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JPH0723596B2 - Method for manufacturing wrapping paper and ball paper - Google Patents
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JPH0723596B2 - Method for manufacturing wrapping paper and ball paper - Google Patents

Method for manufacturing wrapping paper and ball paper

Info

Publication number
JPH0723596B2
JPH0723596B2 JP63069223A JP6922388A JPH0723596B2 JP H0723596 B2 JPH0723596 B2 JP H0723596B2 JP 63069223 A JP63069223 A JP 63069223A JP 6922388 A JP6922388 A JP 6922388A JP H0723596 B2 JPH0723596 B2 JP H0723596B2
Authority
JP
Japan
Prior art keywords
parts
paper
amount
added
per
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 - Fee Related
Application number
JP63069223A
Other languages
Japanese (ja)
Other versions
JPS63256795A (en
Inventor
ブルソン リュシアン
ボノー イヴ
Original Assignee
ソシエテ アトケム
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
Family has litigation
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Application filed by ソシエテ アトケム filed Critical ソシエテ アトケム
Publication of JPS63256795A publication Critical patent/JPS63256795A/en
Publication of JPH0723596B2 publication Critical patent/JPH0723596B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H23/00Processes or apparatus for adding material to the pulp or to the paper
    • D21H23/76Processes or apparatus for adding material to the pulp or to the paper characterised by choice of auxiliary compounds which are added separately from at least one other compound, e.g. to improve the incorporation of the latter or to obtain an enhanced combined effect
    • D21H23/765Addition of all compounds to the pulp
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/03Non-macromolecular organic compounds
    • D21H17/05Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/14Carboxylic acids; Derivatives thereof
    • D21H17/15Polycarboxylic acids, e.g. maleic acid
    • D21H17/16Addition products thereof with hydrocarbons
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/03Non-macromolecular organic compounds
    • D21H17/05Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/17Ketenes, e.g. ketene dimers
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/21Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/24Polysaccharides
    • D21H17/28Starch
    • D21H17/29Starch cationic
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/63Inorganic compounds
    • D21H17/66Salts, e.g. alums

Landscapes

  • Paper (AREA)
  • Making Paper Articles (AREA)
  • Wrappers (AREA)
  • Laminated Bodies (AREA)
  • Packaging Of Special Articles (AREA)
  • Cartons (AREA)

Abstract

1. Process for the manufacture of wrapping paper and of cardboard, characterized in that the following are added to the suspension containing the cellulose fibres before the sheet is formed : a) more than 0.5 parts by weight of cationic starch per 100 parts of cellulose fibres, b) less than 1 part by weigth, expressed as Al2 O3 , of aluminium polychloride per 100 parts of cellulose fibres.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、紙、特に包装紙およびボール紙の製造方法に
関する。
FIELD OF THE INVENTION The present invention relates to a method for producing paper, in particular wrapping paper and cardboard.

従来の技術 主としてセルロース繊維から成る原料の製紙用パルプ
は、希薄水性懸濁液にされて抄紙機のフローボックスに
運ばれ、そこで濾布上に分布されてシート状の紙に形成
される。次に、このシートを脱水し、乾燥させる。この
ようにして得られた紙の品質と特性は、特に抄紙機の操
作条件、原料パルプ、シート形成前に懸濁液中に添加す
る種々の添加剤ならびに濾布上に分布した後にシート上
に塗布する物質によって決定される。
2. Description of the Related Art Papermaking pulp, which is a raw material mainly composed of cellulose fibers, is made into a dilute aqueous suspension and conveyed to a flow box of a paper machine, where it is distributed on a filter cloth to form a sheet of paper. The sheet is then dehydrated and dried. The quality and properties of the paper thus obtained depend on, inter alia, the operating conditions of the paper machine, the raw pulp, various additives added in suspension before sheet formation and on the sheet after distribution on the filter cloth. It is determined by the substance to be applied.

本発明は、特に、上記のシート形成前に添加する物質に
関するものである。
The present invention particularly relates to the substance added before the above-mentioned sheet formation.

