JP2931130B2 - Multilayered hydrolyzed paper and method for producing the same - Google Patents
Multilayered hydrolyzed paper and method for producing the sameInfo
- Publication number
- JP2931130B2 JP2931130B2 JP16760291A JP16760291A JP2931130B2 JP 2931130 B2 JP2931130 B2 JP 2931130B2 JP 16760291 A JP16760291 A JP 16760291A JP 16760291 A JP16760291 A JP 16760291A JP 2931130 B2 JP2931130 B2 JP 2931130B2
- Authority
- JP
- Japan
- Prior art keywords
- paper
- water
- layer
- outermost layer
- weight
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Landscapes
- Cleaning Implements For Floors, Carpets, Furniture, Walls, And The Like (AREA)
- Paper (AREA)
Description
【0001】[0001]
【産業上の利用分野】この発明は、アルコール等の薬液
を含浸したときの強度が高く、しかも優れた水解性を有
する多層構造の水解紙に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a multi-layer water disintegrating paper having high strength when impregnated with a chemical such as alcohol and having excellent water dissolving properties.
【0002】[0002]
【従来の技術】清浄用アルコール等を含浸させて使用す
る清拭用紙であって、これを水中に投棄すると構成繊維
が速やかに水中に分散する水解紙、速溶紙についてはよ
く知られている。例えば、特公昭42ー2925号公報
は実質的に繊維素よりなる連続紙をその紙状のままエー
テル化し速溶性の洗剤含有洗滌紙、化粧紙等を連続的に
製造方法する方法を開示している。この技術によれば市
場の抄造紙を適宜速溶化することができる。また特開平
1ー168999号公報は水分散性製紙用繊維と水不溶
性カルボキシメチル化パルプとを混抄して水易分散性で
あって薬液を含浸したときの強度が高い水解紙を得る技
術を開示している。2. Description of the Related Art It is well known that wiping paper is used by impregnating it with cleaning alcohol or the like, and when it is discarded in water, constituent fibers are rapidly dispersed in water. For example, Japanese Patent Publication No. 42-2925 discloses a method for continuously producing a rapidly dissolving detergent-containing cleaning paper, a decorative paper, etc. by etherifying a continuous paper substantially made of fibrous material in the form of paper. I have. According to this technique, papermaking paper on the market can be rapidly dissolved as appropriate. JP-A-1-168999 discloses a technique of mixing water-dispersible papermaking fibers and water-insoluble carboxymethylated pulp to obtain a water-disintegrated paper which is easily dispersible in water and has high strength when impregnated with a chemical solution. doing.
【0003】[0003]
【発明が解決しようとする課題】前記各技術によれば本
発明が提供しようとする洗剤、消毒薬その他の薬液を含
浸させて使用する、例えば手拭きその他の清拭用紙であ
って、水解性の紙を一応得ることができる。According to each of the above-mentioned technologies , for example, a hand-wiping or other wiping paper which is impregnated with a detergent, a disinfectant or another chemical solution to be provided by the present invention is used. You can get some paper.
【0004】しかしながら、特公昭42ー2925号公
報の技術は折畳み可能な連続紙を必要とし、しかも連続
紙のロールを解いてエーテル化処理する必要から、その
対象にすることができる連続紙は比較的坪量の大きい紙
である。換言すると、例えば坪量10〜50g/m2程
度の比較的坪量の小さい水解紙は作り難いという問題が
ある。また、特開平1ー168999号公報の技術は紙
力増強剤として多量の水不溶性カルボキシメチル化パル
プを混合した紙料を抄紙するものである。かかる紙料
は、抄紙工程のドライパートにおいて接触型乾燥機を使
用すると、乾燥が進行するにつれその接触面が乾燥機に
強く接着し、剥離が難しくなる。それ故にこの技術では
汎用の接触型乾燥機を使用し難いという問題がある。However, the technology disclosed in Japanese Patent Publication No. 42925/1972 requires a foldable continuous paper, and furthermore, it is necessary to unwind the roll of the continuous paper and carry out the etherification treatment. This is a paper with a large basis weight. In other words, there is a problem that it is difficult to produce a hydrolyzed paper having a relatively small basis weight, for example, about 10 to 50 g / m 2 . The technique disclosed in Japanese Patent Application Laid-Open No. 1-168999 is to make a paper stock mixed with a large amount of a water-insoluble carboxymethylated pulp as a paper strength enhancer. When a contact type dryer is used in the dry part of the papermaking process, the contact surface of the paper material strongly adheres to the dryer as drying proceeds, and peeling becomes difficult. Therefore, this technique has a problem that it is difficult to use a general-purpose contact dryer.
