JPH07229082A - Paper board - Google Patents

Paper board

Info

Publication number
JPH07229082A
JPH07229082A JP13710993A JP13710993A JPH07229082A JP H07229082 A JPH07229082 A JP H07229082A JP 13710993 A JP13710993 A JP 13710993A JP 13710993 A JP13710993 A JP 13710993A JP H07229082 A JPH07229082 A JP H07229082A
Authority
JP
Japan
Prior art keywords
pulp
paper
paperboard
fine fibrous
strength
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
JP13710993A
Other languages
Japanese (ja)
Inventor
Hisao Ishikawa
久夫 石川
Seiichi Ide
成一 井出
Chitose Kawamata
千登勢 河又
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.)
New Oji Paper Co Ltd
Original Assignee
New Oji Paper Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by New Oji Paper Co Ltd filed Critical New Oji Paper Co Ltd
Priority to JP13710993A priority Critical patent/JPH07229082A/en
Publication of JPH07229082A publication Critical patent/JPH07229082A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain a paper board having high rigidity and good ply bond strength and surface strength. CONSTITUTION:This paper board is produced by laminating two or more wet paper layers produced by using pulp as main raw material. The pulp is incorporated with 0.5-20wt.% of fine fibrous cellulose substance having a water-retention of 210-550% measured in conformity to JAPAN TAPPI No.26-78 and an average fiber length of 0.01-0.4mm.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は板紙に関し、更に詳しく
は、高い剛度、かつ優れた層間強度、表面強度を有し紙
粉の発生の少ない板紙に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to paperboard, and more particularly to paperboard which has high rigidity, excellent interlaminar strength and surface strength, and produces little paper powder.

【0002】[0002]

【従来の技術】板紙に要求される重要な品質として、剛
度(腰の強さ)が要求され、また作業性の面から層間強
度、表面強度が強く紙粉の発生の少ないことが挙げられ
る。板紙をシートとして使用される場合は勿論である
が、特に加工されて使用された場合、例えば、箱に加工
し、内容物を充填して積み重ねたときの箱のつぶれや、
粉体などを詰めたときの箱の胴ぶくれに係わる品質であ
る。又、紙粉の発生は、作業性を著しく低下させるもの
である。
2. Description of the Related Art As an important quality required for paperboard, it is required that rigidity (strength of the waist) is required, and that from the viewpoint of workability, the interlaminar strength and surface strength are strong and less paper dust is generated. Not only when the paperboard is used as a sheet, but when it is processed and used, for example, when it is processed into a box, and when the contents are filled and stacked, the boxes are crushed,
It is the quality related to the blistering of the box when packed with powder and the like. Further, the generation of paper dust significantly reduces workability.

【0003】板紙の剛度を高める方法としては、(1)
紙層の厚さを厚くする、(2)剛度の高いパルプを使用
する、(3)パルプの叩解度を調節する、等の方法があ
るが、これらの方法では剛度の向上に限界があり、表面
性など他の重要品質が悪化するなどの問題を生じること
もある。又、板紙の表面強度を増す方法として、(1)
強度の強い化学パルプの配合量を増やす、(2)紙に澱
粉やポリアクリルアミド等の紙力増強剤を内添あるいは
外添する等がある。しかし、これらの方法では、表面強
度向上に限界があり、又薬品の外添では、新たに薬品を
紙に塗布する装置を必要とする問題がある。
The method for increasing the rigidity of paperboard is (1)
There are methods such as increasing the thickness of the paper layer, (2) using pulp with high rigidity, (3) adjusting the beating degree of pulp, etc., but there is a limit to the improvement in rigidity with these methods, Problems such as deterioration of other important qualities such as surface properties may occur. In addition, as a method of increasing the surface strength of paperboard, (1)
Increasing the amount of chemical pulp having high strength, (2) adding paper strength enhancer such as starch or polyacrylamide to paper internally or externally. However, in these methods, there is a limit to the improvement of the surface strength, and in the case of external addition of chemicals, there is a problem that a device for newly coating chemicals on paper is required.

【0004】[0004]

【発明が解決しようとする課題】本発明は、従来の板紙
の上記問題点を解決し、高い剛度を有し、かつ層間強
度、表面強度が強く紙粉の発生の少ない板紙を提供しよ
うとするものである。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems of conventional paperboard, and provides a paperboard having high rigidity, high interlaminar strength and surface strength and less generation of paper dust. It is a thing.

