JPH04370300A - Water-disaggregative paper with multilayer structure and production thereof - Google Patents

Water-disaggregative paper with multilayer structure and production thereof

Info

Publication number
JPH04370300A
JPH04370300A JP16760291A JP16760291A JPH04370300A JP H04370300 A JPH04370300 A JP H04370300A JP 16760291 A JP16760291 A JP 16760291A JP 16760291 A JP16760291 A JP 16760291A JP H04370300 A JPH04370300 A JP H04370300A
Authority
JP
Japan
Prior art keywords
paper
water
disintegratable
salt
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.)
Granted
Application number
JP16760291A
Other languages
Japanese (ja)
Other versions
JP2931130B2 (en
Inventor
Naoto Takeuchi
直人 竹内
Kazuya Okada
和也 岡田
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.)
Unicharm Corp
Original Assignee
Unicharm Corp
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 Unicharm Corp filed Critical Unicharm Corp
Priority to JP16760291A priority Critical patent/JP2931130B2/en
Publication of JPH04370300A publication Critical patent/JPH04370300A/en
Application granted granted Critical
Publication of JP2931130B2 publication Critical patent/JP2931130B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To obtain the title paper with high mechanical strength after chemical impregnation, excellent in water disaggregation and productivity, useful as e.g. cleansing tissues, by putting two kinds of paper stock each containing specified amount of a paper strengthening agent to multilayer papermaking process so that said two kinds of paper stock make up the respective outermost layers followed by drying. CONSTITUTION:(A) The first paper stock 10 containing 10-60wt.%, on a dry basis, of a paper strengthening agent, i.e., carboxymethylated pulp salt, water-soluble PVA, water-soluble PVA fibers or a mixture thereof, and (B) the second paper stock 10' containing <=5wt.%, on a dry basis, of such agent, are put to multilayer papermaking process so that the above two kinds of paper stock 10, 10' make up the respective outermost layers 14,15 of a wet paper 16, and the outermost layer 14 consisting of the second paper stock 10' is dried as the contact surface for a contact-type dryer 17, thus obtaining the objective water-disaggregative paper 1. It is preferable that said carboxymethylated pulp salt be a sodium salt or mixed salt containing the same with the substitution degree of 0.2-0.6.

Description

【発明の詳細な説明】[Detailed description of the invention]

【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 This invention relates to water-disintegrable paper having a multilayer structure, which has high strength when impregnated with a chemical solution such as alcohol, and has excellent water-disintegrability.

【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。
BACKGROUND OF THE INVENTION Water-disintegrable paper and quick-dissolve paper, which are cleaning paper impregnated with a cleaning alcohol or the like, and whose constituent fibers are quickly dispersed in water when the paper is thrown into water, are well known. For example, Japanese Patent Publication No. 42-2925 discloses a method for continuously producing fast-dissolving detergent-containing washing paper, decorative paper, etc. by etherifying continuous paper made essentially of cellulose in its paper form. There is. According to this technology, commercially available paper can be suitably and rapidly dissolved. Furthermore, JP-A-1-168999 discloses a technique for obtaining water-disintegrable paper that is easily water-dispersible and has high strength when impregnated with a chemical solution by mixing water-dispersible papermaking fibers and water-insoluble carboxymethylated pulp. are 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。
[Problems to be Solved by the Invention] According to each of the above-mentioned techniques, a detergent, disinfectant, or other chemical solution provided by the present invention is impregnated and used. For example, it is possible to obtain water-disintegrable paper for cleaning paper such as hand towels.