【0005】そこでこの発明は水解紙を少なくとも2層
で構成し、該水解紙の対向する二つの最外層において一
方の最外層が相対的に多量の紙力増強剤を含み、他方の
最外層が相対的に少量の紙力増強剤を含むようにするこ
とで前記問題を解決しようとするものである。Accordingly, the present invention comprises a hydrolytic paper comprising at least two layers, one of the two outermost layers of the hydrolytic paper containing a relatively large amount of a paper-strengthening agent, and the other outermost layer comprising The above problem is intended to be solved by including a relatively small amount of a paper strength enhancer.
【0006】[0006]
【課題を解決するための手段】この発明が前記課題を解
決するために要旨とするところは次のとおりである。The gist of the present invention to solve the above problems is as follows.
【0007】この発明は多層構造の水解紙及びその製造
方法の提供を前提としており、かかる水解紙は、少なく
とも2層からなる多層構造を有し、該水解紙の対向して
位置する両最外層のうちの一方の最外層が10〜60重
量%の紙力増強剤を含み、他方の最外層が5重量%以下
の紙力増強剤を含み、前記紙力増強剤が、カルボキシメ
チル化パルプのナトリウム塩、前記ナトリウム塩を含む
カルボキシメチル化パルプの混合塩、水溶性ポリビニル
アルコール、水溶性ポリビニルアルコール繊維、および
これらの混合物のいずれかであることが要旨である。ま
た、前記製造方法においては、接触型乾燥機を使用して
湿紙を乾燥する工程を含む多層構造の水解紙の製造方法
であって、乾燥重量において10〜60重量%の紙力増
強剤を含む第1紙料と、5重量%以下の紙力増強剤を含
む第2紙料とを少なくとも使用する。各紙料が前記湿紙
の各々の最外層を構成するように多層構造として湿紙を
得た後、前記第2紙料からなる湿紙の最外層を前記接触
型乾燥機に対する接触面として乾燥することにより前記
第1、第2紙料が前記水解紙の各々の最外層を構成する
ようにすることが要旨である。[0007] The present invention is based on the premise of providing water-decomposable paper and a manufacturing method thereof of a multilayer structure, such water-decomposable paper having a multilayer structure comprising at least two layers, both outermost layers located opposite the water-decomposable paper one comprises the outermost layer is 10 to 60% by weight of paper strength agent, only contains the other outermost layer 5 wt% or less of a paper strength agent of the strength agent is carboxymethyl
Sodium salt of chilled pulp, including said sodium salt
Mixed salt of carboxymethylated pulp, water-soluble polyvinyl
Alcohol, water-soluble polyvinyl alcohol fiber, and
The gist is to be any of these mixtures . Further, in the above-mentioned production method, there is provided a method for producing a multi-layered hydrolyzed paper comprising a step of drying a wet paper using a contact dryer, wherein a paper strength enhancer having a dry weight of 10 to 60% by weight is used. At least a first furnish containing at least 5% by weight of a paper furnish. After obtaining the wet paper as a multilayer structure so that each stock constitutes each outermost layer of the wet paper, the outermost layer of the wet paper comprising the second stock is dried as a contact surface to the contact type dryer. The gist is that the first and second stocks constitute the outermost layer of each of the hydrolyzed papers.
【0008】前記製造方法の好ましい実施態様において
は、前記紙力増強剤が、カルボキシメチル化パルプのナ
トリウム塩、前記ナトリウム塩を含むカルボキシメチル
化パルプの混合塩、水溶性ポリビニルアルコール、水溶
性ポリビニルアルコール繊維、およびこれらの混合物の
いずれかである。 In a preferred embodiment of the production method, the paper strength agent, the carboxymethylated pulp Na
Thorium salt, carboxymethyl containing the sodium salt
Mixed salt of pulp, water-soluble polyvinyl alcohol, water-soluble polyvinyl alcohol fiber, and mixtures thereof
Ru der either.
