JPH09302594A - Production of vulcanized fiber - Google Patents

Production of vulcanized fiber

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Publication number
JPH09302594A
JPH09302594A JP13775996A JP13775996A JPH09302594A JP H09302594 A JPH09302594 A JP H09302594A JP 13775996 A JP13775996 A JP 13775996A JP 13775996 A JP13775996 A JP 13775996A JP H09302594 A JPH09302594 A JP H09302594A
Authority
JP
Japan
Prior art keywords
zinc chloride
base paper
vulcanized fiber
dezincification
vibrating
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
JP13775996A
Other languages
Japanese (ja)
Other versions
JP3496107B2 (en
Inventor
Yukio Hoshino
野 幸 雄 星
Yoshihiro Saito
藤 芳 廣 斎
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.)
Hokuetsu Paper Mills Ltd
Original Assignee
Hokuetsu Paper Mills 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 Hokuetsu Paper Mills Ltd filed Critical Hokuetsu Paper Mills Ltd
Priority to JP13775996A priority Critical patent/JP3496107B2/en
Publication of JPH09302594A publication Critical patent/JPH09302594A/en
Application granted granted Critical
Publication of JP3496107B2 publication Critical patent/JP3496107B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To improve the efficiency of zinc chloride removing process with virtually no influence on the diffusion of the zinc chloride in vulcanized fibers even if washing water is agitated because the above diffusion represents a rate-determining step during the zinc chloride removing process. SOLUTION: The vulcanized fibers are obtained by applying the following processes successively: one or more sheets of base paper is immersed in a concentrated aqueous solution of zinc chloride to swell, dissolve and gelatinize the surface of the base paper; when two or more sheets of base paper are to be used, these sheets are mutually laminated; the base paper is subjected to zinc chloride removing process by using a washing liquid; and the resultant sheet(s) of base paper is dried and finished. In this case, a part or the whole of treatment process for the zinc chloride removal using the washing liquid is carried out as follows: an apparatus provided with vibratory blades fixed irrotatably in a single tier or tiers on the axially vibratory shaft is put into the washing liquid in a zinc chloride removal tank and vibrations are applied to the blades with the number of vibrations of 10-60Hz and amplitude of 2-30mm.

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、バルカナイズドフ
ァイバーの製造方法に関し、更に詳しくは従来法に比
べ、洗浄液による脱塩化亜鉛工程の効率を高めることの
できるバルカナイズドファイバーの製造方法に関するも
のである。バルカナイズドファイバーは機械的強度に優
れた天然繊維質材料であり、打抜き、折り曲げ、プレス
成形等の加工性があり、耐衝撃性、耐摩耗性、耐油性、
電気絶縁性等に優れた材料である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing vulcanized fiber, and more particularly to a method for producing vulcanized fiber which can enhance the efficiency of the dezincification process using a cleaning solution as compared with the conventional method. Vulcanized fiber is a natural fiber material with excellent mechanical strength and has workability such as punching, bending, press molding, impact resistance, abrasion resistance, oil resistance,
It is a material with excellent electrical insulation.

【0002】[0002]

【従来の技術】バルカナイズドファイバーの製造工程は
原紙を塩化亜鉛の濃厚水溶液中に浸漬し、その原紙表面
を膨潤、溶解、膠化する工程、その後塩化亜鉛を洗浄液
で除去し溶解反応を停止させる脱塩化亜鉛工程を経て乾
燥、仕上げする工程とからなっている。なお、バルカナ
イズドファイバーの工業製品は厚手のものが多いため
と、バルカナイズ化を完全に行うために、通常、薄手の
原紙を膨潤、溶解、膠化して原紙の複数枚を積層した
後、脱塩化亜鉛し、次いで乾燥、仕上げしているが、1
枚の原紙からなるバルカナイズドファイバーには当然、
積層工程は不要である。
2. Description of the Related Art In the process of manufacturing vulcanized fiber, a process of immersing a base paper in a concentrated aqueous solution of zinc chloride to swell, dissolve and gelatinize the surface of the base paper, and then to remove zinc chloride with a washing liquid to stop the dissolution reaction The process consists of a zinc chloride process followed by a drying and finishing process. In addition, since many vulcanized fiber industrial products are thick, and in order to completely make vulcanized fiber, thin base paper is usually swelled, melted, and glued to form multiple layers of base paper, followed by dezincification chloride. Then dry and finish, but 1
Naturally, the vulcanized fiber made of one sheet of base paper,
No laminating step is required.

