JP2000248486A - Papermaking of paper mixed with fine bubble - Google Patents

Papermaking of paper mixed with fine bubble

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Publication number
JP2000248486A
JP2000248486A JP11055329A JP5532999A JP2000248486A JP 2000248486 A JP2000248486 A JP 2000248486A JP 11055329 A JP11055329 A JP 11055329A JP 5532999 A JP5532999 A JP 5532999A JP 2000248486 A JP2000248486 A JP 2000248486A
Authority
JP
Japan
Prior art keywords
papermaking
pulp
white water
water
pulp suspension
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.)
Pending
Application number
JP11055329A
Other languages
Japanese (ja)
Inventor
Takahiko Furuya
隆彦 古谷
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP11055329A priority Critical patent/JP2000248486A/en
Publication of JP2000248486A publication Critical patent/JP2000248486A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To solve the problems of the use of a chemical mucilaginous agent, such as expensiveness of a cost for procurement of the chemical mucilaginous agent, and requirement of operation time, power cost, an installing space for equipment, when carrying out the papermaking by mixing the chemical mucilaginous agent with a pulp suspension. SOLUTION: A finely bubbled water including fine bubbles not floating-up in the water is joined to a pulp suspension to stick the fine bubbles in the finely bubbled water to the pulp in the pulp suspension, and the pulp suspension containing the pulp with the bubbles is supplied to a papermaking cylinder 11.

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】この発明は、パルプ懸濁液中
のパルプの分散、沈降を防ぐ化学粘剤の使用を廃し、又
は使用量を減少して抄紙する抄紙方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a papermaking method in which the use of a chemical thickener for preventing the dispersion and sedimentation of pulp in a pulp suspension is eliminated or the amount of use is reduced to reduce the amount of use.

【0002】[0002]

【従来の技術】従来は、パルプ懸濁液に、パルプの分
散、沈降を防止する例えばポリエチレンオキサイドなど
の化学粘剤の希釈水を混合したパルプ濃度0.2%程度
の製紙原液を抄紙シリンダーに供給し、抄紙を行ってい
た。
2. Description of the Related Art Conventionally, a stock solution of pulp having a pulp concentration of about 0.2% is prepared by mixing a pulp suspension with a dilution water of a chemical thickener such as polyethylene oxide for preventing dispersion and sedimentation of pulp. Supply and paper making.

【0003】[0003]

【発明が解決しようとする課題】上記従来の方法では、
化学粘剤の入手にコストが嵩むと共に、入手した化学粘
剤を希釈するための溶解に要する作業時間、動力費、設
備の設置スペース等が必要になる。更に、化学粘剤は粘
性、発泡性があるため水垢、スライムが発生し、抄紙シ
リンダー、毛布を汚すと共に、抄紙した紙のトラブルで
ある紙切れの原因になっている。又、水に溶解する際
に、飛散し易く、周囲に付着して作業環境を滑り易くす
る危険がある。
In the above conventional method,
In addition to increasing the cost for obtaining the chemical thickener, the time required for dissolution for diluting the obtained chemical thickener, power cost, installation space for equipment, and the like are required. In addition, since the chemical adhesive has viscosity and foaming property, scale and slime are generated, staining the papermaking cylinder and blanket, and causing paper breakage which is a trouble of the paper made. In addition, when dissolved in water, it is liable to be scattered, adhered to the surroundings, and made the working environment slippery.

【0004】[0004]

【課題を解決するための手段】本発明は上述の問題点を
解消するため、化学粘剤を使用せず、又は使用量を減少
して抄紙するようにしたのであって、水中で浮上しない
微細な気泡を含んだ微細気泡水をパルプ懸濁液と混合
し、微細気泡水の微細気泡をパルプ懸濁液中のパルプに
付着させて抄紙シリンダーに供給することを特徴とす
る。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention does not use a chemical adhesive or reduces the amount of paper used to make paper. The method is characterized in that fine bubble water containing fine bubbles is mixed with a pulp suspension, and fine bubbles of the fine bubble water adhere to pulp in the pulp suspension and are supplied to a papermaking cylinder.