【0009】[0009]
【作用】上述のように構成したこの発明に係る水解紙で
は、紙力増強剤について高含有量の最外層が薬液含浸状
態においても優れた表面強度を発揮し、容易に破れるこ
とがないから、この最外層は専ら清拭用の面として使用
するのに好適である。他方の最外層は紙力増強剤につい
て低含有量であって、高々5%を含有するのみである。
従って、この層は水中において速やかに分散し、一方の
最外層が高含有量の紙力増強剤の影響により、水解紙の
水解性を低下させる傾向を有するにもかかわらず、水解
紙に良好な水解性をもたらす。またかかる構成の水解紙
は、その抄紙工程において紙力増強剤について低含有量
の最外層を接触型乾燥機に対する接触面とすることがで
きる。この接触面は乾燥後、乾燥機から至極容易に剥離
するから一方の最外層が多量の紙力増強剤を含有するに
もかかわらず水解紙の生産性を低下させることがない。In the hydrolytic paper according to the present invention configured as described above, the outermost layer having a high content of the paper strength enhancer exhibits excellent surface strength even in the state of being impregnated with a chemical solution, and does not easily break. This outermost layer is suitable for use exclusively as a wiping surface. The other outermost layer has a low content of the paper strength agent and contains only at most 5%.
Therefore, this layer disperses promptly in water, and although one outermost layer has a tendency to decrease the water disintegration property of the water disintegrated paper due to the effect of the high strength paper strength agent, it is good for water disintegrated paper. Brings water degradability. Further, in the water-disintegrated paper having such a configuration, the outermost layer having a low content of the paper-strength enhancer in the papermaking process can be used as the contact surface to the contact dryer. This contact surface is extremely easily peeled off from the dryer after drying, so that the productivity of hydrolyzed paper does not decrease even though one outermost layer contains a large amount of a paper strength enhancer.
【0010】[0010]
【実施例】この発明の詳細を添付の図に基づいて説明す
ると以下のとおりである。DESCRIPTION OF THE PREFERRED EMBODIMENTS The details of the present invention will be described below with reference to the accompanying drawings.
【0011】図1は、この発明に係る水解紙1の抄紙工
程を模式的に示している。工程は少なくとも2系列の第
1、第2原料調製工程2,2’、1台ずつの短網ワイヤ
ー9と丸網抄紙機13、ピックアップ・フェルトベルト
11、フェルトベルト12、乾燥筒17等を含む。各原
料調製工程2,2’は原料パルプに対する第1、第2離
解タンク4,4’、サイズ剤、紙力増強剤等を配合して
第1、第2紙料10、10’を調製する第1、第2配合
タンク5,5’を備え、これらは移送パイプ6,6’で
つながっている。第1配合タンク5はヘッドボックス7
につながり、ヘッドボックス7は無端のワイヤメッシュ
ベルト9’からなるワイヤーパート9の一端においてベ
ルト9’の上に臨み、ここで紙料10を定量供給する。
ベルト9’は図1において反時計方向に走行し、ワイヤ
ーパート9の他端は無端のピックアップ・フェルトベル
ト11に接する。このベルト11は時計方向に走行す
る。一方第2配合タンク5’は丸網抄紙機13につなが
り、濾槽12に紙料10’を供給する。丸網抄紙機13
において丸網13’はその一部が紙料10’の中につか
り、その頂部がピックアップ・フェルトベルト11に接
する。ピックアップ・フェルトベルト11は時計方向に
走行しながらまずベルト9’から第1紙料10により形
成された紙層14をピックアップし、その後に丸網1
3’から第2紙料10’による紙層15を紙層14に粘
着させるかたちでピックアップする。ピックアップ・フ
ェルトベルト11に形成された紙層14と15とからな
る湿紙16は、フェルトベルト12にピックアップされ
たのち、乾燥筒(ドライヤー)17の表面に移し取られ
て加熱乾燥を受け2層構造の水解紙1となって捲き取ら
れ、ロール18となる。このような一連の抄紙工程は周
知の工程、設備を利用すればよいものであり、適宜上記
以外の附帯設備を追加することができる。この発明で
は、第1原料調製工程2において紙力増強剤添加量を紙
料10の乾燥重量基準で5%以下とし、第2調製工程
2’においてはその添加量を10〜60%とする。これ
により湿紙16は紙力増強剤添加量の少ない紙層14を
乾燥筒17に接触させるかたちで乾燥することができ
る。乾燥後には紙力増強剤を高々5%しか含まない紙層
14が乾燥筒17から容易に剥離する。FIG. 1 schematically shows a paper making process of the hydrolyzed paper 1 according to the present invention. The process includes at least two series of first and second raw material preparation steps 2 and 2 ′, one short net 9 and one round net paper machine 13, a pickup / felt belt 11, a felt belt 12, a drying cylinder 17 and the like. . In each raw material preparation step 2, 2 ', first and second disintegration tanks 4, 4' for the raw pulp, a sizing agent, a paper strength enhancer, and the like are blended to prepare first and second stocks 10, 10 '. First and second compounding tanks 5, 5 'are provided, which are connected by transfer pipes 6, 6'. The first mixing tank 5 is a head box 7
, The head box 7 faces the belt 9 ′ at one end of the wire part 9 comprising the endless wire mesh belt 9 ′, where the stock 10 is supplied in a fixed amount.