【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. 42-2925 requires foldable continuous paper, and furthermore, it is necessary to unroll the continuous paper and etherify it, so the continuous paper that can be used for this purpose is comparatively difficult. It is a paper with a large basis weight. In other words, there is a problem in that it is difficult to produce water-disintegratable paper with a relatively small basis weight, for example, about 10 to 50 g/m2. Furthermore, the technique disclosed in Japanese Patent Application Laid-open No. 1-168999 involves making paper from a paper stock mixed with a large amount of water-insoluble carboxymethylated pulp as a paper strength enhancer. When such a paper stock is used in a contact dryer in the dry part of the papermaking process, as drying progresses, the contact surface strongly adheres to the dryer, making it difficult to separate. Therefore, this technique has a problem in 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。
[0005] Therefore, the present invention comprises a water-disintegratable paper with at least two layers, one of the two opposing outermost layers of the water-disintegratable paper contains a relatively large amount of paper strength enhancer, and the other outermost layer contains a paper strength enhancer in a relatively large amount. This problem is attempted to be solved by including a relatively small amount of 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。
[Means for Solving the Problems] The gist of the present invention for solving 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
力増強剤を含むことがその要旨である。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 provision of a multi-layered water-disintegratable paper and a method for producing the same, and the water-disintegratable paper has a multi-layer structure consisting of at least two layers, and the two outermost layers of the water-disintegratable paper are located opposite to each other. One of the outermost layers is 10 to 60% by weight.
The gist is that the other outermost layer contains 5% by weight or less of a paper strength enhancer. Further, the method for producing a multilayered water-disintegratable paper includes a step of drying a wet paper using a contact dryer, and the method includes a paper strength enhancer in an amount of 10 to 60% by weight on a dry weight basis. 1st
At least a paper stock and a second paper stock containing 5% by weight or less of a paper strength agent are used. After obtaining a wet paper with a multilayer structure such that each stock constitutes the outermost layer of each of the wet paper webs, the outermost layer of the wet paper made of the second paper stock is used as a contact surface for the contact dryer to dry. The gist is that the first and second stock constitute the outermost layer of each of the water-disintegratable papers.

【0008】好ましい実施態様においては前記紙力増強
剤がいずれの場合においてもカルボキシメチル化パルプ
の塩、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、またはこれらの混合物であり、さらに
は前記カルボキシメチル化パルプの塩にはナトリウム塩
またはナトリウム塩を含む混合塩を使用する。
In a preferred embodiment, the paper strength agent is in each case a salt of carboxymethylated pulp, water-soluble polyvinyl alcohol, water-soluble polyvinyl alcohol fiber, or a mixture thereof; To salt the pulp, use sodium salts or mixed salts containing sodium salts.