包装紙に求められる主な品質は強度であるが、この包装
紙に防湿性を付与できればさらに有利である。セルロー
ス繊維は原料パイプから得られるが、再生紙はまた再生
段ボール紙であることも多く、さらにこれと原料パルプ
とを混合したものも用いられる。
The main quality required for the wrapping paper is strength, but it is more advantageous if the wrapping paper can be provided with moisture resistance. Cellulose fibers are obtained from a raw material pipe, but recycled paper is often recycled corrugated cardboard, and a mixture of this and raw material pulp is also used.

発明が解決しようとする課題 イギリス国特許第2,015,614号には、包装紙および段ボ
ール紙の製造方法が記載されているが、この製造による
と、フローボックスに先立ち、陽イオンスターチ(デン
プン)と塩基性アルミニウムポリクロロスルフェートま
たは硫酸アンモニウムを繊維懸濁液に添加する。このと
き、用イオンスターチの添加量は、セルロース繊維に対
し、0.4重量%以下である。陽イオンスターチが、紙に
機械的強度をもたらすことは公知であり、懸濁液中に0.
4%よりはるかに多くのスターチを導入し、特にこのス
ターチを形成されたシート中に保持できればさらに有利
である。ところが、スターチは親水性が大きいため、0.
5%の量を越えると、濾布上でシート状に紙を形成する
ことが全く不可能になるか、あるいは抄紙機の生産性が
著しく低下してしまう。
Problems to be Solved by the Invention British Patent No. 2,015,614 describes a method for producing wrapping paper and corrugated paper. According to this production, cationic starch (starch) and basic starch are added before a flow box. Aluminum polychlorosulfate or ammonium sulfate is added to the fiber suspension. At this time, the added amount of the ion starch for use is 0.4% by weight or less based on the cellulose fiber. Cation starch is known to provide mechanical strength to paper and can be used in suspensions at 0.
It would be further advantageous if much more than 4% of the starch could be introduced and in particular this starch could be retained in the formed sheet. However, since starch is highly hydrophilic,
If the amount exceeds 5%, it becomes impossible at all to form a sheet of paper on the filter cloth, or the productivity of the paper machine is significantly reduced.

そこで、本発明により、抄紙機のフローボックス中に0.
5%以上の量のスターチを用いることを可能にする新規
な方法が見出された。
Therefore, according to the present invention, in the flow box of the paper machine 0.
A new method has been found which makes it possible to use starch in amounts of 5% and above.

課題を解決するための手段 本発明は、シート形成に先立ち、セルロース繊維を含む
懸濁液に、 (a) セルロース繊維100部に対して0.5部以上の陽イ
オンスターチと、 (b) ポリ塩化アルミニウムと を添加することを特徴とする包装紙およびボール紙の製
造方法を提供するものである。
Means for Solving the Problems In the present invention, prior to sheet formation, (a) 0.5 parts by weight or more of cationic starch per 100 parts of cellulose fibers, and (b) polyaluminum chloride are added to a suspension containing cellulose fibers. The present invention provides a method for producing wrapping paper and cardboard, which is characterized by adding and.

上記のセルロース繊維を含む懸濁液は、未処理または漂
白剤のパルプあるいは、これらの混合パルプでもよい。
この混合パルプには、使用済みの紙やボール紙が加えら
れていることが多い。
The above-mentioned suspension containing cellulose fibers may be untreated or bleached pulp or a mixed pulp thereof.
Used paper and cardboard are often added to this mixed pulp.