【0005】[0005]

【課題を解決するための手段】本発明者らは、上記の目
的を達成すべく、板紙についてパルプに注目して鋭意研
究した結果、本発明に至った。すなわち本発明に係わる
板紙は、パルプを主原料とする湿紙の紙層を2層以上合
わせて製造する板紙において、前記パルプ中に、JAPAN
TAPPI No.26-78により規定される保水値が 210%〜550%
で、かつ平均繊維長が 0.01〜0.4mm の微細繊維状セル
ロース物質を 0.5〜20 重量%配合したことを特徴とす
るものである。
[Means for Solving the Problems] In order to achieve the above-mentioned object, the inventors of the present invention have conducted intensive studies by paying attention to pulp for paperboard, and as a result, arrived at the present invention. That is, the paperboard according to the present invention is a paperboard produced by combining two or more paper layers of a wet paper whose main raw material is pulp.
Water retention value specified by TAPPI No. 26-78 is 210% ~ 550%
And 0.5 to 20% by weight of a fine fibrous cellulosic material having an average fiber length of 0.01 to 0.4 mm.

【0006】本発明のための保水値は、微細繊維状セル
ロース物質の微細化の程度と連動している値であり、微
細化の指標として用いた。本発明のための保水値が 210
%以上の微細繊維状セルロース物質の形態は、例えば振
動型粉砕装置にてセルロース物質から得られたパルプの
スラリーを湿式粉砕処理したものを光学顕微鏡で観察す
ると、保水値が210〜250%では繊維幅20〜30μmあるパ
ルプ繊維の一部が破壊され、繊維幅3〜5μmの微細繊維
状のものが生成し始めた状態にある。更に保水値が上昇
するに従い、繊維細胞壁が壊れ、繊維幅3〜5μmのフィ
ブリルが多くなり、これら繊維同士が数本から数十本、
一部で結合乃至絡み合った形状にある。また、繊維を走
査電子顕微鏡にて観察すると繊維幅 0.5μm以下の微細
な繊維も観察される。保水値は、セルロース物質、パル
プの種類、粉砕方式等により変化する。
The water retention value for the present invention is a value that is linked to the degree of miniaturization of the fine fibrous cellulosic material, and was used as an index for the miniaturization. The water retention value for the present invention is 210
% Or more of the fine fibrous cellulosic material is, for example, when a slurry of pulp obtained from the cellulosic material in a vibration type pulverizer is wet pulverized and observed with an optical microscope, the fiber has a water retention value of 210 to 250%. A part of the pulp fiber having a width of 20 to 30 μm is broken, and a fine fiber having a fiber width of 3 to 5 μm starts to be produced. Furthermore, as the water retention value rises, the fiber cell wall is broken, and the number of fibrils with a fiber width of 3 to 5 μm increases.
It has a shape that is partly connected or entangled. When the fibers are observed with a scanning electron microscope, fine fibers with a fiber width of 0.5 μm or less are also observed. The water retention value changes depending on the cellulosic substance, the type of pulp, the grinding method, and the like.

【0007】パルプに微細繊維状のセルロース物質を添
加して用いると板紙の剛度、層間強度、表面強度が向上
する。これは微細繊維状セルロース物質の繊維幅が前記
した如く細いことから繊維表面積の増大と繊維間ネット
ワークの形成に寄与し、パルプの繊維間結合を強める働
きしており、この作用により剛度、層間強度、表面強度
が向上するものと推定される。又、湿紙の紙層を合わせ
る際、紙層表面の微細繊維状セルロース物質が結合に大
きく寄与することが推定される。本発明において用いら
れる微細繊維状セルロース物質の長さについては、平均
繊維長0.01〜0.4mmのものの方が前記の効果が大きく、
繊維長が0.4mmを超えて大き過ぎても、又0.01mm未満の
ように小さ過ぎても効果が小さい。これは繊維長の違い
により、繊維間のネツトワークの形成の仕方が異なるこ
とが考えられる。
When the fine fibrous cellulosic material is added to the pulp, the rigidity, interlayer strength and surface strength of the paperboard are improved. This is because the fiber width of the fine fibrous cellulosic material is thin as described above, which contributes to an increase in the fiber surface area and the formation of an interfiber network, and strengthens the interfiber bond of pulp. It is estimated that the surface strength is improved. In addition, it is presumed that the fine fibrous cellulosic material on the surface of the paper layers greatly contributes to the binding when the paper layers of the wet paper are combined. Regarding the length of the fine fibrous cellulosic material used in the present invention, those having an average fiber length of 0.01 to 0.4 mm have a greater effect as described above,
If the fiber length exceeds 0.4 mm and is too large, or too small, such as less than 0.01 mm, the effect is small. It is conceivable that the way of forming a network between fibers differs depending on the difference in fiber length.