【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。
[Function] In the water-disintegratable paper according to the present invention constructed as described above, the outermost layer containing a high content of paper strength enhancer exhibits excellent surface strength even when impregnated with a chemical solution, and does not tear easily. This outermost layer is suitable for use exclusively as a wiping surface. The other outermost layer has a low content of paper strength agents, containing at most 5%. Therefore, this layer quickly disperses in water, and is good for water-disintegratable paper, even though the outermost layer tends to reduce the water-disintegratability of water-disintegratable paper due to the influence of high content of paper strength enhancer. Provides water degradability. Furthermore, in the water-disintegratable paper having such a structure, the outermost layer containing a low content of paper strength enhancer can be used as a contact surface for a contact dryer during the paper-making process. This contact surface is extremely easily peeled off from the dryer after drying, so that the productivity of the water-disintegratable paper is not reduced even though one of the outermost layers contains a large amount of 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 explained 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13’
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1
7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 the paper-making process of water-disintegratable paper 1 according to the present invention. The process includes at least two lines of first and second raw material preparation processes 2 and 2', one short screen wire 9 and one circular screen paper machine 13, a pickup felt belt 11, a felt belt 12, a drying cylinder 17, etc. . In each raw material preparation process 2, 2', first and second disintegrating tanks 4, 4', sizing agents, paper strength enhancers, etc. are mixed with the raw material pulp to prepare first and second paper stock 10, 10'. It includes first and second blending tanks 5, 5', which are connected by transfer pipes 6, 6'. The first mixing tank 5 is a head box 7
The head box 7 faces above the belt 9' at one end of the wire part 9 consisting of an endless wire mesh belt 9', and supplies the stock 10 therein. The belt 9' runs counterclockwise in FIG. 1, and the other end of the wire part 9 contacts an endless pick-up felt belt 11. This belt 11 runs clockwise. On the other hand, the second blending tank 5' is connected to the circular mesh paper machine 13, and supplies the stock 10' to the filter tank 12. In the circular screen paper machine 13, a portion of the circular screen 13' is immersed in the paper stock 10', and its top is in contact with the pick-up felt belt 11. While traveling clockwise, the pickup felt belt 11 first picks up the paper layer 14 formed by the first stock 10 from the belt 9', and then picks up the paper layer 14 formed by the first stock 10, and then picks up the paper layer 14 formed by the first stock 10 from the belt 9'.
A paper layer 15 made of the second paper stock 10' is picked up from the paper layer 14 in a manner that it adheres to the paper layer 14. The wet paper web 16 consisting 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 dryer 17 where it is heated and dried to form two layers. The structured water-disintegratable paper 1 is rolled up and
This results in a roll of 18. Such a series of papermaking processes can be performed using well-known processes and equipment, and incidental equipment other than those described above may be added as appropriate. In this invention, in the first raw material preparation step 2, the amount of paper strength enhancer added is
The amount added is 5% or less on a dry weight basis, and in the second preparation step 2', the amount added is 10 to 60%. As a result, the wet paper 16 has a paper layer 14 containing a small amount of paper strength enhancer added to the drying tube 1.
It can be dried by contacting it with water. After drying, the paper layer 14 containing at most 5% paper strength agent is easily peeled off from the drying tube 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, showing a state in which the paper layer 14 of the wet paper web 16 is in contact with the drying cylinder 17. Incidentally, if the paper layer 15 of the wet paper web 16 is in contact with the drying cylinder 17, as the drying progresses, the paper layer 15 will strongly adhere to the drying cylinder 17, and subsequent peeling may become 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-disintegratable paper 30 illustrating a usage mode of the water-disintegratable paper according to the present invention. In the figure (A), two sheets of water-disintegratable paper 1 according to the present invention are interposed between water-disintegratable tissue paper 33, the layer 35 containing a large amount of paper strength enhancer is the outermost layer, and the layer 34 containing less paper strength enhancer is the inner layer. It is integrated by embossing so that it faces towards the surface. In this way, both the outermost layers of the water-disintegratable paper 30 have high chemical solution impregnation strength. (B) in the figure shows the water-disintegratable paper 30 of (A) subjected to crepe processing, and by doing so, it is possible to give a supple feel to the water-disintegratable paper 30, which tends to be relatively thick.