【0003】[0003]

【発明が解決しようとする課題】バルカナイズドファイ
バーの脱塩化亜鉛工程において、バルカナイズドファイ
バーを直接水に浸漬するとバルカナイズドファイバー内
の塩化亜鉛濃度と水との濃度差が大きいために過大な浸
透圧がバルカナイズドファイバー積層内部に発生し、積
層面のはく離現象を生じて製品価値を失う。従って、実
際の製造工程ではこのような現象を防ぐために、最初は
積層面のはく離現象を生じない範囲で比較的濃度の低い
塩化亜鉛水溶液に浸漬させ、段階的により濃度の低い塩
化亜鉛水溶液に浸漬させ、最後に水に浸漬させてバルカ
ナイズドファイバー中の塩化亜鉛含有量を所定量以下に
減少せしめるといった工程をとる。この一連の工程を脱
塩化亜鉛工程という。
In the process of dezincification of vulcanized fiber, if the vulcanized fiber is directly immersed in water, an excessive osmotic pressure causes an excessive osmotic pressure due to a large difference in concentration between zinc chloride in the vulcanized fiber and water. It occurs inside the laminate and causes a peeling phenomenon on the laminate surface, resulting in loss of product value. Therefore, in order to prevent such a phenomenon in the actual manufacturing process, first dip it in a relatively low concentration zinc chloride aqueous solution within a range that does not cause delamination of the laminated surface, and then gradually dip it in a lower concentration zinc chloride aqueous solution. Then, a step of finally immersing in water to reduce the zinc chloride content in the vulcanized fiber to a predetermined amount or less is taken. This series of steps is called a dezincification step.

【0004】このバルカナイズドファイバーの製造工程
には、連続方式とバッチ方式とがあり、連続方式では原
紙の塩化亜鉛濃厚水溶液への浸漬から脱塩化亜鉛、乾燥
までを連続して行っている。バッチ方式では原紙を塩化
亜鉛に浸漬させドラムに巻き所定の厚さになったところ
で切断し、脱塩化亜鉛、乾燥をロット毎に行っている。
通常、連続方式によることが多いが、厚さが著しく厚い
場合にはバッチ方式によることもある。
The vulcanized fiber manufacturing process includes a continuous system and a batch system. In the continuous system, the process of immersing the base paper in a concentrated aqueous solution of zinc chloride, dezincification and drying is continuously performed. In the batch method, the base paper is dipped in zinc chloride, wound around a drum, cut to a predetermined thickness, cut, and dezincified and dried for each lot.
Usually, the continuous method is often used, but when the thickness is extremely large, the batch method may be used.

【0005】バルカナイズドファイバーの製造工程の中
で脱塩化亜鉛工程が最も所要時間が長くかかる工程であ
り、厚さが厚くなると一段と長時間を要する。バルカナ
イズドファイバーの脱塩化亜鉛は多孔質繊維材料中にお
ける固体内拡散支配であり、脱塩化亜鉛槽内の洗浄液の
温度を高くすることによりある程度バルカナイズドファ
イバー内の塩化亜鉛の拡散を促進させることは可能であ
るが、脱塩化亜鉛工程はきわめて多量の洗浄液を使用す
るため、かかる多量の洗浄液の温度を高くするには莫大
なエネルギーコストがかかるとともに、脱塩化亜鉛初期
のいまだバルカナイズドファイバー中に塩化亜鉛がかな
り残存している領域では温度上昇によりバルカナイズド
ファイバーを構成するセルロ−スの溶解反応がさらに進
行してしまう結果、製品品質に悪影響を与えることとな
り好ましくない。
The dezincification step takes the longest time in the manufacturing process of vulcanized fiber, and the thicker it takes, the longer it takes. Dezincification of vulcanized fiber is dominated by solid diffusion in the porous fiber material, and it is possible to promote the diffusion of zinc chloride in the vulcanized fiber to some extent by increasing the temperature of the cleaning solution in the dezincification tank. However, since the zinc dechlorination process uses an extremely large amount of cleaning liquid, raising the temperature of such a large amount of cleaning liquid requires enormous energy costs, and zinc chloride is still present in the vulcanized fiber in the early stages of dechlorinating zinc. In the remaining region, the dissolution reaction of the cellulose constituting the vulcanized fiber further progresses due to the temperature increase, which adversely affects the product quality, which is not preferable.