The belt 9 'runs counterclockwise in FIG. 1, and the other end of the wire part 9 contacts the endless pickup / felt belt 11. This belt 11 runs clockwise. On the other hand, the second blending tank 5 ′ is connected to a round paper machine 13, and supplies the stock 10 ′ to the filter tank 12. Round mesh paper machine 13
In FIG. 7, a part of the round net 13 'hangs in the stock 10', and the top of the net 13 'comes into contact with the pickup felt belt 11. The pickup / felt belt 11 picks up the paper layer 14 formed by the first stock 10 from the belt 9 ′ while traveling clockwise, and thereafter,
From 3 ′, the paper layer 15 of the second stock 10 ′ is picked up in a form of being adhered to the paper layer 14. The wet paper web 16 composed of the paper layers 14 and 15 formed on the pickup / felt belt 11 is picked up by the felt belt 12 and then transferred to the surface of a drying cylinder (dryer) 17 to be heated and dried to be subjected to heat drying. It becomes a water disintegrated paper 1 having a structure and is wound up to form a roll 18. Such a series of papermaking steps may use well-known steps and equipment, and additional equipment other than the above may be added as appropriate. In the present invention, in the first raw material preparation step 2, the added amount of the paper strength enhancer is 5% or less based on the dry weight of the stock 10, and in the second preparation step 2 ', the added amount is 10 to 60%. As a result, the wet paper web 16 can be dried by bringing the paper layer 14 having a small amount of the paper strength enhancer into contact with the drying cylinder 17. After drying, the paper layer 14 containing at most 5% of the paper strength agent is easily peeled off from the drying cylinder 17.
【0012】図2は乾燥筒17の一部分Aの拡大側面図
であって、乾燥筒17に湿紙16の紙層14が接触して
いる状態を示している。ちなみに湿紙16の紙層15が
乾燥筒17に接触している場合には、乾燥の進行ととも
に紙層15が乾燥筒17に強く接着し、その後における
剥離が困難乃至不可能になることがある。FIG. 2 is an enlarged side view of a portion A of the drying cylinder 17 and shows a state in which the paper layer 14 of the wet paper 16 is in contact with the drying cylinder 17. Incidentally, when the paper layer 15 of the wet paper 16 is in contact with the drying cylinder 17, the paper layer 15 strongly adheres to the drying cylinder 17 as the drying proceeds, and the subsequent peeling may be difficult or impossible. .
【0013】図3は、本発明に係る水解紙の使用態様を
例示する水解紙30の側面の模式図である。図において
(A)は本発明に係る2枚の水解紙1を水解性のティシ
ュー紙33を介し、紙力増強剤を多く含む層35が最外
層となり、紙力増強剤の少ない層34が内側に向くよう
にしてエンボス加工により一体化させたものである。こ
のようにすると水解紙30は両最外層が薬液含浸強度の
高いものになる。図の(B)は(A)の水解紙30にク
レープ加工を施したもので、このようにすると比較的厚
手になりがちな水解紙30にしなやかな手触り感を与え
ることができる。FIG. 3 is a schematic side view of a water disintegration paper 30 illustrating the mode of use of the water disintegration paper according to the present invention. In the figure, (A) shows two sheets of hydrolyzed paper 1 according to the present invention interposed through a water-decomposable tissue paper 33, a layer 35 containing a large amount of paper strength enhancer becomes the outermost layer, and a layer 34 containing a small amount of paper strength enhancer inside. And integrated by embossing. In this way, the outermost layers of the water disintegrated paper 30 have a high chemical liquid impregnation strength. (B) of the figure is obtained by creping the hydrolyzed paper 30 of (A), and in this case, the hydrolyzed paper 30 that tends to be relatively thick can be given a soft touch.