上記の陽イオンスターチ(デンプン)とは、陽イオンス
ターチの総称で商品化されている1種または複数の製品
の混合物を指す。これらの製品は、例えば、“カークオ
スマー(KIRK OTHMER)”の第三版、第21巻の503ページ
に記載されている。添加量は、セルロース繊維100部に
対して0.5〜5部が望ましく、さらには0.7〜2部が好ま
しい。ポリ塩化アルミニウムとは、通常、“ポリ塩化ア
ルミニウム”、“塩基性ポリ塩化アルミニウム”、“塩
基性アルミニウムポリクロロサルフェート”を意味する
が、特に、下記の物質のうちの1種または複数が望まし
い。
The above-mentioned cationic starch (starch) refers to a mixture of one or more products commercialized under the general term of cationic starch. These products are described, for example, in "KIRK OTHMER", 3rd edition, volume 21, page 503. The addition amount is preferably 0.5 to 5 parts, more preferably 0.7 to 2 parts, based on 100 parts of the cellulose fiber. Polyaluminum chloride generally means "polyaluminum chloride", "basic polyaluminum chloride", "basic aluminum polychlorosulfate", but in particular one or more of the following substances are preferred.

(1) 式: Aln(OH)mCl3n-m (I) (ただし、nは任意の値、3n−mは正の値、またmとn
は正の整数である) で表される塩。この塩はさらに硫酸、燐酸、ポリ燐酸、
珪酸、クロム酸、カルボン酸、スルホン酸の各陰イオン
の中から選択された多価陰イオンYを含んでいてもよ
く、Y/Alのモル比は、望ましくは0.015〜0.4である。
(1): Aln (OH) mCl 3 n - m (I) ( where, n is an arbitrary value, 3n-m is a positive value, and m and n
Is a positive integer). This salt also contains sulfuric acid, phosphoric acid, polyphosphoric acid,
It may contain a polyvalent anion Y selected from anions of silicic acid, chromic acid, carboxylic acid and sulfonic acid, and the Y / Al molar ratio is preferably 0.015 to 0.4.

(2) 式: Aln(OH)mCl3n-m-2k(SO4)k (II) (ただし、k、m、nは正の整数;3n>m+2k;塩基度m/
3nは0.3〜0.7;k/n=0.01〜0.3である) で表される塩。この物質は、アメリカ合衆国特許第3,92
9,666号に記載された方法に従って製造することができ
る。
(2): Aln (OH) mCl 3 n - m -2 k (SO 4) k (II) ( provided that, k, m, n is a positive integer; 3n> m + 2k; basicity m /
3n is 0.3 to 0.7; k / n = 0.01 to 0.3). This material is the subject of U.S. Pat.
It can be manufactured according to the method described in No. 9,666.

(3) 式: 〔Aln(OH)3n-m-2pClm(SO4P)〕z (III) 〔ただし、(3n−m−2p)/3n=0.4〜0.7;p=0.04〜0.2
5n;m/p=8〜35;k、m、nおよびpは整数;zは1以上の
値である〕 で表される塩。この物質は、イギリス国特許第2,128,97
7号中に記載されている。
(3): [Aln (OH) 3 n - m -2 pClm (SO 4P) ] z (III) [However, (3n-m-2p) /3n=0.4~0.7;p=0.04~0.2
5n; m / p = 8 to 35; k, m, n and p are integers; z is a value of 1 or more]. This material is a British Patent No. 2,128,97
It is described in No. 7.

(4) 式: AlnOHm(SO4)kCl3n-m-2k (IV) (ただし、塩基度すなわちモル比(m/3n)×100は約40
〜65%の範囲内;Al当量/Cl当量の比は2.8〜5;公知の光
散乱により測定された見掛分子量AM、ならびに準弾性光
散乱により測定された見掛の流体力学的粒径φZおよび
φWは、それぞれ AM=7,000〜35,000 φZ(Å)=350〜2,500 φW(Å)=200〜1,200 である) で表される塩基正アルミニウムクロロサルフェート。こ
の物質はフランス国特許第2,584,699号に記載されてい
る。
(4): AlnOHm (SO 4) kCl 3 n - m -2 k (IV) ( where basicity namely the molar ratio (m / 3n) × 100 is about 40
In the range of ~ 65%; Al equivalent / Cl equivalent ratio of 2.8 to 5; apparent molecular weight AM measured by known light scattering, and apparent hydrodynamic particle size φZ measured by quasi-elastic light scattering. And φW are AM = 7,000 to 35,000 φZ (Å) = 350 to 2,500 φW (Å) = 200 to 1,200 respectively), which is a basic positive aluminum chlorosulfate. This material is described in French Patent No. 2,584,699.