【0006】また、脱塩化亜鉛槽内の洗浄水を通常の回
転羽根式撹拌機で攪拌することも考えられるが、脱塩化
亜鉛においてバルカナイズドファイバー内の塩化亜鉛の
拡散が律速段階となっているため、洗浄水を攪拌しても
バルカナイズドファイバー内の塩化亜鉛の拡散にはほと
んど影響せず脱塩化亜鉛の効率を向上せしめる効果はほ
どんどない。従って、本発明の目的は従来のバルカナイ
ズドファイバー製造工程における上記課題を解決し、脱
塩化亜鉛工程の効率を向上せしめることである。
It is also conceivable to stir the washing water in the dezincification tank with an ordinary rotary vane type agitator, but since diffusion of zinc chloride in the vulcanized fiber is the rate-determining step in dechlorination zinc. Even if the washing water is stirred, it hardly affects the diffusion of zinc chloride in the vulcanized fiber and has little effect of improving the efficiency of dezincification. Therefore, an object of the present invention is to solve the above problems in the conventional vulcanized fiber manufacturing process and improve the efficiency of the dezincification process.

【0007】[0007]

【課題を解決するための手段】本発明のバルカナイズド
ファイバーの製造方法は、1枚または2枚以上の原紙を
塩化亜鉛の濃厚水溶液中に浸漬し、その原紙表面を膨
潤、溶解、膠化する工程と、2枚以上の原紙を用いる場
合はそれらの原紙を積層する工程と、洗浄液による原紙
の脱塩化亜鉛工程と、原紙の乾燥、仕上工程を順次適用
してバルカナイズドファイバーを製造する方法におい
て、洗浄液による原紙の脱塩化亜鉛の全部または一部の
処理工程は、軸方向に振動する振動軸に一段または多段
に振動羽根板を回転不能に固定してなる装置を脱塩化亜
鉛槽内の洗浄液中に投入し、前記振動羽根板に振動数1
0〜60HZ、振動幅2〜30mmの振動を与えながら行
うようにしたものである。
The method for producing vulcanized fibers according to the present invention comprises a step of immersing one or more base papers in a concentrated aqueous solution of zinc chloride, and swelling, dissolving, and gelatinizing the surface of the base papers. In the method for producing vulcanized fiber by sequentially applying a step of laminating two or more base papers, a step of dechlorinating the base paper with a cleaning solution, a drying and finishing step of the base paper when two or more base papers are used, All or part of the dezincification treatment of the base paper by means of a device in which the vibrating blade plate is fixed to the vibrating shaft that vibrates in the axial direction in one or more stages so that it does not rotate in the washing liquid in the dechlorination zinc tank. Then, put it into the vibrating vane and make it 1
It is performed while giving a vibration of 0 to 60 HZ and a vibration width of 2 to 30 mm.