【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、第1層と第2層との重量比率を:1とし
て坪量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2
0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, the multilayered handmade paper according to the present invention and a single layered handmade paper as a comparative example were produced in a process substantially comparable to the papermaking process described above, and the results of a comparative study of their properties are as follows. show. (Example 1) A first layer containing 30% by weight of sodium salt of carboxymethylated pulp with a degree of substitution of 0.4 and pH 6 and 70% by weight of bleached softwood kraft pulp, and 5% by weight of sodium salt of the same carboxymethylated pulp. % and a second layer containing 95% by weight of softwood bleached kraft pulp, a handmade two-layer paper with a basis weight of 30 g/m2 was produced with a weight ratio of the first layer and the second layer of 1:1. (Example 2) A first layer containing 60% by weight of a mixture of sodium salt and aluminum salt of carboxymethylated pulp with a degree of substitution of 0.4 and a pH of 6 and 40% by weight of bleached softwood kraft pulp, and a bleached softwood kraft pulp. A handmade two-layer paper with a basis weight of 30 g/m2 was produced by setting the weight ratio of the first layer and the second layer to 1:1. (Example 3) The first layer containing 25% by weight of water-soluble polyvinyl alcohol fibers and 75% by weight of bleached softwood kraft pulp was one of the outermost layers, and 10% by weight of the water-soluble polyvinyl alcohol fibers and 90% by weight of bleached softwood kraft pulp. A second layer consisting of 5% by weight of the same polyvinyl alcohol fiber and 95% by weight of softwood bleached kraft pulp is used as an intermediate layer.
A handmade multilayer paper was manufactured by stacking the first to third layers in order such that the third layer consisting of % by weight was the other outermost layer. The weight ratio of each layer is 1:1:1, and the overall basis weight is 30g/m2
And so. (Comparative Example 1) A handmade single-layer paper with a basis weight of 30 g/m 2 was produced using the same sodium salt of carboxymethylated pulp as in Example 1 at 20% by weight and bleached softwood kraft pulp at 80% by weight. (Comparative Example 2) The same polyvinyl alcohol as in Example 3 was
0% by weight and 80% by weight of softwood bleached kraft pulp,
A handmade single-layer paper with a basis weight of 30 g/m2 was produced. Example 1
Table 1 shows the results of evaluating the surface strength, water disintegrability (water dispersibility), and paper-making property when wetted by chemical impregnation for Comparative Examples 1 and 3 and Comparative Examples 1 and 2. Table 1 shows that the multilayer papers of Examples 1 to 3 exhibited almost the same performance in surface strength as the single-layer papers of Comparative Examples 4 and 5, and were superior in water disintegration (water dispersibility) and paper-making 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 for each evaluation item is as follows. Surface strength (chemical impregnation strength) For a test paper impregnated with 50% propylene glycol aqueous solution in an amount twice the weight of the test paper, a smooth ABS resin sheet was applied over a distance of approximately 10 cm at a pressing force of 100 g/cm2 and a speed of 5 cm/sec. Scrub the surface in a reciprocating motion,
Evaluation was made as follows based on 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 after 11 times or more B:
Breaks in 4 to 10 times C: Water disintegrability (water dispersibility) breaks in 3 times or less Pour 500 ml of tap water into a 1 liter beaker and rotate at 5 rotations.
A 5 x 5 cm test paper was added while stirring with a stirrer at 00 rpm, 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: Dispersion in the form of fibers B: Dispersion paper making with small fiber agglomerates Using a small rotary dryer, the outer layer of the test paper with less paper strength agent is in contact with the dryer.
After drying the wet paper of the test paper at a temperature of about 60 seconds, the peelability 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: Easily peeled off B:
Slightly adheres but peels off C: Does not peel off

【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。
[Effect] The water-disintegratable paper obtained as described above has a relatively small basis weight, and therefore, a wiping paper that is pliable and easy to handle can be obtained. Such wiping paper has high chemical impregnation strength in one outermost layer while exhibiting excellent water-disintegrability in the other outermost layer, and as a result, the water-disintegratable paper as a whole has good water-disintegrability. Such water-disintegratable paper can be easily produced by bringing the outermost layer containing relatively less paper strength enhancer into contact with a contact dryer.

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

【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 papermaking process for producing water-disintegratable 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 the positional relationship between the surface of the contact dryer and water-disintegratable 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 illustrating how water-disintegratable paper is used.

【符号の説明】[Explanation of symbols]

1            水解紙 14,15    最外層 16          湿紙 17          乾燥機 10,10’  紙料 1 Water-dissolving paper 14,15 Outermost layer 16 Wet paper 17 Dryer 10,10’ Paper stock