Al2O3で表されるポリ塩化アルミニウムの使用量は、セ
ルロース繊維100部に対して1部以下が望ましく、さら
には0.02〜0.3部が好ましい。
The amount of polyaluminum chloride represented by Al 2 O 3 is preferably 1 part or less, and more preferably 0.02 to 0.3 part, based on 100 parts of the cellulose fiber.

上記の物質(a)および(b)は抄紙機のフローボック
ス前であれば任意の順序でまた任意の位置で、添加する
ことができるが、陽イオンスターチの後にポリ塩化アル
ミニウムを添加するのが望ましい。また、ポリ塩化アル
ミニウムは、フローボックスに出来る限り近い地点で添
加するのが望ましい。
The above substances (a) and (b) can be added in any order and at any position before the flow box of the paper machine, but it is preferable to add the polyaluminum chloride after the cation starch. desirable. Further, it is desirable to add the polyaluminum chloride at a point as close as possible to the flow box.

シート形成に先立ち、セルロース繊維を含む懸濁液に、
物質(a)および(b)の他に、着色剤等の他の物質を
添加することも可能である。
Prior to sheet formation, a suspension containing cellulose fibers,
In addition to substances (a) and (b), it is also possible to add other substances such as colorants.

本発明に従う別の態様によると、陽イオンスターチの他
に、ポリアクリルアミド、ポリエチレンイミン、カルボ
キシメチルセルロース、尿素−ホルムアルデヒド樹脂、
メラミン−ホルムアルデヒド樹脂、アミノポリアミド−
エピクロロヒドリン樹脂およびポリアミド−エピクロロ
ヒドリン樹脂の中から選択される1種または複数の物質
を添加することができる。これらの物質は、陽イオンス
ターチに加えて用いられ、これと同じ量を添加するのが
望ましい。
According to another aspect according to the invention, in addition to cationic starch, polyacrylamide, polyethyleneimine, carboxymethylcellulose, urea-formaldehyde resin,
Melamine-formaldehyde resin, aminopolyamide-
One or more substances selected from epichlorohydrin resins and polyamide-epichlorohydrin resins can be added. These substances are used in addition to the cation starch, and it is desirable to add the same amount.

本発明の別の態様では、上記物質(a)および(b)あ
るいは陽イオンスターチの他に添加されるポリアクリル
アミド等の上記の物質の他に、さらにサイズ剤を添加す
ることにより、紙を若干疎水性にしてこれに防湿性を帯
びさせることができる。
In another aspect of the invention, the paper may be slightly modified by adding a sizing agent in addition to the above substances (a) and (b) or the above substances such as polyacrylamide added in addition to the cationic starch. It can be made hydrophobic to make it moisture proof.

この場合、任意のサイズ剤の適用が可能であるが、ロジ
ンあるいは、二量体アルキルケテンおよびその誘導体、
弗素化燐酸塩、脂肪族カルボン酸の無水物、ポリウレタ
ンおよびスチレン/無水マレイン酸コポリマーの中から
選択される1種または複数の物質を用いるのが望まし
い。
In this case, any sizing agent can be applied, but rosin or dimer alkyl ketene and its derivative,
It is desirable to use one or more materials selected from fluorinated phosphates, anhydrides of aliphatic carboxylic acids, polyurethanes and styrene / maleic anhydride copolymers.

特に、二量体アルキルケテンおよび無水カルボン酸を用
いるのが好ましい。これらの使用量は、紙またはボール
紙に求められる特性に応じて異なるが、セルロース繊維
100部に対し10部以下が望ましく、さらには0.1〜2部が
好ましい。
Particularly, it is preferable to use dimer alkyl ketene and carboxylic acid anhydride. The amount of these used varies depending on the properties required for the paper or the cardboard, but the cellulose fiber
It is preferably 10 parts or less with respect to 100 parts, and more preferably 0.1 to 2 parts.