【0014】次に上述の抄紙工程に実質的に匹敵する工
程でこの発明に係る多層構造の手漉き紙、及び比較例と
しての単層手漉き紙を製造し、それらの諸性質について
比較検討した結果を示す。 (実施例1) 置換度0.4、pH6のカルボキシメチル化パルプのナ
トリウム塩が30重量%及び針葉樹晒クラフトパルプが
70重量%の第1層と、同カルボキシメチル化パルプの
ナトリウム塩が5重量%及び針葉樹晒クラフトパルプが
95重量%の第2層とにより、第1層と第2層との重量
比率を1:1として坪量30g/m2の手漉き2層紙を
製造した。 (実施例2) 置換度0.4,pH6のカルボキシメチル化パルプのナ
トリウム塩とアルミニウム塩との混合物が60重量%及
び針葉樹晒クラフトパルプが40重量%の第1層と、針
葉樹晒クラフトパルプが100重量%の第2層とによ
り、坪量30g/m2の手漉き2層紙を製造した。 (実施例3) 水溶性ポリビニルアルコール繊維が25重量%及び針葉
樹晒クラフトパルプが75重量%の第1層を最外層の一
方とし、同水溶性ポリビニルアルコールが10重量%及
び針葉樹晒クラフトパルプが90重量%からなる第2層
を中間層とし、さらに同ポリビニルアルコール繊維が5
重量%及び針葉樹晒クラフトパルプが95重量%からな
る第3層を他方の最外層となるように、第1〜3層を順
に重ねて手漉きの多層紙を製造した。各層の重量比を
1:1:1として全体の坪量を30g/m2とした。 (比較例1) 実施例1と同じカルボキシメチル化パルプのナトリウム
塩が20重量%及び針葉樹晒クラフトパルプが80重量
%で坪量30g/m2の手漉き単層紙を製造した。 (比較例2) 実施例3と同じポリビニルアルコールが20重量%及び
針葉樹晒クラフトパルプが80重量%で、坪量30g/
m2の手漉き単層紙を製造した。実施例1〜3及び比較
例1〜2について薬液含浸による湿潤時の表面強度、水
解性(水分散性)及び抄紙性を評価した結果を表1に示
した。表1において実施例1〜3の多層紙が、比較例
4,5の単層紙と比較して表面強度に関してほぼ同等の
性能を示し、水解性(水分散性)と抄紙性とにおいてよ
り優れた性能を有することがわかる。Next, in a process substantially equivalent to the above-described papermaking process, a multi-layer handmade paper according to the present invention and a single-layer handmade paper as a comparative example were produced, and the results of comparative examination of various properties thereof were obtained. Show. (Example 1) First layer of 30% by weight of sodium salt of carboxymethylated pulp having substitution degree of 0.4 and pH 6 and 70% by weight of bleached softwood kraft pulp, and 5% by weight of sodium salt of the carboxymethylated pulp % And a second layer of bleached kraft pulp of 95% by weight, and a weight ratio of the first layer to the second layer of 1: 1 was used to produce a handmade two-layer paper having a basis weight of 30 g / m 2 . Example 2 A first layer of 60% by weight of a mixture of sodium salt and aluminum salt of carboxymethylated pulp having a substitution degree of 0.4 and pH 6 and 40% by weight of softwood bleached kraft pulp and softwood bleached kraft pulp A hand-made two-layer paper having a basis weight of 30 g / m 2 was produced with the second layer of 100% by weight. (Example 3) The first layer having 25% by weight of water-soluble polyvinyl alcohol fiber and 75% by weight of softwood bleached kraft pulp was used as one of the outermost layers. % Of the second alcohol layer as an intermediate layer, and
Hand-made multilayer paper was manufactured by sequentially stacking the first to third layers such that the third layer consisting of 95% by weight of bleached kraft pulp and 95% by weight of softwood bleach became the other outermost layer. The weight ratio of each layer was 1: 1: 1 and the total basis weight was 30 g / m 2 . (Comparative Example 1) was produced handsheets monolayer sheet of Example 1 of sodium salt of the same carboxymethylated pulp 20 wt and% and a basis weight of 30 g / m 2 softwood bleached kraft pulp 80% by weight. Comparative Example 2 The same polyvinyl alcohol as in Example 3 was 20% by weight and softwood bleached kraft pulp was 80% by weight, with a basis weight of 30 g /
It was produced handsheets monolayer sheet of m 2. Table 1 shows the results of evaluating the surface strength, water disintegration (water dispersibility), and papermaking properties of Examples 1 to 3 and Comparative Examples 1 and 2 when wet by impregnation with a chemical solution. In Table 1, the multilayer papers of Examples 1 to 3 show almost the same performance in terms of surface strength as compared with the single-layer papers of Comparative Examples 4 and 5, and are more excellent in water disintegration (water dispersibility) and papermaking properties. It can be seen that it has excellent performance.