【0008】本発明で、脱塩化亜鉛槽内の洗浄液中に投
入する装置は、軸方向に振動する振動軸に一段または多
段に振動羽根板を回転不能に固定したもので、振動数は
10〜60Hz、好ましくは20〜40Hzの振動を発
生する振動モーターなどにより行う。振動数が10Hz
未満あるいは60Hzを超えた場合は脱塩化亜鉛促進効
果が不十分となる。また、振動板の振動幅は2〜30m
m好ましくは10〜15mmである。振動幅が2mm未
満では脱塩化亜鉛効果が不十分となり、30mmを超え
る場合は、脱塩化亜鉛槽内の洗浄液の動揺が激しくな
り、該洗浄液中のバルカナイズドファイバーが係る洗浄
液の動揺の影響を受け、しわあるいは破断等を生じやす
くなり不適である。
In the present invention, the apparatus for introducing the cleaning liquid in the dechlorination zinc tank is one in which the vibrating vane plates are non-rotatably fixed to the vibrating shaft vibrating in the axial direction in one stage or in multiple stages, and the vibration frequency is 10 to 10. It is performed by a vibration motor or the like that generates a vibration of 60 Hz, preferably 20 to 40 Hz. Frequency is 10Hz
If it is less than 60 Hz or more than 60 Hz, the effect of promoting dechlorination zinc becomes insufficient. The vibration width of the diaphragm is 2 to 30 m.
m is preferably 10 to 15 mm. If the vibration width is less than 2 mm, the dezincification effect is insufficient, and if it exceeds 30 mm, the shaking of the cleaning liquid in the dechlorination zinc tank becomes violent, and the vulcanized fiber in the cleaning liquid is affected by the shaking of the cleaning liquid. Wrinkles or fractures are likely to occur, which is not suitable.

【0009】本発明のバルカナイズドファイバーの製造
方法によりバルカナイズドファイバーを製造するには、
木綿パルプ及び木材パルプなどの精製天然セルロース繊
維パルプあるいは最終製品の使用目的に応じて炭素繊
維、ガラス繊維等の無機繊維や各種合成繊維を混合して
なる原紙を用いて、従来慣用の方法で係る原紙を塩化亜
鉛の濃厚水溶液中に浸漬し、その原紙表面を膨潤、溶
解、膠化せしめ、その後2枚以上の原紙を用いる場合
は、これらの原紙を積層する。次に、脱塩化亜鉛槽内の
洗浄液中に予め、軸方向に振動する振動軸に一段または
多段に振動羽根板を回転不能に固定した装置を投入し、
該振動羽根板に振動数10〜60Hz、振動幅2〜30
mmの振動を与えながら脱塩化亜鉛槽内に浸潰したバル
カナイズドファイバーの脱塩化亜鉛処理を行う。最後に
従来慣用の方法で乾燥、仕上げして製品とする。なお、
本発明のバルカナイズドファイバーの製造方法は、連続
方式とバッチ方式のいずれにも適用できる。また、本発
明のバルカナイズドファイバーの製造方法において、軸
方向に振動する振動軸に一段または多段に振動羽根板を
回転不能に固定してなる装置を用いる脱塩化亜鉛法を脱
塩化亜鉛工程の全部に適用してもよいし、その一部に適
用してもよい。
To produce vulcanized fiber by the method for producing vulcanized fiber of the present invention,
Purified natural cellulose fiber pulp such as cotton pulp and wood pulp, or a conventional paper using a base paper made by mixing inorganic fibers such as carbon fiber and glass fiber and various synthetic fibers depending on the intended use of the final product. The base paper is dipped in a concentrated aqueous solution of zinc chloride to swell, dissolve, and gelatinize the surface of the base paper, and when two or more base papers are used, these base papers are laminated. Next, in the cleaning liquid in the dechlorination zinc tank, in advance, put a device in which the vibrating blade plate is fixed in a non-rotatable manner in one or more stages on the vibrating shaft that vibrates in the axial direction,
The vibrating blade plate has a frequency of 10 to 60 Hz and a vibration width of 2 to 30 Hz.
The vulcanized fiber that has been immersed in the dezincification tank is subjected to dezincification treatment while giving a vibration of mm. Finally, the product is dried and finished by a conventional method. In addition,
The method for producing vulcanized fiber of the present invention can be applied to both the continuous method and the batch method. Further, in the method for producing a vulcanized fiber according to the present invention, the dezincification method using a device in which the vibrating vane is fixed to the vibrating shaft vibrating in the axial direction in a one-stage or multi-stage manner so as to be non-rotatable is used for all dezincification steps. It may be applied or may be applied to a part thereof.