【0008】微細繊維状セルロース物質のパルプに対す
る添加割合が 0.5%重量未満では添加の効果は見られ
ず、又20重量%を超えて添加すると、この原料を用いて
抄紙機において抄紙する際にろ水性が悪くなり、ワイヤ
ーからの脱水ができないので塗工紙原紙を抄造すること
が困難になる。一方、微細繊維状セルロース物質の添加
割合は、微細繊維状セルロース物質の有する保水値にも
関係し、同じ添加の効果を得るのに保水値の高い方が、
添加割合を少なくできるが、使用できる保水値の上限は
550%程度である。
If the addition ratio of the fine fibrous cellulosic material to the pulp is less than 0.5% by weight, the effect of the addition is not seen, and if it is added in excess of 20% by weight, the raw material is filtered during papermaking in a paper machine. Since the water quality becomes poor and the wire cannot be dehydrated, it becomes difficult to make coated paper base paper. On the other hand, the addition ratio of the fine fibrous cellulosic material is also related to the water retention value of the fine fibrous cellulosic material, the higher the water retention value to obtain the same effect of addition,
The addition ratio can be reduced, but the upper limit of the water retention value that can be used is
It is about 550%.

【0009】古紙パルプはリサイクルの回数がますに従
って劣化し、強度が低下してくることが知られており、
又、劣化に伴いパルプが壊れやすく紙粉となり易いた
め、古紙パルプを多く含む原料を使用すると品質上問題
が大きい。このため古紙パルプの配合量が多く、特に全
原料パルプに対し70%以上配合された場合、微細繊維状
セルロース物質の配合効果は大きい。
It is known that the used paper pulp deteriorates and the strength decreases as the number of times of recycling increases,
In addition, since pulp is easily broken into paper powder with deterioration, quality problems are serious when raw materials containing a large amount of waste paper pulp are used. For this reason, when the amount of used paper pulp is large, especially when the amount is 70% or more based on the total raw material pulp, the effect of adding fine fibrous cellulosic material is great.

【0010】本発明に使用される微細繊維状セルロース
物質は、セルロース物質からのパルプ繊維のスラリーを
振動型粉砕装置、奈良機械製作所製「マイクロス粉砕装
置」、高圧均質化装置、メディア撹拌式粉砕装置、コロ
イドミル等により処理することにより得られる。
The fine fibrous cellulosic material used in the present invention is a slurry of pulp fibers from the cellulosic material, vibrating type pulverizer, "Micros pulverizer" manufactured by Nara Machinery Co., Ltd., high pressure homogenizer, media agitation type pulverizer. It is obtained by treating with a device, a colloid mill or the like.