【0015】なお各評価項目の評価方法は次のとおりで
ある。表面強度 (薬液含浸強度) 50%プロピレングリコール水溶液を試験紙重量の2倍
量含浸させた試験紙について、100g/cm2の押圧
力、5cm/sec速度で、約10cmの距離にわたり
平滑なABS樹脂シート表面を往復動作によりこすり、
試験紙が破れた時の往復回数により下記のように評価し
た。The evaluation method of each evaluation item is as follows. Surface strength (chemical solution impregnation strength) For a test paper impregnated with a 50% propylene glycol aqueous solution twice as much as the test paper weight, a pressing force of 100 g / cm 2, a speed of 5 cm / sec, and a smooth ABS resin over a distance of about 10 cm Rub the sheet surface by reciprocating motion,
Evaluation was made as follows by the number of reciprocations when the test paper was torn.
【0016】 A : 11回以上で破れる B : 4〜10回で破れる C : 3回以下で破れる水解性 (水分散性) 1lのビーカーに500mlの水道水を入れ、回転数5
00rpmのスタラーで撹拌しながら5×5cmの試験
紙を投入し、1分後の分散状態を下記のように評価し
た。A: Breaks 11 times or more B: Breaks 4 to 10 times C: Breaks 3 times or less Water dissolvability (water dispersibility) Put 500 ml of tap water into a 1 liter beaker, and rotate 5 times.
While stirring with a stirrer at 00 rpm, a test paper of 5 × 5 cm was charged, and the dispersion state after 1 minute was evaluated as follows.
【0017】 A : 繊維状に分散 B : 小さな繊維塊を伴う分散抄紙性 小型ロータリー乾燥機を使用し、試験紙の紙力増強剤が
少ない方の外層が乾燥機に接触するようにして、100
℃で約60秒間試験紙の湿紙を乾燥後、試験紙の乾燥機
からの剥離性を下記のように評価した。A: dispersed in fibrous form B: dispersed papermaking property with small fiber mass Using a small rotary dryer, the outer layer of the test paper having the smaller paper strength agent was brought into contact with the dryer by 100
After drying the wet paper of the test paper at about 60 ° C. for about 60 seconds, the releasability of the test paper from the dryer was evaluated as follows.
【0018】 A : 容易に剥離する B : やや接着ぎみであるが剥離する C : 剥離しないA: peels off easily B: peels slightly but slightly adheres C: does not peel
【0019】[0019]
【表1】 [Table 1]
【0020】[0020]
【効果】上述のようにして得られる水解紙であれば、相
対的に坪量が小さくそれゆえにしなやかで取扱い易い清
拭用紙が得られる。かかる清拭用紙は、一方の最外層に
おいて高い薬液含浸強度を有しながら、他方の最外層に
おいて優れた水解性を発揮し、それにより水解紙全体と
しても良好な水解性を有する。かかる水解紙は紙力増強
剤が相対的に少ない方の最外層を接触型乾燥機に接触さ
せれば、その製造が容易である。With the water-disintegrated paper obtained as described above, it is possible to obtain a wiping paper having a relatively small basis weight and being flexible and easy to handle. Such a wiping paper has a high chemical solution impregnation strength in one outermost layer, while exhibiting excellent water disintegration properties in the other outermost layer, thereby having good water disintegration properties as a whole. Such a water-disintegrated paper can be easily manufactured by bringing the outermost layer having a relatively small paper strength agent into contact with a contact dryer.