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】少なくとも2層からなる多層構造の水解紙
であって、該水解紙の対向して位置する両最外層のうち
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むことを特
徴とする前記多層構造の水解紙。
Claim 1: A water-disintegratable paper having a multilayer structure consisting of at least two layers, wherein one of the two opposing outermost layers of the water-disintegratable paper contains 10 to 60% by weight of a paper strength enhancer. ,
The water-disintegratable paper having a multilayer structure as described above, wherein the other outermost layer contains 5% by weight or less of a paper strength enhancer.
【請求項2】前記紙力増強剤がカルボキシメチル化パル
プの塩、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、またはこれらの混合物であることを
特徴とする請求項1記載の水解紙。
2. The water-disintegratable paper according to claim 1, wherein the paper strength enhancer is a salt of carboxymethylated pulp, water-soluble polyvinyl alcohol, water-soluble polyvinyl alcohol fiber, or a mixture thereof.
【請求項3】前記カルボキシメチル化パルプの塩がナト
リウム塩またはナトリウム塩を含む混合塩であり、かつ
それらの置換度が0.2〜0.6であることを特徴とす
る請求項2記載の水解紙。
3. The carboxymethylated pulp salt according to claim 2, wherein the salt of the carboxymethylated pulp is a sodium salt or a mixed salt containing a sodium salt, and the degree of substitution thereof is from 0.2 to 0.6. Water-decomposable paper.
【請求項4】接触型乾燥機による湿紙の乾燥工程を含む
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、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。
4. A method for producing a multilayered water-disintegratable paper comprising a step of drying a wet paper paper using a contact dryer, the first stock containing a paper strength enhancer in an amount of 10 to 60% by weight on a dry basis; A second paper stock containing a paper strength enhancer of 5% by weight or less on dry weight is multi-layered so that the first and second paper stocks each constitute the outermost layer of the wet paper web, and the second paper stock is The first and second paper stocks constitute the outermost layer of each of the water-disintegratable paper by drying the wet paper web made of paper stock as the contact surface for the contact dryer. A method for producing water-disintegratable paper.
【請求項5】前記紙力増強剤がカルボキシメチル化パル
プの塩、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、またはこれらの混合物であることを
特徴とする請求項4記載の水解紙の製造方法。
5. The method for producing water-disintegratable paper according to claim 4, wherein the paper strength enhancer is a salt of carboxymethylated pulp, water-soluble polyvinyl alcohol, water-soluble polyvinyl alcohol fiber, or a mixture thereof. .
【請求項6】前記カルボキシメチル化パルプの塩がナト
リウム塩またはナトリウム塩を含む混合塩であり、かつ
それらの置換度が0.2〜0.6であることを特徴とす
る請求項5記載の水解紙の製造方法。
6. The carboxymethylated pulp salt according to claim 5, wherein the salt of the carboxymethylated pulp is a sodium salt or a mixed salt containing a sodium salt, and the degree of substitution thereof is from 0.2 to 0.6. A method for producing water-disintegratable paper.
JP16760291A 1991-06-12 1991-06-12 Multilayered hydrolyzed paper and method for producing the same Expired - Lifetime JP2931130B2 (en)

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 true JPH04370300A (en) 1992-12-22
JP2931130B2 JP2931130B2 (en) 1999-08-09

Family

ID=15852816

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Country Link
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100559111B1 (en) * 1996-09-27 2006-06-29 유니챰 가부시키가이샤 Wiper Sheet and Manufacturing Method
US8821687B2 (en) 2010-12-10 2014-09-02 H.B. Fuller Company Flushable article including polyurethane binder and method of using the same
WO2018088179A1 (en) 2016-11-09 2018-05-17 日本製紙パピリア株式会社 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
JP2019178446A (en) * 2018-03-30 2019-10-17 大王製紙株式会社 Water-disintegrable sheet and water-disintegrable sheet laminate body
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

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100559111B1 (en) * 1996-09-27 2006-06-29 유니챰 가부시키가이샤 Wiper Sheet and Manufacturing Method
US8821687B2 (en) 2010-12-10 2014-09-02 H.B. Fuller Company Flushable article including polyurethane binder and method of using the same
WO2018088179A1 (en) 2016-11-09 2018-05-17 日本製紙パピリア株式会社 Water dispersing sheet
US11052694B2 (en) 2016-11-09 2021-07-06 Nippon Paper Papylia Co., Ltd Water-dispersible sheet
WO2019049619A1 (en) 2017-09-05 2019-03-14 日本製紙パピリア株式会社 Water-dispersible sheet
JP2019178446A (en) * 2018-03-30 2019-10-17 大王製紙株式会社 Water-disintegrable sheet and water-disintegrable sheet laminate body
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

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