【0011】振動型粉砕装置は、粉砕容器を高速振動さ
せることにより、容器内に充填されたビーズ、ボールま
たはロッド間で試料に衝撃、摩擦、剪断等の力を試料に
作用させて粉砕装置である。奈良機械製作所製マイクロ
ス粉砕装置は、粉砕容器とその中で回転する主軸及び主
軸の回転と連動して公転する数本の副軸から構成され、
各副軸にそれぞれ多数のリング状粉砕媒体が付けられ、
公転、自転するリングと粉砕容器壁面の間で試料を処理
する装置である。又、高圧均質化装置は、セルロース繊
維スラリーを少なくとも3000 psiの圧力差で小径オリフ
ィスを高速度で通過させて粉砕する装置である。メディ
ア撹拌式湿式粉砕装置は、固定した粉砕容器に挿入した
撹拌機を高速で回転させて、粉砕容器内に充填したメデ
ィア(例、ガラスビーズ、アルミナビーズ等)と試料を
撹拌して剪断応力、衝撃力等の力を発生させて試料を粉
砕する装置であり、塔式、槽式、流通管式、アニュラー
式等あるが、メディア撹拌方法であればどの装置でも使
用可能である。コロイドミルとしては、砥粒を樹脂で固
めた回転する円盤状のグラインダー間で試料を処理する
例えば増幸産業製スーパーマスコロイダーが挙げられ
る。
The vibrating crushing device is a crushing device in which a crushing container is vibrated at a high speed to exert a force such as impact, friction or shear on the sample between beads, balls or rods filled in the container. is there. Nara Machinery's Micros crushing device consists of a crushing container, a main shaft that rotates in it, and several sub-shafts that revolve around the rotation of the main shaft.
A large number of ring-shaped grinding media are attached to each counter shaft,
It is a device that processes the sample between the orbiting and rotating ring and the wall of the crushing container. The high-pressure homogenizer is a device for pulverizing the cellulose fiber slurry by passing it through a small diameter orifice at a high speed with a pressure difference of at least 3000 psi. The media agitation type wet pulverization device rotates the agitator inserted in the fixed pulverization container at high speed to agitate the media (eg, glass beads, alumina beads, etc.) and the sample filled in the pulverization container and shear stress, It is a device for crushing a sample by generating a force such as an impact force, and there are a tower type, a tank type, a flow pipe type, an annular type, etc., but any device can be used as long as it is a media stirring method. Examples of the colloid mill include a supermass colloider manufactured by Makoto Sangyo Co., Ltd., which processes a sample between rotating disc-shaped grinders in which abrasive grains are hardened with a resin.

【0012】又、処理方法としては、バッチ式或いは連
続式の何れでも良いし、数台の装置を直列に接続して、
第一段で粗く処理し、後段で微細に処理することも可能
である。また、第一段と第二段で種類の違う装置で処理
することも可能である。本発明の微細繊維状セルロース
に供する原料には、針葉樹パルプ、広葉樹パルプ、古紙
パルプ、これらの混合パルプ、又麻等の非木材パルプ、
コットン等の繊維状セルロース、更にはセルロース微粉
体または粒子類が使用可能である。
The processing method may be either a batch type or a continuous type, and several devices may be connected in series,
It is also possible to perform rough treatment in the first stage and fine treatment in the latter stage. It is also possible to process with different types of devices in the first and second stages. Raw materials to be used for the fine fibrous cellulose of the present invention include softwood pulp, hardwood pulp, waste paper pulp, mixed pulp thereof, and also non-wood pulp such as hemp,
Fibrous cellulose such as cotton, and further cellulose fine powder or particles can be used.

【0013】本発明における抄紙パルプスラリーには、
必要に応じて澱粉、澱粉誘導体或いは、カルボキシメチ
ルセルロース、ポリビニルアルコール、ポリアクリルア
ミド等の湿式紙力増強剤、乾式紙力増強剤を含有させて
もよい。更には、通常の抄紙で使用される添加剤、例え
ばサイズ剤、消泡剤、染料、スライムコントロール剤、
填料、歩留向上剤等を必要に応じて含ませることができ
る。
The papermaking pulp slurry in the present invention includes
If necessary, starch, a starch derivative, or a wet paper strength enhancer such as carboxymethyl cellulose, polyvinyl alcohol, or polyacrylamide may be contained. Furthermore, additives used in ordinary papermaking, such as sizing agents, defoamers, dyes, slime control agents,
Fillers, retention aids and the like can be included as necessary.

【0014】本発明で用いたJAPAN TAPPI No.26-78に準
じた保水値の測定法で一部変更した条件は、G3のガラス
フィルターを取り付けた、低部に穴の開いた円筒状の遠
心管に試料を入れ、3000Gで15分間遠心力を作用させる
ことにより脱水処理し、この遠心脱水された湿潤試料の
重量を測定し、更に105℃で少なくとも5時間に亘って乾
燥させて乾燥重量を測定し、遠心脱水処理後の湿潤試料
重量から乾燥試料重量を減算し、これを乾燥試料重量で
除算し、これに100を乗算して得られる値を意味するも
のである。
The conditions partially changed in the method for measuring the water retention value according to JAPAN TAPPI No. 26-78 used in the present invention are the conditions such as a centrifugal centrifuge with a glass filter of G3 and a hole in the lower part. Put the sample in a tube, dehydration treatment by applying centrifugal force at 3000 G for 15 minutes, measure the weight of this centrifugally dehydrated wet sample, and further dry at 105 ° C for at least 5 hours to obtain the dry weight. It means a value obtained by measuring, subtracting the dry sample weight from the wet sample weight after centrifugal dehydration treatment, dividing this by the dry sample weight, and multiplying this by 100.