【図1】水解紙を製造する抄紙工程の概略図である。FIG. 1 is a schematic diagram of a paper making process for producing a hydrolyzed paper.
【図2】接触型乾燥機の表面と水解紙との位置関係を示
す模式的拡大図である。FIG. 2 is a schematic enlarged view showing a positional relationship between the surface of the contact dryer and water disintegration paper.
【図3】(A)、(B)いずれも水解紙の使用態様を例
示する側面図である。FIGS. 3A and 3B are side views exemplifying usage modes of hydrolyzed paper.
1 水解紙 14,15 最外層 16 湿紙 17 乾燥機 10,10’ 紙料 DESCRIPTION OF SYMBOLS 1 Hydrolysis paper 14,15 Outermost layer 16 Wet paper 17 Dryer 10,10 'Stock
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI D21H 27/00 D21H 27/00 E ──────────────────────────────────────────────────続 き Continued on front page (51) Int.Cl. 6 Identification code FI D21H 27/00 D21H 27/00 E
Claims (3)
であって、該水解紙の対向して位置する両最外層のうち
の一方の最外層が10〜60重量%の紙力増強剤を含
み、他方の最外層が5重量%以下の紙力増強剤含み、前
記紙力増強剤が、カルボキシメチル化パルプのナトリウ
ム塩、前記ナトリウム塩を含むカルボキシメチル化パル
プの混合塩、水溶性ポリビニルアルコール、水溶性ポリ
ビニルアルコール繊維、およびこれらの混合物のいずれ
かであることを特徴とする前記多層構造の水解紙。 1. A water disintegration paper having a multilayer structure comprising at least two layers, wherein the water disintegration paper includes two outermost layers which are opposed to each other.
While the outermost layer of comprises 10 to 60 wt% of a paper strength agent, seen including other outermost layer 5 wt% or less of a paper strength agent, before
The paper-enhancing agent is sodium carboxymethylated pulp.
Salt, carboxymethylated pal containing the sodium salt
Mixed salt, water-soluble polyvinyl alcohol, water-soluble poly
Any of vinyl alcohol fibers and their mixtures
The water-disintegrated paper having the multilayer structure as described above.
多層構造の水解紙の製造方法であって、乾燥重量におい
て10〜60重量%の紙力増強剤を含む第1紙料と、乾
燥重量において5重量%以下の紙力増強剤を含む第2紙
料とを、前記第1、第2紙料が前記湿紙の各々最外層を
構成するように多層抄きし、前記第2紙料からなる湿紙
の最外層を前記接触型乾燥機に対する接触面として乾燥
することにより、前記第1、第2紙料が前記水解紙の各
々の最外層を構成することを特徴とする前記水解紙の製
造方法。 2. A method for producing a multi-layer hydrolyzed paper comprising a wet paper web drying step using a contact dryer, comprising: a first stock containing 10 to 60% by weight of a paper strength agent in a dry weight; A second paper stock containing 5% by weight or less of a paper strength agent on a dry weight basis, making the first and second paper stocks each form an outermost layer of the wet paper; By drying the outermost layer of wet paper made of paper stock as a contact surface to the contact type dryer, the first and second stocks constitute the respective outermost layers of the hydrolyzed paper. Water disintegration paper manufacturing method.