【0005】[0005]

【発明の実施の形態】図示の各実施形態において、10
は矢印方向に回転駆動されて抄紙を行う丸網式の抄紙シ
リンダー11と、該抄紙シリンダーにパルプ懸濁液と白
水とが混合したパルプ濃度0.2%程度の製紙原液を供
給する製紙原液供給装置12とからなる抄紙装置であ
り、抄紙装置10の下方には該装置が抄紙シリンダーに
供給した製紙原液のうち、抄紙シリンダーを透過して流
れ落ちる液を受入れるための白水ピット13が設けてあ
る。尚、白水ピット13にはオーバーフローした白水を
受入れる溢流ピット14が設けてあり、溢流ピットに流
入した白水はポンプP2 で晒パルプの洗浄工程に洗浄水
として供給される。
BRIEF DESCRIPTION OF THE DRAWINGS FIG.
Is a circular net-type papermaking cylinder 11 which is driven to rotate in the direction of the arrow to make paper, and a papermaking stock solution supply for supplying a stock solution of pulp suspension and white water having a pulp concentration of about 0.2% to the papermaking cylinder. A papermaking apparatus including an apparatus 12, and a white water pit 13 is provided below the papermaking apparatus 10 for receiving a liquid flowing through the papermaking cylinder and flowing down from the papermaking stock solution supplied to the papermaking cylinder by the apparatus. Incidentally, the white water pit 13 Yes to overflow the pit 14 for receiving the white water that overflowed provided, white water that has flowed into the overflow pit is supplied as washing water to the washing step of bleached pulp pump P 2.

【0006】図1の実施形態の抄紙シリンダーへの製紙
原液供給装置12はほぼU字形のヘッドボックス15を
備え、このヘッドボックスは一端の上端部に、製紙原液
を抄紙シリンダーの斜め上向きの円周面11aに接触さ
せて流し掛けるバット16を備えている。バッド16の
上面は開放している。上記ヘッドボックス15の他端部
の内部は、上面が開放し、高さが低い仕切壁17により
下端が閉じた混合溢流部18と、下端が前記バット16
に下から連なった連通部19に区劃されている。そし
て、ヘッドボックスの上記混合溢流部18にはパルプ濃
度0.5%±0.1%程度のパルプ懸濁液の給液管20
と、白水ピット13からの白水給水管21とが上から突
入している。
The apparatus 12 for supplying a stock solution to a papermaking cylinder in the embodiment of FIG. 1 includes a substantially U-shaped head box 15, which is provided at the upper end of one end with a papermaking stock solution at an obliquely upward circumferential direction of the papermaking cylinder. A bat 16 is provided which is brought into contact with the surface 11a and is poured. The upper surface of the pad 16 is open. The inside of the other end of the head box 15 has a mixing overflowing part 18 whose upper surface is open and whose lower end is closed by a partition wall 17 having a low height,
It is divided into a communication section 19 connected from below. Then, a feed pipe 20 for a pulp suspension having a pulp concentration of about 0.5% ± 0.1% is provided in the mixing overflow section 18 of the head box.
And the white water supply pipe 21 from the white water pit 13 rush from above.

【0007】白水の給水管21には白水ピット中の白水
を吐出、圧送するポンプP1 、エアコンプレッサ22か
らの圧縮空気を送気する送気管23、公知の微細気泡製
造ミキサー24が接続し、ポンプP1 が白水ピットから
吸出して圧送する白水にはエアコンプレッサ22からの
加圧空気が混合し、微細気泡製造ミキサーは白水中の加
圧空気を水中でほゞ浮上することがない大きさの約10
ミクロン、好ましくは10ミクロンよりも小さく微細化
する。
A pump P 1 for discharging and supplying white water in a white water pit, an air supply pipe 23 for supplying compressed air from an air compressor 22, and a known fine bubble production mixer 24 are connected to the white water supply pipe 21. from the pump P 1 is white water pit pressurized air mixed from the air compressor 22 is in the white water pumping Te sucking, fine bubble production mixer of the lack sized to Ho Isuzu floating pressurized air in the white water in the water About 10
Micronization, preferably smaller than 10 microns.

【0008】これによって、ヘッドボックスの混合溢流
部18には上から突入した給液管20から下向きにパル
プ懸濁液が供給され、同時に白水給水管21からは10
ミクロン、又はそれよりも大きさが小さい微細気泡を含
む白水の微細気泡水が下向きに供給され、上記パルプ懸
濁液と混合しながら一旦下降したのち上昇することによ
り均一に混合してパルプ濃度0.2%程度の製紙原液に
なり、それから仕切壁17の上端を越えて連通部19に
溢流し、連通部19からバット16に流送されて抄紙シ
リンダー11に流れかゝってシリンダーの周面に湿紙の
地合を構成し、コーチロール9で剥離されてドライパー
トに搬送される。
As a result, the pulp suspension is supplied to the mixing overflow portion 18 of the head box downward from the liquid supply pipe 20 which has entered from above, and at the same time, 10% of the pulp suspension is supplied from the white water supply pipe 21.
Microbubble water containing microbubbles of a micron or smaller size is supplied downward, and once mixed with the pulp suspension, descends and then ascends to mix uniformly so that the pulp concentration is 0. .2% of the stock solution, and then overflows over the upper end of the partition wall 17 into the communication section 19, flows from the communication section 19 to the vat 16, flows into the papermaking cylinder 11, and flows into the cylinder surface. , Forming a wet paper formation, separated by the coach roll 9 and transported to the dry part.