【0015】尚、遠心脱水処理すべき供試試料について
は、粉砕処理後の生成物の保水値が高いため、そのまま
で保水値の測定を行うと脱水が困難となり、水相が試料
上部に残るので、前処理としてろ過により予備脱水して
固形分濃度8〜12重量%にしてから保水値測定に供し
た。
Regarding the test sample to be subjected to centrifugal dehydration treatment, since the water retention value of the product after the pulverization treatment is high, dehydration becomes difficult if the water retention value is measured as it is, and the aqueous phase remains on the upper part of the sample. Therefore, as a pretreatment, preliminary dehydration was performed by filtration to obtain a solid content concentration of 8 to 12% by weight, and then the water retention value was measured.

【0016】又、平均繊維長は、フィンランド国KAJAAN
I社製FS-200型繊維長測定装置で測定した数平均繊維長
値及びFS-200型繊維長測定装置では0.05mm以下の測定が
困難なため、繊維長の更に短いものは島津製作所製SALD
-1100型粒度分布測定装置により測定した数値である。
本発明では前記した如き微細繊維状セルロース物質をパ
ルプに添加して用いることにより高い剛度、優れた層間
強度、表面強度を有する板紙を得ることができる。
The average fiber length is KAJAAN in Finland.
Since the number average fiber length value measured by the FS-200 type fiber length measuring device manufactured by Company I and the FS-200 type fiber length measuring device are difficult to measure less than 0.05 mm, those with a shorter fiber length are manufactured by Shimadzu SALD
-1100 is a value measured by a particle size distribution analyzer.
In the present invention, a paperboard having high rigidity, excellent interlaminar strength and surface strength can be obtained by adding the fine fibrous cellulosic material to pulp as described above.

【0017】[0017]

【実施例】下記実施例によって本発明をさらに具体的に
説明するが、本発明はこれによって制限されるものでは
ない。なお、実施例および比較例中の「%」はすべて
「固形分重量%」である。
The present invention will be described in more detail with reference to the following examples, but the present invention is not limited thereto. In addition, all "%" in an Example and a comparative example is "solid content weight%."

【0018】実施例1〜2及び比較例1〜4 フリーネス(c.s.f.) 410mlの段ボール古紙パルプと表1
に示す保水値及び平均繊維長を有する微細繊維状セルロ
ース物質とを表1に示す割合で配合したパルプスラリー
を調製し、次いで、これらのパルプスラリーを JIS P 8
209 に準じ、実験室用角型手抄機を用いて絶乾坪量10
0g/m2 となるよう抄紙し、2枚の湿紙を重ねて絶乾
坪量200g/m2 の一枚の紙として、ウェットプレス
に供した。この時、湿紙をプレスする際にプレス圧を変
化させて同一緊度の板紙を作製した。
Examples 1-2 and Comparative Examples 1-4 Freeness (csf) 410 ml corrugated cardboard waste paper pulp and Table 1
The pulp slurries prepared by mixing the fine fibrous cellulosic material having the water retention value and the average fiber length shown in Table 1 in the ratio shown in Table 1 were prepared.
In accordance with 209, use a square-type laboratory paper machine to obtain an absolute dry basis weight of 10
The paper was made to have a weight of 0 g / m 2, and two wet papers were superposed on each other to obtain a sheet having an absolute dry basis weight of 200 g / m 2 and then subjected to a wet press. At this time, when pressing the wet paper web, the press pressure was changed to produce a paper board having the same tenacity.