プのナトリウム塩、前記ナトリウム塩を含むカルボキシ
メチル化パルプの混合塩、水溶性ポリビニルアルコー
ル、水溶性ポリビニルアルコール繊維、およびこれらの
混合物のいずれかであることを特徴とする請求項2記載
の水解紙の製造方法。 3. The paper strength-enhancing agent is a sodium salt of carboxymethylated pulp;
The method for producing hydrolyzed paper according to claim 2, wherein the mixed paper is any one of a mixed salt of methylated pulp, water-soluble polyvinyl alcohol, water-soluble polyvinyl alcohol fiber, and a mixture thereof.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16760291A JP2931130B2 (en) | 1991-06-12 | 1991-06-12 | Multilayered hydrolyzed paper and method for producing the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16760291A JP2931130B2 (en) | 1991-06-12 | 1991-06-12 | Multilayered hydrolyzed paper and method for producing the same |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04370300A JPH04370300A (en) | 1992-12-22 |
JP2931130B2 true JP2931130B2 (en) | 1999-08-09 |
Family
ID=15852816
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16760291A Expired - Lifetime JP2931130B2 (en) | 1991-06-12 | 1991-06-12 | Multilayered hydrolyzed paper and method for producing the same |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2931130B2 (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SG64435A1 (en) * | 1996-09-27 | 1999-04-27 | Uni Charm Corp | Disposable wiper sheet and method for producing the same |
CA2819862A1 (en) | 2010-12-10 | 2012-06-14 | H.B. Fuller Company | Flushable article including polyurethane binder and method of using the same |
EP3540121A4 (en) | 2016-11-09 | 2020-05-27 | Nippon Paper Papylia Co., Ltd. | Water dispersing sheet |
WO2019049619A1 (en) | 2017-09-05 | 2019-03-14 | 日本製紙パピリア株式会社 | Water-dispersible sheet |
JP7038582B2 (en) * | 2018-03-30 | 2022-03-18 | 大王製紙株式会社 | Hydrolyzable sheet and laminate of hydrolyzable sheet |
CN111663367A (en) * | 2019-03-08 | 2020-09-15 | 天津大学 | Manufacturing method for clean production of pulping and papermaking based on CMC-NA liquid system |
-
1991
- 1991-06-12 JP JP16760291A patent/JP2931130B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH04370300A (en) | 1992-12-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR100665072B1 (en) | Water-decomposable fibrous sheet of high resistance to surface friction, and method for producing it | |
TW440641B (en) | Paper products and methods for applying chemical additives to cellulosic fibers | |
JP4733070B2 (en) | Water-degradable article | |
JP6211160B1 (en) | Water disintegratable sheet | |
US6379498B1 (en) | Method for adding an adsorbable chemical additive to pulp during the pulp processing and products made by said method | |
JP4753738B2 (en) | Bulky cleaning article and manufacturing method thereof | |
KR19990030092A (en) | Hydrolyzable fibrous sheet and sheet for wiping in overlapping form | |
PL178164B1 (en) | Method of making soft handkerchiefs | |
HUT78000A (en) | Tissue paper product comprising a quaternary ammonium compound, a polysiloxane compound and binder materials | |
JP2001288657A (en) | Water-disintegrable fiber sheet having multilayered structure | |
SE1251427A1 (en) | Wet-laid sheet material of a microfibrillated material composition | |
KR19990029627A (en) | Hydrolyzable fiber sheet containing fibers of different lengths | |
JP2002339218A (en) | Water-disintegrable sheet and method of production for the same | |
AU2001239938A1 (en) | Method for adding an adsorbable chemical additive to pulp during the pulp processing and products made by said method | |
EP0342646A2 (en) | Hand or wiper towel | |
JP6346969B1 (en) | Water-decomposable sheet and method for producing the water-decomposable sheet | |
JPH11206611A (en) | Hydrolytic tissue | |
JP4219323B2 (en) | Manufacturing method of water-disintegrating paper | |
JP2931130B2 (en) | Multilayered hydrolyzed paper and method for producing the same | |
JPH0327194A (en) | Laminar two-ply tissue and its manufacture | |
JPH07216781A (en) | Wipe paper | |
JP4315893B2 (en) | Bulky water degradable cleaning article | |
JP4619110B2 (en) | Method for producing hydrolyzed paper and method for producing hydrolyzable wiping article | |
JP6474923B2 (en) | Method for producing water-degradable sheet | |
JP2006150695A (en) | Method for producing hydrolysis paper |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 19990507 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090521 Year of fee payment: 10 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090521 Year of fee payment: 10 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100521 Year of fee payment: 11 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110521 Year of fee payment: 12 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110521 Year of fee payment: 12 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120521 Year of fee payment: 13 |
|
EXPY | Cancellation because of completion of term | ||
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120521 Year of fee payment: 13 |