【0010】[0010]

【作用】本発明の作用、機構については必ずしも明確で
はないが次のように推定される。前述したように、バル
カナイズドファイバーの脱塩化亜鉛は、多孔質繊維材料
中における固体内拡散支配であり、通常の回転式撹拌機
などによって脱塩化亜鉛槽内の洗浄液を攪拌してもバル
カナイズドファイバー内の塩化亜鉛の拡散にはあまり影
響せず、結果的にほとんど脱塩化亜鉛の促進効果は得ら
れない。これに対して、本発明では脱塩化亜鉛槽内の洗
浄液に、軸方向に振動する振動軸に一段または多段に振
動羽根板を回転不能に固定してなる装置を投入し、係る
振動羽根板に振動数10〜60Hz、振動幅2〜30m
mの振動を与えることとしたので、振動羽根板の振動が
脱塩化亜鉛槽内の洗浄液に伝わり、次いで洗浄液内に浸
漬されたバルカナイズドファイバーに伝達され、バルカ
ナイズドファイバーそのものが振動するとともに多孔質
繊維材料たるバルカナイズドファイバー内の繊維間空隙
に充満している塩化亜鉛水溶液にもこの振動が伝達され
繊維間空隙内において塩化水溶液が微細流動することと
なる結果、バルカナイズドファイバー内での塩化亜鉛の
拡散が加速され、脱塩化亜鉛が顕著に促進されるという
特異な効果を発現するものと考えられる。
The function and mechanism of the present invention are not necessarily clear, but they are presumed as follows. As mentioned above, dezincification of vulcanized fiber is dominated by solid diffusion in the porous fiber material, and even if the cleaning liquid in the dezincification tank is stirred by a normal rotary stirrer, It has little effect on the diffusion of zinc chloride, and as a result, almost no promoting effect of dezincification is obtained. On the other hand, in the present invention, the cleaning liquid in the dezincification tank is provided with a device in which the vibrating blade plate is fixed to the vibrating shaft that vibrates in the axial direction in one or more stages so that the vibrating blade plate is not rotated. Vibration frequency 10-60Hz, vibration width 2-30m
The vibration of the vibrating blade plate is transmitted to the cleaning liquid in the dechlorination zinc tank and then to the vulcanized fiber immersed in the cleaning liquid, and the vulcanized fiber itself vibrates and the porous fiber material is used. This vibration is also transmitted to the zinc chloride aqueous solution that fills the inter-fiber voids in the barrel vulcanized fiber, causing the chloride aqueous solution to finely flow in the inter-fiber voids, resulting in accelerated diffusion of zinc chloride in the vulcanized fibers. It is considered that the specific effect that dezincification is significantly promoted is exhibited.

【0011】[0011]

【実施例】次に本発明を実施例に基づき説明する。なお
実施例中の試験片の厚さ及び塩素含有量の測定はJIS
C2315に規定する方法によった。
EXAMPLES The present invention will now be described based on examples. The thickness and chlorine content of the test pieces in the examples are measured according to JIS
According to the method specified in C2315.