【0019】実施例1〜2及び比較例2〜4で使用した
微細繊維状セルロースは、中央化工機製振動型粉砕装置
(MB−1型)を用い、径5mmジルコニアビーズ容量200
0ml、1重量%パルプスラリー900mlを粉砕容器(3400m
l)に入れ、回転数、振幅条件及び供試パルプの種類を
変えて湿式粉砕処理して得たものである。
The fine fibrous cellulose used in Examples 1 to 2 and Comparative Examples 2 to 4 was prepared by using a vibration type pulverizer (MB-1 type) manufactured by Chuo Kakoki Co., Ltd. and having a diameter of 5 mm and a zirconia bead capacity of 200.
Crush container (3400m
It was obtained by wet-grinding in l), changing the number of revolutions, amplitude conditions, and the type of pulp under test.

【0020】本発明で用いた剛度、層間強度及び表面強
度の測定方法は次の通り。 (1)剛度の測定方法 JIS P 8125に準じてテーバーこわさ試験機を使用して測
定した。 (2)層間強度の測定方法 熊谷理機工業製インターナルボンドテスターを用いて測
定した。 (3)表面強度の測定方法 紙試料の表面にRI印刷試験機(明製作所製)で印刷
し、紙表面10cm2 当りの繊維が剥がれた跡の白点(白抜
け)の個数を測定した。
The methods of measuring rigidity, interlaminar strength and surface strength used in the present invention are as follows. (1) Stiffness measurement method According to JIS P 8125, it was measured using a Taber stiffness tester. (2) Method of measuring interlaminar strength It was measured using an internal bond tester manufactured by Kumagai Riki Kogyo. (3) surface strength of the measuring methods paper RI printing tester on the surface of the sample was printed with (manufactured by Akira Seisakusho) to measure the number of white spots trace fibers per paper surface 10 cm 2 was peeled off (white spots).

【0021】実施例3及び比較例5 フリーネス(c.s.f.) 410mlの段ボール古紙パルプ(フリ
ーネス、)とフリーネス(c.s.f.) 470mlの広葉樹漂白パ
ルプ及び表2に示す保水値、平均繊維長を有する微細繊
維状セルロースとを表2に示す割合で配合したパルプス
ラリーを調製し、次いで、これらのパルプスラリーを J
IS P 8209 に準じ、実験室用角型手抄機を用いて絶乾坪
量200g/m2 となるよう抄紙し、2枚の湿紙を重ね
て絶乾坪量400g/m2 の一枚の紙として、ウェット
プレスに供した。この時、湿紙をプレスする際にプレス
圧を変化させて同一緊度の板紙を作製し、板紙の評価を
行った。
Example 3 and Comparative Example 5 Freeness (csf) 410 ml corrugated cardboard waste paper pulp (freeness) and freeness (csf) 470 ml hardwood bleached pulp and fine fibrous cellulose having water retention value and average fiber length shown in Table 2. To prepare pulp slurries containing them in the proportions shown in Table 2 and then adding these pulp slurries to J
According to IS P 8209, paper is made to have an absolute dry basis weight of 200 g / m 2 using a laboratory square-type hand machine, and two wet paper sheets are stacked to form an absolute dry basis weight of 400 g / m 2 . The paper was subjected to a wet press. At this time, when the wet paper web was pressed, the press pressure was changed to produce a paper board having the same tenacity, and the paper board was evaluated.

【0022】実施例3で使用した微細繊維状セルロース
は、2重量%のパルプスラリーを奈良機械製作所製 MIC
RO-2型粉砕装置(ジルコニアリング使用)を使用して湿
式粉砕処理して得たものである。
For the fine fibrous cellulose used in Example 3, 2% by weight of pulp slurry was prepared by MIC manufactured by Nara Machinery Co., Ltd.
It was obtained by wet pulverization using an RO-2 type pulverizer (using zirconia ring).