サイズ剤は、ポリ塩化アルミニウムの前に添加するのが
望ましい。
The size is preferably added before the polyaluminum chloride.

また、着色剤等の通常の添加剤をシート形成前の懸濁液
に添加することもできる。
Further, usual additives such as colorants may be added to the suspension before sheet formation.

本発明による利点として、優れた機械的性質をもたらす
以外に、シート形成中濾布の下に回収される水中の浮遊
物が大幅に減少する点が挙げられる。
Among the advantages of the present invention, besides providing excellent mechanical properties, is that the amount of suspended solids in the water collected under the filter cloth during sheet formation is greatly reduced.

さらに、本発明により、抄紙紙の生産性が高まり、内部
凝集が向上する。このような利点の全ては実施例におい
て認めることができる。以下に示す実施例により、本発
明をさらに詳しく説明する。
Furthermore, the present invention improves the productivity of papermaking paper and improves internal cohesion. All of these advantages can be seen in the examples. The present invention will be described in more detail with reference to the following examples.

比較例(本発明によらないもの) (1) フローボックス中の成分 100%古紙 サイズ剤:二量体アルキルケテン0.15部 (2) 抄紙機の操作条件: 金網、有効ウェブ幅:2.6m 基本重量:190g/m2 紙の種類:段ボール用ライナー (3) 抄紙後の処理: 表面に天然スターチを噴霧。Comparative example (not according to the present invention) (1) Ingredients in flow box 100% waste paper Sizing agent: dimer alkylketene 0.15 parts (2) Operating conditions of paper machine: wire mesh, effective web width: 2.6 m Basic weight : 190g / m 2 Paper type: Cardboard liner (3) Treatment after paper making: Natural starch is sprayed on the surface.

本比較例では、繊維100部に対して1.4部の陽イオンスタ
ーチをフローボックス中に添加した。
In this comparative example, 1.4 parts of cation starch was added to the flow box per 100 parts of fiber.

結果は下記の通り: 抄紙機速度:163m/分 全残量:79% ミューレン破裂係数:2.75 (AFNOR規格NF Q 03053に基づく) pH(フローボックス中):7.2。Results are as follows: Paper machine speed: 163m / min Total balance: 79% Mullen burst factor: 2.75 (based on AFNOR standard NF Q 03053) pH (in flow box): 7.2.

実施例1(本発明による) 比較例と同様な操作を行うが、フローボックス中に、ポ
リ塩化アルミニウムを、Al2O3で表した場合、セルロー
ス繊維100部に対し0.15部の割合でさらに添加した。
Example 1 (according to the invention) The same operation as in the comparative example is carried out, but when polyaluminum chloride is represented by Al 2 O 3 in the flow box, it is further added in a ratio of 0.15 parts to 100 parts of the cellulose fibers. did.

結果は下記の通り: 抄紙機速度:200m/分 全残量:85% ミューレン破裂係数:3.09 pH(フローボックス中):7.2。The results are as follows: Paper machine speed: 200 m / min Total balance: 85% Mullen burst coefficient: 3.09 pH (in flow box): 7.2.

実施例2(本発明による) 実施例1と同様な操作を行うが、実施例1で添加したポ
リ塩化アルミニウムをセルロース繊維100部に対し0.16
部添加した。
Example 2 (according to the invention) The same operation as in Example 1 is carried out, except that the polyaluminum chloride added in Example 1 is added in an amount of 0.16 per 100 parts of the cellulose fiber.
Added in parts.