【0012】実施例1 精製天然セルロースパルプよりなる原紙を常法に従って
塩化亜鉛の濃厚水溶液(液濃度70度ボーメ、液温35
℃)に浸漬し、その原紙表面を膨潤、溶解、膠化せしめ
た後積層し、次いで常法により脱塩化亜鉛処理を行い、
該脱塩化亜鉛処理の途中のまだバルカナイズドファイバ
ー中にかなり塩化亜鉛を含有している段階で30cm×
30cmの試験片を4枚切り取った。次に、実験用脱塩
化亜鉛槽(容量200リットル)内に洗浄液として水を
満たし、この洗浄液中に、軸方向に振動する振動軸に6
段の振動羽根板を回転不能に固定してなる装置(商品名
超振動撹拌機α−1型:日本テクノ社製)を投入し、係
る装置の振動羽根板に振動数25Hz、振動幅15mm
の振動を与えながら前記試験片の内の3枚を投入し1時
間後、2時間後及び4時間後にそれぞれ1枚ずつ引き上
げた。次いで、実験用脱塩化亜鉛槽に浸漬しなかった試
験片を含め計4枚の試験片を常法により乾燥したところ
4枚の試験片のいずれも厚さ約1.6mmのバルカナイ
ズドファイバーとなった。この4枚の試験片について塩
素含有量を測定し、得られた結果を第1表に示した。
Example 1 A base paper made of purified natural cellulose pulp was prepared according to a conventional method in a concentrated aqueous solution of zinc chloride (liquid concentration 70 ° Baume, liquid temperature 35).
℃), swelling, dissolving, and gelatinizing the surface of the base paper, and then laminating, and then dezincing zinc treatment by a conventional method,
30 cm × at the stage where the vulcanized fiber still contains a considerable amount of zinc chloride during the dezincification treatment.
Four 30 cm test pieces were cut out. Next, water was filled as a cleaning liquid in an experimental dechlorination zinc bath (volume: 200 liters), and the cleaning shaft was vibrated in the axial direction by 6
A device (product name: super-vibration stirrer α-1 type: manufactured by Nippon Techno Co., Ltd.) in which the stepped vibrating blade plate is fixed in a non-rotatable manner is introduced, and the vibrating blade plate of the device has a vibration frequency of 25 Hz and a vibration width of 15 mm.
Three of the test pieces were put in while applying the vibration of 1. and after 1 hour, 2 hours, and 4 hours, one piece was pulled up. Next, when a total of 4 test pieces including the test piece that was not immersed in the experimental dechlorination tank were dried by a conventional method, all of the 4 test pieces became vulcanized fiber having a thickness of about 1.6 mm. . The chlorine content of the four test pieces was measured, and the obtained results are shown in Table 1.

【0013】[0013]

【表1】 [Table 1]

【0014】実施例2 実施例1において、原紙の積層数を変え、振動羽根板の
振動数を35Hz、振動幅を10mmとし、実験用脱塩
化亜鉛槽での処理時間を変えた以外は実施例1と同様に
して得た試験片バルカナイズドファイバー(厚さ約1.
0mm)の塩素含有量を測定し、得られた結果を第2表
に示した。
Example 2 Example 2 is different from Example 1 except that the number of laminated base papers was changed, the vibration frequency of the vibrating blade plate was 35 Hz, the vibration width was 10 mm, and the treatment time in the experimental dechlorination zinc tank was changed. Specimen vulcanized fiber (thickness: about 1.
The chlorine content of 0 mm) was measured, and the obtained results are shown in Table 2.

【0015】[0015]

【表2】 [Table 2]

【0016】比較例1 実施例1において、実験用脱塩化亜鉛槽内での脱塩化亜
鉛処理において、軸方向に振動する振動軸に6段の振動
羽根板を回転不能に固定してなる装置を使用しない以外
は、実施例1と同様にして得た試験片バルカナイズドフ
ァイバー(厚さ約1.6mm)の塩素含有量を測定し、
得られた結果を第1表に併せて示した。
Comparative Example 1 In Example 1, in the dezincification treatment in the experimental dezincification tank, an apparatus in which 6 stages of vibrating blade plates were non-rotatably fixed to a vibrating shaft vibrating in the axial direction was used. The chlorine content of the test piece vulcanized fiber (thickness: about 1.6 mm) obtained in the same manner as in Example 1 except that it was not used was measured,
The obtained results are also shown in Table 1.

【0017】比較例2 実施例2において、実験用脱塩化亜鉛槽内での脱塩化亜
鉛処理において、軸方向に振動する振動軸に6段の振動
羽根板を回転不能に固定してなる装置を使用しない以外
は、実施例2と同様にして得た試験片バルカナイズドフ
ァイバー(厚さ約1.0mm)の塩素含有量を測定し、
得られた結果を第2表に併せて示した。
COMPARATIVE EXAMPLE 2 In Example 2, in the dezincification treatment in the experimental dezincification tank, an apparatus in which 6 stages of vibrating blade plates were non-rotatably fixed to the vibrating shaft vibrating in the axial direction was used. The chlorine content of the test piece vulcanized fiber (thickness: about 1.0 mm) obtained in the same manner as in Example 2 was measured except that it was not used.
The results obtained are shown in Table 2.

