equipment.

[本発明の効果] 本発明は上述のごとく構成したもので、洗浄効率がきわ
めて優れているうえ、装置内面の精密洗浄を確実にしか
も完全に実施できるという顕著な実用効果を奏するもの
である。
[Effects of the Present Invention] The present invention configured as described above has a remarkable practical effect that the cleaning efficiency is extremely excellent and precision cleaning of the inner surface of the apparatus can be performed reliably and completely.

以下、本発明の効果を実施例により具体的に説明する。Hereinafter, the effects of the present invention will be specifically described with reference to examples.

実施例1 第2図に示す装置により開放系加熱洗浄を実施した。Example 1 An open heating cleaning was carried out by the apparatus shown in FIG.

洗浄液貯槽の材質はステンレスであり、液送ポンプは液
接する部分の材質がテトラフロロエチレンとステンレス
のみから成るギヤポンプ((株)イワキ製)を使用し
た。
The material of the cleaning liquid storage tank was stainless steel, and the liquid feed pump used was a gear pump (manufactured by Iwaki Co., Ltd.) in which the material in contact with the liquid consisted only of tetrafluoroethylene and stainless steel.

ミクロフィルターは、水銀ポロシメーターによる値が0.
1μmである孔径を有するテトラフロロエチレンメンブ
レンフィルター(住友電工(株)製)をステンレス製フ
ィルターホルダーに装填して使用した。
The microfilter has a mercury porosimeter value of 0.
A tetrafluoroethylene membrane filter (manufactured by Sumitomo Electric Co., Ltd.) having a pore size of 1 μm was loaded into a stainless steel filter holder and used.

洗浄系路を構成する配管は、テトラフロロエチレンパー
フロロビニルエーテル製のチューブを使用し接続部のジ
ョイントには、“スエージロック”(スエージロック・
カンパニー製)を使用した。
The pipes that make up the cleaning system use tubes made of tetrafluoroethylene perfluorovinyl ether, and the joints at the connection are "Sagelock" (Sagelock
Manufactured by Company) was used.

洗浄液には、電子工業用アセトン((株)関東化学製)
を使用し、液送ポンプにより送られる洗浄液は一旦重合
紡糸装置に貯めた後、重合紡糸装置とバイパス回路とを
同時に流し、循環洗浄を開始した。重合紡糸装置の加熱
装置を80℃に昇温し加熱循環洗浄を連続で3時間行なっ
た。
Acetone for electronic industry (Kanto Chemical Co., Ltd.)
The cleaning liquid fed by the liquid feed pump was once stored in the polymerization spinning device, and then the polymerization spinning device and the bypass circuit were simultaneously flown to start circulation cleaning. The heating device of the polymerization spinning device was heated to 80 ° C., and heating and circulation washing was continuously performed for 3 hours.

その結果は表−1示す通りきわめて優れたものであっ
た。
The results were extremely excellent as shown in Table 1.

尚、本洗浄液を回収し無機分析を行なった結果PPbオー
ダーにおいても、ブランク品からの増加分は見られなか
った。
In addition, as a result of collecting this cleaning liquid and performing an inorganic analysis, no increase was observed from the blank product even in the PPb order.

比較例1 洗浄装置として第1図に示す装置を使用し、洗浄液貯
槽、ミクロフィルター、配管パイプ、洗浄液は実施例1
と同様のものを使用した。又、パイプジョイントとして
“スエージロック”(スエージロック・カンパニー製)
を使用した。
Comparative Example 1 The apparatus shown in FIG. 1 was used as the cleaning apparatus, and the cleaning solution storage tank, microfilter, piping pipe, and cleaning solution were used in Example 1.
The same as was used. Also, as a pipe joint, "Sagelock" (made by Swagelock Company)
It was used.

洗浄液の移送は、重合紡糸装置を真空にし、洗浄液貯槽
をN2ガスにて0.5Kg/cm2程度加圧し、その差圧により移
送した。
The cleaning liquid was transferred by vacuumizing the polymerization spinning device, pressurizing the cleaning liquid storage tank with N 2 gas at about 0.5 kg / cm 2 , and transferring the cleaning liquid by the pressure difference.

洗浄液は重合紡糸装置本体で130℃に加熱し30分間洗浄
に供した後排出した。
The washing liquid was heated to 130 ° C. in the main body of the polymerization spinning device, washed for 30 minutes, and then discharged.

引続き洗浄液の移送を可能にするため重合紡糸装置本体
の冷却を30分間行なった。
Subsequently, the main body of the polymerization spinning device was cooled for 30 minutes so that the cleaning liquid could be transferred.

本操作を16回繰り返し行なった結果を表−1に示すが全
く不満足なものであった。
The results of repeating this operation 16 times are shown in Table 1, but they were completely unsatisfactory.