【0023】実施例4及び比較例6〜7 フリーネス(c.s.f.) 360mlの段ボール古紙パルプと表3
に示す保水値及び平均繊維長を有する微細繊維状セルロ
ース物質とを表3に示す割合で配合したパルプスラリー
を調製し、次いで、これらのパルプスラリーを JIS P 8
209 に準じ、実験室用角型手抄機を用いて絶乾坪量10
0g/m2 となるよう抄紙し、2枚の湿紙を重ねて絶乾
坪量200g/m2 の一枚の紙として、ウェットプレス
に供した。この時、湿紙をプレスする際にプレス圧を変
化させて同一緊度の板紙を作製し、板紙の評価を行っ
た。
Example 4 and Comparative Examples 6 to 7 Freeness (csf) 360 ml corrugated cardboard waste paper pulp and Table 3
A pulp slurry was prepared by mixing the water retention value and the fine fibrous cellulosic material having the average fiber length shown in Table 3 in the proportions shown in Table 3. Then, these pulp slurries were prepared according to JIS P 8
In accordance with 209, use a square-type laboratory paper machine to obtain an absolute dry basis weight of 10
The paper was made to have a weight of 0 g / m 2, and two wet papers were superposed on each other to obtain a sheet having an absolute dry basis weight of 200 g / m 2 and then subjected to a wet press. At this time, when the wet paper web was pressed, the press pressure was changed to produce a paper board having the same tenacity, and the paper board was evaluated.

【0024】実施例4で使用した微細繊維状セルロース
物質は、セルロース微粉体(日本製紙製KCフロック、
平均径25μm、保水値62%)を中央化工機製振動型粉砕
装置(MB−1型)を用い、径5mmのジルコニアビー
ズ 200mlと4重量%濃度のセルロース微粉体 1
000mlを粉砕容器に入れ、湿式粉砕処理して得たも
のである。
The fine fibrous cellulosic material used in Example 4 was a cellulose fine powder (KC Flock manufactured by Nippon Paper Industries,
Using a vibration type pulverizer (MB-1 type) made by Chuo Kakoki Co., Ltd., with an average diameter of 25 μm and a water retention value of 62%), 200 ml of zirconia beads having a diameter of 5 mm and a cellulose fine powder having a concentration of 4% by weight 1
It was obtained by putting 000 ml in a crushing container and performing wet crushing treatment.

【0025】比較例8 湿式粉砕処理していない未処理のセルロース微粉体(日
本製紙製KCフロック、平均径25μm、保水値62%)を
5%、段ボール古紙パルプ(フリーネス、c.s.f360ml)9
5%であること以外実施例4と同様に板紙を作製し、板
紙の評価を行った。表1に実施例1〜2及び比較例1〜
4、表2に実施例3及び比較例5、表3に実施例4及び
比較例6〜8で得られた緊度0.5g/cm3 における
板紙の剛度、層間強度及び表面強度の値を示す。
Comparative Example 8 Untreated cellulose fine powder not subjected to wet crushing treatment (KC floc made by Nippon Paper Industries, average diameter 25 μm, water retention value 62%)
5%, cardboard waste paper pulp (freeness, csf360ml) 9
A paperboard was prepared in the same manner as in Example 4 except that the content was 5%, and the paperboard was evaluated. In Table 1, Examples 1-2 and Comparative Examples 1-
4, Table 2 shows the values of the stiffness, interlayer strength and surface strength of the paperboard at the tightness of 0.5 g / cm 3 obtained in Example 3 and Comparative Example 5 and Table 3 in Example 4 and Comparative Examples 6 to 8. Show.

【0026】[0026]

【表1】 [Table 1]

【0027】[0027]

【表2】 [Table 2]

【0028】[0028]

【表3】 [Table 3]

【0029】表1〜表3の結果から明かなように、本発
明の板紙は剛度が高く、層間強度が強く、又表面強度が
強い(実施例1〜4)のに対し、本発明で用いた微細繊
維状セルロース物質を含まない板紙(比較例1、5、
6)及び平均繊維長0.01mm以下または 0.4mm以上の微細
繊維状セルロース物質、保水値210%以下の微細繊維状セ
ルロース物質を配合したものは、紙の剛度、層間強度、
表面強度の向上効果がないか、小さい(比較例2、4、
7)。公知のセルロース微粉体を用いると未配合の板紙
より剛度、層間強度、表面強度がむしろ悪くなる(比較
例6、8)。更に比較例3に示すように本発明で用いた
微細繊維状セルロース物質を多く使用するとろ水性が悪
くなって抄紙が困難であった。
As is clear from the results shown in Tables 1 to 3, the paperboard of the present invention has high rigidity, strong interlaminar strength, and strong surface strength (Examples 1 to 4), whereas it is used in the present invention. Paperboard containing no fine fibrous cellulosic material (Comparative Examples 1, 5,
6) and fine fiber cellulose material having an average fiber length of 0.01 mm or less or 0.4 mm or more, and a fine fibrous cellulose material having a water retention value of 210% or less are used for paper stiffness, interlayer strength,
There is little or no effect of improving the surface strength (Comparative Examples 2, 4,
7). When the known cellulose fine powder is used, the rigidity, interlaminar strength and surface strength are rather worse than those of unblended paperboard (Comparative Examples 6 and 8). Further, as shown in Comparative Example 3, when a large amount of the fine fibrous cellulosic material used in the present invention was used, the drainage property was deteriorated and the papermaking was difficult.