【0018】比較例3 実施例1において、実験用脱塩化亜鉛槽内での脱塩化亜
鉛処理において、軸方向に振動する振動軸に6段の振動
羽根板を回転不能に固定してなる装置に代えて通常の回
転羽根式撹拌機を用いて実験用脱塩化亜鉛槽内の洗浄液
を攪拌した以外は実施例1と同様にして得た試験片バル
カナイズドファイバー(厚さ約1.6mm)の塩素含有
量を測定し、得られた結果を第1表に併せて示した。
COMPARATIVE EXAMPLE 3 In Example 1, in the dezincification treatment in the experimental dezincification tank, a device in which 6 stages of vibrating vanes were non-rotatably fixed to the vibrating shaft vibrating in the axial direction was used. Instead, the chlorine content of the test piece vulcanized fiber (thickness: about 1.6 mm) obtained in the same manner as in Example 1 except that the cleaning liquid in the experimental dechlorination zinc tank was stirred using an ordinary rotary blade type stirrer The amount was measured, and the obtained results are also shown in Table 1.

【0019】比較例4 実施例2において、実験用脱塩化亜鉛槽内での脱塩化亜
鉛処理において、軸方向に振動する振動軸に6段の振動
羽根板を回転不能に固定してなる装置に代えて通常の回
転羽根式撹拌機を用いて実験用脱塩化亜鉛槽内の洗浄液
を攪拌した以外は実施例2と同様にして得た試験片バル
カナイズドファイバー(厚さ約1.0mm)の塩素含有
量を測定し、得られた結果を第2表に併せて示した。な
お、実施例1、2、及び比較例1、2、3、4、いずれ
においても脱塩化亜鉛処理によるバルカナイズドファイ
バー積層面のはく離現象は生じなかった。
COMPARATIVE EXAMPLE 4 In Example 2, in the dezincification treatment in the experimental dezincification tank, a device in which six vibrating vanes were non-rotatably fixed to the vibrating shaft vibrating in the axial direction was used. Instead, the chlorine content of the test piece vulcanized fiber (thickness: about 1.0 mm) obtained in the same manner as in Example 2 except that the cleaning liquid in the experimental dechlorination zinc tank was stirred using an ordinary rotary vane type stirrer The amount was measured, and the obtained results are also shown in Table 2. In all of Examples 1 and 2 and Comparative Examples 1, 2, 3, and 4, delamination of the vulcanized fiber laminated surface due to the dechlorination treatment did not occur.

【0020】[0020]