【0009】図2の実施形態において、図1の構成要素
と同等の構成部分には同じ符号を付して説明を省略す
る。この図2の実施形態の抄紙シリンダー11への製紙
原液供給装置12のバット16は、抄紙シリンダーに向
くスリットを備えた密閉状のボックス形であり、抄紙シ
リンダー11の内部には上記バット16のスリットから
シリンダーの周面に向かって噴出する製紙原液の白水を
吸引する固定のサクションボックス11′が設けてあ
る。このサクションボックスに吸引された白水はシリン
ダーの中心部から白水ピット13に供給される。
In the embodiment of FIG. 2, the same components as those of FIG. 1 are denoted by the same reference numerals, and the description thereof will be omitted. The vat 16 of the papermaking stock solution supply device 12 to the papermaking cylinder 11 in the embodiment of FIG. 2 is a closed box having a slit facing the papermaking cylinder, and the slit of the vat 16 is provided inside the papermaking cylinder 11. There is provided a fixed suction box 11 'for sucking white water of the stock undiluted paper ejected from the cylinder toward the peripheral surface of the cylinder. The white water sucked into the suction box is supplied to the white water pit 13 from the center of the cylinder.

【0010】パルプ懸濁液をバット16に供給する給液
管20の途中には接続点25で白水ピット13からの白
水の給水管21が接続している。この白水の給水管21
にもポンプP1 、エアコンプレッサ22からの送気管2
3、微細気泡製造ミキサー24が接続してあるので、給
液管20によりバット16に向かって供給されるパルプ
濃度0.5%程度のパルプ懸濁液には、接続点25で1
0ミクロン、又はそれよりも大きさが小さい微細気泡を
含む白水の微細気泡水が給水管21から供給されて均一
に混合し、パルプ濃度0.2%程度の製紙原液となって
バット16に流送され、バットから抄紙シリンダー11
に噴出してシリンダーの周面に湿紙の地合を構成し、コ
ーチロール9で剥離されてドライパートに搬送される。
At the connection point 25, a white water supply pipe 21 from the white water pit 13 is connected at an intermediate point of the liquid supply pipe 20 for supplying the pulp suspension to the vat 16. This white water supply pipe 21
Also the pump P 1 , the air supply pipe 2 from the air compressor 22
3. Since the fine bubble production mixer 24 is connected, a pulp suspension having a pulp concentration of about 0.5% supplied toward the vat 16 by the liquid supply pipe 20 is connected at the connection point 25 by one.
Microbubble water of white water containing microbubbles of 0 micron or smaller is supplied from the water supply pipe 21 and uniformly mixed to form a stock solution having a pulp concentration of about 0.2% and flows into the vat 16. Sent from the vat to the papermaking cylinder 11
To form a wet paper web on the peripheral surface of the cylinder, separated by the coach roll 9 and conveyed to the dry part.

【0011】図1,図2のどちらの実施形態において
も、微細気泡製造ミキサー24の効率を高めるため、図
1に拡大して示したように、白水の給水管21に接続す
る送気管23の端部に多孔質の散気体26を取付けて給
水管21の内部に位置させ、エアコンプレッサ22の圧
力を例えば3kg/cm2 に高めることにより上記散気
体26から直径2mm±1mm程度の気泡を給水管21
中を流れる白水に混合することが好ましい。
In both of the embodiments shown in FIGS. 1 and 2, in order to increase the efficiency of the fine bubble production mixer 24, as shown in an enlarged view in FIG. A porous gas diffuser 26 is attached to the end and positioned inside the water supply pipe 21. By increasing the pressure of the air compressor 22 to, for example, 3 kg / cm 2 , bubbles having a diameter of about 2 mm ± 1 mm are supplied from the gas diffuser 26. Tube 21
It is preferable to mix with white water flowing through.