結果は下記の通り: 抄紙機速度:220m/分 全残量:85% ミューレン破裂係数:2.96 pH(フローボックス中):7.2。Results are as follows: Paper machine speed: 220 m / min Total balance: 85% Mullen burst coefficient: 2.96 pH (in flow box): 7.2.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 D21H 17/33 17/63 (56)参考文献 特公 昭36−21810(JP,B1) 特公 昭45−28004(JP,B1)─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location D21H 17/33 17/63 (56) References Japanese Patent Publication Sho 36-21810 (JP, B1) Japanese Patent Publication 45-2804 (JP, B1)

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】抄紙前に、セルロース繊維を含む懸濁液に
フローボックス中で下記(a)および(b)を添加する
ことを特徴とする包装紙およびボール紙の製造方法: (a) セルロース繊維100部に対して0.5部以上の陽イ
オンスターチ、 (b) ポリ塩化アルミニウム。
1. A method for producing wrapping paper and cardboard, which comprises adding the following (a) and (b) in a flow box to a suspension containing cellulose fibers before papermaking: (a) Cellulose 0.5 parts or more of cationic starch per 100 parts of fiber, (b) polyaluminum chloride.
【請求項2】サイズ剤をさらに添加する請求項1に記載
の方法。
2. The method of claim 1, further comprising adding a sizing agent.
【請求項3】(b)が塩基性アルミニウムポリクロロサ
ルフェートである請求項1または2に記載の方法。
3. The method according to claim 1, wherein (b) is basic aluminum polychlorosulfate.
【請求項4】(a)をセルロース繊維100部に対して0.5
〜5部の量で使用する請求項1〜3のいずれか一項に記
載の方法。
4. The amount of (a) is 0.5 per 100 parts of cellulose fiber.
The method according to any one of claims 1 to 3, which is used in an amount of -5 parts.
【請求項5】(b)を、Al2O3で表した場合、セルロー
ス繊維100部に対して1部以下の量で使用する請求項1
〜4のいれか一項に記載の方法。
5. When (b) is represented by Al 2 O 3 , it is used in an amount of 1 part or less per 100 parts of the cellulose fiber.
4. The method according to any one of 4 to 4.
【請求項6】上記サイズ剤が二量体アルキルケテンまた
は無水カルボン酸である請求項2〜5のいずれか一項に
記載の方法。
6. The method according to claim 2, wherein the sizing agent is a dimeric alkylketene or a carboxylic acid anhydride.
【請求項7】上記サイズ剤の使用量がセルロース繊維10
0部に対して10部以下である請求項2〜6のいずれか一
項に記載の方法。
7. The amount of the sizing agent used is cellulose fiber 10
The method according to any one of claims 2 to 6, which is 10 parts or less with respect to 0 parts.
【請求項8】(a)および(b)または(a)、(b)
およびサイズ剤の他に、ポリアクリルアミド、ポリエチ
レンイミン、カルボキシメチルセルロース、尿素−ホル
ムアルデヒド樹脂、メラミン−ホルムアルデヒド樹脂、
アミノポリアミド−エピクロロヒドリン樹脂およびポリ
アミド−エピクロロヒドリン樹脂の中から選択される少
なくとも1種の物質を添加する請求項1〜7のいずれか
一項に記載の方法。
8. (a) and (b) or (a), (b)
And sizing agents, polyacrylamide, polyethyleneimine, carboxymethylcellulose, urea-formaldehyde resin, melamine-formaldehyde resin,
8. The method according to any one of claims 1 to 7, wherein at least one substance selected from aminopolyamide-epichlorohydrin resin and polyamide-epichlorohydrin resin is added.
JP63069223A 1987-03-23 1988-03-23 Method for manufacturing wrapping paper and ball paper Expired - Fee Related JPH0723596B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8704002 1987-03-23
FR8704002A FR2612960B1 (en) 1987-03-23 1987-03-23 PROCESS FOR THE MANUFACTURE OF PACKAGING PAPER AND CARDBOARD BY ADDITION TO THE FIBROUS SUSPENSION OF CATIONIC STARCH AND ALUMINUM POLYCHLORIDE

Publications (2)

Publication Number Publication Date
JPS63256795A JPS63256795A (en) 1988-10-24
JPH0723596B2 true JPH0723596B2 (en) 1995-03-15

Family

ID=9349311

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Application Number Title Priority Date Filing Date
JP63069223A Expired - Fee Related JPH0723596B2 (en) 1987-03-23 1988-03-23 Method for manufacturing wrapping paper and ball paper