【発明の効果】実施例1、2、比較例1、2、3、4、
第1表及び第2表からわかるように、脱塩化亜鉛を、軸
方向に振動する振動軸に一段または多段に振動羽根板を
回転不能に固定してなる装置を脱塩化亜鉛槽内の洗浄液
中に投入し、係る装置の振動羽根板に本発明で特定する
振動数及び振動幅の振動を与えながら行うことにより、
脱塩化亜鉛が大きく促進され、同一条件比較で、係る装
置を用いなかった場合あるいは通常の回転式撹拌機で洗
浄液を撹拌した場合に比べ、バルカナイズドファイバー
中の塩素含有量すなわち塩化亜鉛含有量を、積層面での
はく離現象を生じることなく、約1/1.5〜1/15
程度に飛躍的に減少せしめることができた。本発明に係
る脱塩化亜鉛方法を適用することにより今まで著しく長
時間を要していた脱塩化亜鉛処理の所要時間が大幅に短
縮され、バルカナイズドファイバーの生産性向上効果を
享受できる。
EFFECTS OF THE INVENTION Examples 1, 2 and Comparative Examples 1, 2, 3, 4,
As can be seen from Tables 1 and 2, a device in which dechlorinated zinc is fixed to a vibrating shaft that vibrates in the axial direction in one or more stages with non-rotatable vibrating vanes is used in the cleaning liquid in the dechlorinated zinc tank. By applying to the vibrating blade plate of such a device while vibrating at the frequency and the vibration width specified in the present invention,
Dezincification is greatly promoted, and in the same condition comparison, the chlorine content in the vulcanized fiber, that is, the zinc chloride content, compared to the case where such a device was not used or the cleaning solution was stirred with a normal rotary stirrer, About 1 / 1.5 to 1/15 without peeling phenomenon on the laminated surface
I was able to reduce it dramatically. By applying the dezincification method according to the present invention, the time required for the dezincification treatment, which has required a remarkably long time until now, is significantly shortened, and the effect of improving the productivity of vulcanized fiber can be enjoyed.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 1枚または2枚以上の原紙を塩化亜鉛の
濃厚水溶液中に浸漬し、その原紙表面を膨潤、溶解、膠
化する工程と、2枚以上の原紙を用いる場合はそれらの
原紙を積層する工程と、洗浄液による原紙の脱塩化亜鉛
工程と、原紙の乾燥、仕上工程を順次適用してバルカナ
イズドファイバーを製造する方法において、洗浄液によ
る原紙の脱塩化亜鉛の全部または一部の処理工程は、軸
方向に振動する振動軸に一段または多段に振動羽根板を
回転不能に固定してなる装置を脱塩化亜鉛槽内の洗浄液
中に投入し、前記振動羽根板に振動数10〜60HZ、
振動幅2〜30mmの振動を与えながら行うことを特徴と
するバルカナイズドファイバーの製造方法。
1. A step of immersing one or more base papers in a concentrated aqueous solution of zinc chloride to swell, dissolve, and gelatinize the surface of the base papers, and when two or more base papers are used, those base papers. In the method for producing vulcanized fiber by sequentially applying the step of stacking, the step of dezincing the base paper with a cleaning solution, the step of drying the base paper, and the finishing step, a step for treating all or part of the dezincification of the base paper with the cleaning solution. Is a system in which a vibrating vane plate is fixed to a vibrating shaft vibrating in the axial direction in a non-rotatable manner in a single stage or in multiple stages, and the device is put into a cleaning solution in a dechlorination zinc tank.
A method for producing a vulcanized fiber, which is characterized in that it is performed while applying a vibration having a vibration width of 2 to 30 mm.
JP13775996A 1996-05-09 1996-05-09 Manufacturing method of vulcanized fiber Expired - Lifetime JP3496107B2 (en)

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JP13775996A JP3496107B2 (en) 1996-05-09 1996-05-09 Manufacturing method of vulcanized fiber

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JP3496107B2 JP3496107B2 (en) 2004-02-09

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010089013A (en) * 2008-10-08 2010-04-22 Nagaoka Univ Of Technology Fiber sheet having liquid-liquid separation function
CN103147356A (en) * 2013-03-07 2013-06-12 杭州特种纸业有限公司 Abrasive steel paperboard and manufacturing process thereof
CN103321101A (en) * 2013-05-27 2013-09-25 朱佳慧 Formula and preparation method of vulcanized fiber paper
JP2015089986A (en) * 2013-11-07 2015-05-11 北越紀州製紙株式会社 Method of producing vulcanized fiber
CN105002781A (en) * 2015-05-30 2015-10-28 玛纳斯源源纸业有限公司 Production method avoiding vulcanized fiber paper from turning white
CN106012673A (en) * 2016-05-24 2016-10-12 玛纳斯源源纸业有限公司 Gelling process in vulcanized paper production

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010089013A (en) * 2008-10-08 2010-04-22 Nagaoka Univ Of Technology Fiber sheet having liquid-liquid separation function
CN103147356A (en) * 2013-03-07 2013-06-12 杭州特种纸业有限公司 Abrasive steel paperboard and manufacturing process thereof
CN103321101A (en) * 2013-05-27 2013-09-25 朱佳慧 Formula and preparation method of vulcanized fiber paper
JP2015089986A (en) * 2013-11-07 2015-05-11 北越紀州製紙株式会社 Method of producing vulcanized fiber
CN105002781A (en) * 2015-05-30 2015-10-28 玛纳斯源源纸业有限公司 Production method avoiding vulcanized fiber paper from turning white
CN106012673A (en) * 2016-05-24 2016-10-12 玛纳斯源源纸业有限公司 Gelling process in vulcanized paper production

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