【0030】これらの結果から、本発明において、平均
繊維長と保水値が前記数値範囲ないにある微細繊維状セ
ルロース物質を所定量配合した板紙を使用することが優
れた剛度、層間強度、表面強度を有する板紙を得る上で
不可欠な要件であることが判る。
From these results, it was found in the present invention that the paperboard containing a predetermined amount of fine fibrous cellulosic material having an average fiber length and a water retention value not within the above-mentioned numerical ranges is excellent in stiffness, interlayer strength and surface strength. It turns out that this is an essential requirement for obtaining a paperboard having

【0031】[0031]

【発明の効果】以上詳細に説明した如く、本発明は、板
紙の原料パルプに特定の微細繊維状セルロース物質を添
加することにより高い剛度で、優れた層間強度を有し、
表面強度が強く紙粉の発生しない板紙が得られ、実用的
に価値の高いものである。
As described in detail above, the present invention has high rigidity and excellent interlaminar strength by adding a specific fine fibrous cellulosic material to the raw material pulp of paperboard,
A board having high surface strength and free of paper dust can be obtained, which is of high practical value.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 パルプを主原料とする湿紙の紙層を2層
以上合わせて製造する板紙において、前記パルプ中に、
JAPAN TAPPI No.26-78により規定される保水値が210%
〜550%で、かつ平均繊維長が 0.01〜0.4mm の微細繊維
状セルロース物質を0.5〜20 重量%配合したことを特徴
とする板紙。
1. A paperboard produced by combining two or more paper layers of a wet paper containing pulp as a main raw material, wherein the pulp contains:
Water retention value specified by JAPAN TAPPI No.26-78 is 210%
A paperboard characterized by containing 0.5 to 20% by weight of a fine fibrous cellulosic material having an average fiber length of 0.01 to 0.4 mm in an amount of 550%.
JP13710993A 1993-06-08 1993-06-08 Paper board Pending JPH07229082A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13710993A JPH07229082A (en) 1993-06-08 1993-06-08 Paper board

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13710993A JPH07229082A (en) 1993-06-08 1993-06-08 Paper board

Publications (1)

Publication Number Publication Date
JPH07229082A true JPH07229082A (en) 1995-08-29

Family

ID=15191056

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13710993A Pending JPH07229082A (en) 1993-06-08 1993-06-08 Paper board

Country Status (1)

Country Link
JP (1) JPH07229082A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010503775A (en) * 2006-09-12 2010-02-04 ミードウエストベコ・コーポレーション Paperboard containing microplatelet cellulose particles
JP2010513741A (en) * 2006-12-18 2010-04-30 アクゾ ノーベル ナムローゼ フェンノートシャップ Method for manufacturing paper products
JP2012197544A (en) * 2011-03-23 2012-10-18 Nippon Paper Industries Co Ltd Method for manufacturing multi-ply paper
KR101360923B1 (en) * 2013-08-20 2014-02-12 신풍제지 주식회사 Method for manufacturing paper board material using wooden organic filler

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010503775A (en) * 2006-09-12 2010-02-04 ミードウエストベコ・コーポレーション Paperboard containing microplatelet cellulose particles
JP2010513741A (en) * 2006-12-18 2010-04-30 アクゾ ノーベル ナムローゼ フェンノートシャップ Method for manufacturing paper products
JP2013064222A (en) * 2006-12-18 2013-04-11 Akzo Nobel Nv Method for producing paper product
JP2012197544A (en) * 2011-03-23 2012-10-18 Nippon Paper Industries Co Ltd Method for manufacturing multi-ply paper
KR101360923B1 (en) * 2013-08-20 2014-02-12 신풍제지 주식회사 Method for manufacturing paper board material using wooden organic filler

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