【0012】又、抄紙シリンダー11に供給される製紙
原液中に混合した微細気泡のエア量は、製紙原液の量
(抄紙水量)の10〜25%であるため、送気管23の
途中の逆止弁27の上流に接続した制御弁28でエアコ
ンプレッサ22からの圧縮空気の供給量を製紙原液の濾
水度(フリーネス)に応じて調節可能にすることが好ま
しい。
The amount of air of fine bubbles mixed in the stock solution supplied to the papermaking cylinder 11 is 10 to 25% of the amount of stock solution (papermaking water amount). It is preferable that the supply amount of compressed air from the air compressor 22 can be adjusted by a control valve 28 connected upstream of the valve 27 according to the freeness (freeness) of the stock solution.

【0013】更に、給液管20、給水管21の水平な個
所や、図2のバット16の上壁にはエア抜き29を設
け、複数の微細気泡が1つに合同して生じた粗大気泡を
排気し、抄造した湿紙の地合構成を悪化するのを防止す
る。
Further, air vents 29 are provided on horizontal portions of the liquid supply pipe 20 and the water supply pipe 21 and on the upper wall of the bat 16 in FIG. To prevent the formation of the wet paper web from being deteriorated.

【0014】更に、図1の実施形態のバット16の背面
や、ヘッドボックスの連通部19の開放部には溢流樋3
0を設け、合同した粗大気泡や、浮上した浮遊パルプを
オーバーフロー水で溢流樋30に排出し、湿紙の地合構
成の悪化を防止する。尚、溢流樋30,30に排出され
た液は白水ピット13の溢流ピット14に供給し、晒パ
ルプの洗浄水に使用する。又、ヘッドボックスの混合溢
流部18に供給されるパルプ懸濁液の供給圧力と、微細
気泡を混合した白水の供給圧力はほゞ同じであることが
好ましい。このため給液管20、給水管21の水面上に
夫々圧力計31を取付けて供給圧力を測定可能にし、こ
の圧力計31,31の値がほゞ同じになるようにパルプ
懸濁液と、微細気泡を混合した白水の供給量を調節でき
るようにすることが好ましい。
Further, the overflow gutter 3 is provided on the back surface of the bat 16 in the embodiment of FIG.
0 is provided to discharge the combined coarse bubbles and the floating pulp that has floated to the overflow gutter 30 with overflow water, thereby preventing the formation of wet paper from being deteriorated. The liquid discharged into the overflow gutters 30 and 30 is supplied to the overflow pit 14 of the white water pit 13 and used as washing water for bleached pulp. Further, it is preferable that the supply pressure of the pulp suspension supplied to the mixing overflow portion 18 of the head box and the supply pressure of the white water mixed with the fine bubbles are substantially the same. For this reason, a pressure gauge 31 is mounted on the water surface of the liquid supply pipe 20 and the water supply pipe 21 so that the supply pressure can be measured, and the pulp suspension and the pressure gauges 31 and 31 are made to have substantially the same value. It is preferable that the supply amount of white water mixed with fine bubbles can be adjusted.

【0015】又、図2の実施形態では微細気泡を混合し
た白水の給水管21は、図示の如く、パルプ懸濁液の給
液管20に対して接続点25で約45゜の角度αで合流
するように接続し、給液管20中を下流に向かって流れ
るパルプ懸濁液と、接続点25においてほゞ同じ圧力で
微細気泡を含む白水を合流、混合させることが好まし
い。31,31は両管20と21の合流点の近傍に設け
た圧力計を示す。
In the embodiment shown in FIG. 2, the water supply pipe 21 containing fine air bubbles is connected to the pulp suspension liquid supply pipe 20 at an angle α of about 45 ° at a connection point 25 as shown in FIG. It is preferable that the pulp suspension, which is connected so as to be merged, flows downstream in the liquid supply pipe 20, and the white water containing microbubbles at the connection point 25 at almost the same pressure, are mixed and mixed. Reference numerals 31 and 31 denote pressure gauges provided near the junction of the two pipes 20 and 21.

【0016】[0016]