Country Status (13)

Country Link
EP (1) EP0285486B2 (en)
JP (1) JPH0723596B2 (en)
AT (1) ATE56493T1 (en)
CA (1) CA1324704C (en)
DE (1) DE3860586D1 (en)
DK (1) DK171149B1 (en)
ES (1) ES2018079T5 (en)
FI (1) FI94971C (en)
FR (1) FR2612960B1 (en)
GR (2) GR3001183T3 (en)
IE (1) IE60108B1 (en)
NO (1) NO174012C (en)
PT (1) PT87043B (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02293493A (en) * 1989-04-28 1990-12-04 Arakawa Chem Ind Co Ltd Sizing agent for ketene dimer-based paper making
FR2678961B1 (en) * 1991-07-12 1993-10-15 Atochem NEW PROCESS FOR THE MANUFACTURE OF PAPER AND THE PAPER THUS OBTAINED.
IT1271003B (en) * 1994-09-08 1997-05-26 Ausimont Spa HIGH MECHANICAL RESISTANCE PAPER AND CARDBOARD PRODUCTION PROCESS
FR2732368B1 (en) * 1995-03-31 1997-06-06 Roquette Freres NEW PAPERMAKING PROCESS
FR2743810B1 (en) 1996-01-23 1998-04-10 Roquette Freres MODIFIED CATIONIC POLYSACCHARIDES, BONDING COMPOSITIONS CONTAINING THEM AND METHODS FOR BONDING PLANAR STRUCTURES USING THE SAME
CN114673025B (en) 2016-06-01 2023-12-05 艺康美国股份有限公司 High-efficiency strength scheme for papermaking in high-charge-demand systems
CN109468886A (en) * 2018-12-27 2019-03-15 东莞市江高包装材料有限公司 A kind of production technology of wrapping paper
CA3228526A1 (en) 2021-08-31 2023-03-09 Mingli Wei Novel composition and method for papermaking

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5374118A (en) * 1976-12-09 1978-07-01 Toa Gosei Chem Ind Additives for paper making
FR2418297A1 (en) * 1978-02-27 1979-09-21 Ugine Kuhlmann IMPROVEMENT OF PAPER AND BOARD MANUFACTURING PROCESSES
JPS59199900A (en) * 1983-04-18 1984-11-13 三菱製紙株式会社 Neutral paper
JPS60185899A (en) * 1984-03-05 1985-09-21 三菱製紙株式会社 acid-free paper
SE8405260L (en) * 1984-10-22 1986-04-23 Eka Ab HYDROPHOBING AGENTS FOR ORGANIC FIBERS, Separate CELLULOS FIBERS, SET TO MAKE THIS AGENT AND THE USE OF THE MELD HYDROPHOBING AGENT

Also Published As

Publication number Publication date
NO881030L (en) 1988-09-26
PT87043A (en) 1988-04-01
GR3001183T3 (en) 1992-06-30
DK154688D0 (en) 1988-03-22
FI881368L (en) 1988-09-24
ES2018079B3 (en) 1991-03-16
CA1324704C (en) 1993-11-30
EP0285486A1 (en) 1988-10-05
JPS63256795A (en) 1988-10-24
FR2612960A1 (en) 1988-09-30
FI94971C (en) 1995-11-27
FI881368A0 (en) 1988-03-22
NO174012B (en) 1993-11-22
DK171149B1 (en) 1996-07-01
FI94971B (en) 1995-08-15
EP0285486B2 (en) 1997-12-17
IE880841L (en) 1988-09-23
ES2018079T5 (en) 1998-02-16
FR2612960B1 (en) 1989-06-16
NO174012C (en) 1994-03-02
IE60108B1 (en) 1994-06-01
ATE56493T1 (en) 1990-09-15
DE3860586D1 (en) 1990-10-18
PT87043B (en) 1992-07-31
GR3026342T3 (en) 1998-06-30
EP0285486B1 (en) 1990-09-12
NO881030D0 (en) 1988-03-08
DK154688A (en) 1988-09-24

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