【図面の簡単な説明】[Brief description of drawings]

第1図は従来の洗浄装置を示す概略図、第2図は本発明
の洗浄装置に例示する概略図、第3図は本発明において
用いられる開放系の洗浄液貯槽を例示する概略図であ
る。1:重合紡糸装置 2:洗浄液貯槽 17:濾過装置 18:ルッキンググラス 14:洗浄液供給ライン 15:洗浄液回収ライン 25:バイパス回路
FIG. 1 is a schematic diagram showing a conventional cleaning device, FIG. 2 is a schematic diagram illustrating the cleaning device of the present invention, and FIG. 3 is a schematic diagram illustrating an open-system cleaning liquid storage tank used in the present invention. 1: Polymerization spinning device 2: Cleaning liquid storage tank 17: Filtration device 18: Looking glass 14: Cleaning liquid supply line 15: Cleaning liquid recovery line 25: Bypass circuit

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭55−46350(JP,A) 特開 昭51−50885(JP,A) 実開 昭54−75068(JP,U) 実開 昭57−111381(JP,U) ─────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-55-46350 (JP, A) JP-A-51-50885 (JP, A) Actually opened 54-75068 (JP, U) Actual-opened 57- 111381 (JP, U)

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】加・減圧調整ラインを備えた重合装置と洗
浄液貯槽との間に洗浄液を循環させる配管が配設され、
前記洗浄液貯槽から前記重合装置へと洗浄液を供給する
洗浄液供給ラインに洗浄液濾過用の孔径0.5μm以下の
ミクロフィルターが配設され、かつ、前記重合装置から
前記洗浄液貯槽へと洗浄液を回収する洗浄液回収ライン
にルッキンググラスが配設されてなる洗浄液循環洗浄装
置により、前記重合装置内部を有機溶媒からなる洗浄液
で加熱循環洗浄することを特徴とする重合装置の洗浄液
循環洗浄方法。
1. A pipe for circulating a cleaning liquid is provided between a polymerization device equipped with a pressurization / decompression adjusting line and a cleaning liquid storage tank,
A cleaning liquid recovery line for supplying the cleaning liquid from the cleaning liquid storage tank to the polymerization device is provided with a microfilter having a pore size of 0.5 μm or less for filtering the cleaning liquid, and the cleaning liquid recovery from the polymerization device to the cleaning liquid storage tank. A cleaning liquid circulation cleaning method for a polymerization device, wherein the inside of the polymerization device is heated and circulatingly cleaned with a cleaning liquid composed of an organic solvent by a cleaning liquid circulation cleaning device having a line of a looking glass.
【請求項2】一端が加・減圧調整ラインに連通され、か
つ、他端が洗浄液回収ラインに連通するバイパス回路が
設けられたことを特徴とする特許請求の範囲第1項記載
の重合装置の洗浄液循環洗浄方法。
2. A polymerization apparatus according to claim 1, further comprising a bypass circuit, one end of which is connected to the pressurization / decompression adjustment line and the other end of which is connected to the cleaning liquid recovery line. Cleaning solution circulation cleaning method.
JP59026975A 1984-02-17 1984-02-17 Method for circulating cleaning liquid of polymerization equipment Expired - Lifetime JPH0674525B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59026975A JPH0674525B2 (en) 1984-02-17 1984-02-17 Method for circulating cleaning liquid of polymerization equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59026975A JPH0674525B2 (en) 1984-02-17 1984-02-17 Method for circulating cleaning liquid of polymerization equipment

Publications (2)

Publication Number Publication Date
JPS60173109A JPS60173109A (en) 1985-09-06
JPH0674525B2 true JPH0674525B2 (en) 1994-09-21

Family

ID=12208157

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59026975A Expired - Lifetime JPH0674525B2 (en) 1984-02-17 1984-02-17 Method for circulating cleaning liquid of polymerization equipment

Country Status (1)

Country Link
JP (1) JPH0674525B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0281307A (en) * 1988-09-19 1990-03-22 Mitsubishi Electric Corp Magnetic head
WO2016013051A1 (en) * 2014-07-21 2016-01-28 ゼプト株式会社 Nanofibre-forming injection nozzle head, and nanofibre production device equipped with nanofibre-forming injection nozzle head
CN110685023A (en) * 2018-07-05 2020-01-14 宁波方太厨具有限公司 Spinneret cleaning device and method
CN114808154B (en) * 2022-04-23 2023-04-07 浙江毅聚新材料有限公司 Cleaning method of spinning assembly

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6023037Y2 (en) * 1977-11-07 1985-07-09 明治乳業株式会社 liquid storage plant
JPS5546350A (en) * 1978-09-29 1980-04-01 Mitsubishi Heavy Ind Ltd Method of circulating chemical washing liquid through forced circulation boiler
JPS57111381U (en) * 1980-12-26 1982-07-09

Also Published As

Publication number Publication date
JPS60173109A (en) 1985-09-06

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