【発明の効果】以上で明らかなように、本発明によれば
製紙原液供給装置12から抄紙シリンダー11に供給さ
れる製紙原液の中には、白水中に吹込まれた水中で浮上
しない適量の微細気泡が存在し、この微細気泡が比重
1.2〜1.5程度のパルプ繊維に付着して沈降を抑
え、且つ気泡の流速によってパルプ繊維を分散するの
で、従来の化学粘剤を使用しないでも、使用するにして
も極く少量使用するだけで、抄紙シリンダーによって湿
紙を抄造することができる。従って、化学粘剤を使用し
ない分、コストダウンが図れると共に、抄紙シリンダ
ー、毛布の汚れの発生、紙切れの発生が減少する。又、
微細気泡の混合により、抄紙シリンダー11から白水ピ
ット13に流れ落ちる白水中の溶存酸素の濃度が高ま
り、工場内のパルプの腐敗臭が消え、白水ピット、作業
環境が綺麗に保たれると共に、排水処理のための薬品の
使用量が減少する。
As is apparent from the above description, according to the present invention, the papermaking stock solution supplied from the papermaking stock solution supply device 12 to the papermaking cylinder 11 contains an appropriate amount of fine particles which do not float in the water blown into the white water. Since bubbles are present and these fine bubbles adhere to pulp fibers having a specific gravity of about 1.2 to 1.5 to suppress sedimentation and disperse the pulp fibers by the flow rate of the bubbles, even without using a conventional chemical thickener. Even when used, a wet paper can be formed by a papermaking cylinder by using only a very small amount. Accordingly, the cost can be reduced and the occurrence of stains on the papermaking cylinder and the blanket and the occurrence of paper breakage can be reduced because the chemical tackifier is not used. or,
Due to the mixing of the fine bubbles, the concentration of dissolved oxygen in the white water flowing down from the papermaking cylinder 11 to the white water pit 13 is increased, the odor of pulp in the mill disappears, the white water pit and the working environment are kept clean, and the wastewater is treated. The use of chemicals for is reduced.

【0017】湿紙をドライパートの乾燥ドラムの周面に
付着させて乾燥し、乾燥ドラムの周面からドクターで剥
離することにより紙にクレープを形成する際、紙が乾燥
ドラムの周面に適度に付着していないとクレープを形成
することができない。従って、クレープ付きの紙を製造
する際には微細気泡のほかに少量のはりつけ剤を製紙原
液中に存在させ、これにより抄造した湿紙を乾燥ドラム
の周面に適度に付着させて乾燥し、ドクターで剥離して
クレープが付いた紙を得るようにする。
When wet paper is adhered to the peripheral surface of the drying drum of the dry part and dried, and peeled off from the peripheral surface of the drying drum by a doctor to form crepe on the paper, the paper is appropriately applied to the peripheral surface of the drying drum. If it does not adhere to the crepe, crepe cannot be formed. Therefore, when producing creped paper, a small amount of a sizing agent is present in the stock solution in addition to the fine bubbles, and the wet paper thus formed is appropriately adhered to the peripheral surface of the drying drum and dried. Peel off with a doctor to get creped paper.

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

【図1】本発明による抄紙方法の、一部を拡大断面で示
した一実施形態の説明図。
FIG. 1 is an explanatory view of one embodiment of a papermaking method according to the present invention, in which a part is shown in an enlarged cross section.

【図2】本発明による抄紙方法の他の一実施形態の説明
図。
FIG. 2 is an explanatory view of another embodiment of the papermaking method according to the present invention.

【符号の説明】[Explanation of symbols]

9 コーチロール 10 抄紙装置 11 抄紙シリンダー 12 抄紙シリンダーへの製紙原液供給装置 13 白水ピット 20 パルプ懸濁液の給液管 21 白水の給水管 22 エアコンプレッサー 23 送気管 24 微細気泡製造ミキサー 26 散気体 Reference Signs List 9 coach roll 10 papermaking apparatus 11 papermaking cylinder 12 papermaking stock solution supply device to papermaking cylinder 13 white water pit 20 pulp suspension supply pipe 21 white water supply pipe 22 air compressor 23 air supply pipe 24 fine bubble production mixer 26

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 水中で浮上しない微細な気泡を含んだ微
細気泡水をパルプ懸濁液と混合し、微細気泡水の微細気
泡をパルプ懸濁液中のパルプに付着させて抄紙シリンダ
ーに供給することを特徴とする微細気泡を混入した抄紙
方法。
1. A microbubble water containing microbubbles that do not float in water is mixed with a pulp suspension, and microbubbles of the microbubble water adhere to the pulp in the pulp suspension and are supplied to a papermaking cylinder. A papermaking method containing fine bubbles.
JP11055329A 1999-03-03 1999-03-03 Papermaking of paper mixed with fine bubble Pending JP2000248486A (en)

Priority Applications (1)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005146477A (en) * 2003-11-18 2005-06-09 Fuji Xerox Co Ltd Security paper, method and apparatus for producing the same

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005146477A (en) * 2003-11-18 2005-06-09 Fuji Xerox Co Ltd Security paper, method and apparatus for producing the same
JP4529420B2 (en) * 2003-11-18 2010-08-25 富士ゼロックス株式会社 Security paper and method and apparatus for manufacturing the same

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