JPH0311831B2 - - Google Patents
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- JPH0311831B2 JPH0311831B2 JP24535083A JP24535083A JPH0311831B2 JP H0311831 B2 JPH0311831 B2 JP H0311831B2 JP 24535083 A JP24535083 A JP 24535083A JP 24535083 A JP24535083 A JP 24535083A JP H0311831 B2 JPH0311831 B2 JP H0311831B2
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- Prior art keywords
- water
- soluble
- acid
- base
- solid acid
- Prior art date
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Description
本発明は、塩基中和能力を有する水溶性シート
に関する。さらに詳しくは、本発明は、繊維状カ
ルボキシメチルセルロースから成る水溶性基材を
特定の酸に含浸もしくは塗布して成る水溶性シー
トであつて、塩基中和能力と保水性との二機能を
具備した水溶性シートに関する。
従来、繊維状カルボキシメチルセルロース(以
下、CMC−Naという)から成る水溶紙が機密文
書用紙、ラベル等の筆記、印刷用に、また使用後
に溶解流去させる産業用資材として、さらに婦
人、乳幼児の衛材用として用いられている。他
方、アルカリ液を使用する各種の産業用機器分
野、フアインケミカル工業分野等においては、使
用ずみのアルカリ液を自動的に中和し、保持する
プロセスコントロール材が要望されている。この
ため、特殊な中和タイミング層ポリマーが開発さ
れているが、製造が難かしく、価格の高いものと
なつていた。また、いわゆる吸水性樹脂の使用も
考えられるが、中和能力がないので上記要望を完
全には満たすものではなかつた。
本発明者は、上記プロセスコントロール材の具
備すべき特性が(イ)吸水性と保水性を有すること、
(ロ)アルカリ中和能力を有すること、(ハ)アルカリ中
和後も適当な保水性を有すること、等である点に
着目し、先ず水溶紙をプロセスコントロール材の
基材とすることの可能性について検討した。その
結果、水溶紙は、吸水量、保水量とも自重の50倍
以上であり、(イ)の条件を十分に満たすので、プロ
セスコントロール材の基材とし得る資質を有する
ことが判明した。そこで、本発明者は水溶紙を基
材として、これに酸を含浸させることによつて(ロ)
と(ハ)の特性を具備したプロセスコントロール材を
得ることを目的として鋭意研究を重ねた結果、含
浸すべき酸を特定すること、および含浸工程に一
定の条件を付することにより、(イ),(ロ),(ハ)の諸特
性をすべて具備したプロセスコントロール材が得
られることを見出し、本発明に到達した。
従来の水溶紙は、特公昭48−27605号に開示さ
れている如く、繊維状セルロースグリコール酸
(以下、CMC−Hという)を抄紙し、プレスパー
ト以降の湿紙匹に炭酸ソーダ、苛性ソーダなどの
アルカリ液を塗布含浸し、イオン交換してナトリ
ウム塩(CMC−Na)とした後、脱水し乾燥して
製造される。そして、その塩基飽和度は通常100
%である。また、吸水性、保水性についていえ
ば、たとえばエーテル化度0.43のCMC−H(ニチ
リン化学製)を100%用いて抄造した秤量約
80g/m2の水溶紙の吸水量は77g/g、保水量は
52g/gと高く、保水量と吸水量の比率は67.5%
である。そして、水中での溶解過程は膨潤を経て
溶解するものであり、その膨潤度を本発明におい
ては保水量を以て示す。しかし、酸の含浸によつ
てCMC−NaのNa+イオンがH+イオンによつて
置換されるに従つて塩基飽和度が低下し、溶解状
態がコロイド状から繊維状ゲルの分散した状態へ
と変化する。そして、保水量も次第に小さくな
る。CMC−Naが完全にH+イオンによつて置換
されると、CMC−Hの塩基飽和度は0%となる
とともに水に不溶となり、保水量は自重の1〜2
倍まで低下する。即ち本発明水溶性シートが具備
すべき所定の保水量は水溶性という資質に従属す
るものである。ここで水溶性とは、通常、後述の
試験法による溶解液を肉眼で観察した場合にコロ
イド状を示す状態をいうが、繊維状ゲルが分散さ
れた状態であつてもよい。
水溶紙に含浸または塗布すべき酸は、水溶性を
妨げないことが必要で、換言すれば、含浸または
塗布に際してCMC−Naの塩基飽和度を一定水準
以上に維持しうる程度の弱酸でなければならな
い。塩基飽和度が低下するに従つて溶解時間が長
くなり遂には難溶性、不溶性となつて所定の保水
量を維持できなくなるからである。本発明では所
定の保水量を8g/g以上とし、これを維持し得
る塩基飽和度を40%以上とする。
本発明において、選択使用する酸の指標として
水中酸指数(pKa)を用いる。ここで水中酸指数
とは、電解質の水中における解離定数の逆数の対
数である。水中酸指数が高い酸ほど酸の強さは弱
く、CMC−Naの塩基飽和度は低下しにくい。本
発明では水中酸指数(以下、酸指数という)が
3.8以上の酸を用いる。また本発明水溶性シート
の構成材料たる酸は、前述の要件を満たすもので
あつても事実上潮解性があつてはならない。基材
たる水溶紙がCMC−Naから成るためその平衡水
分は約16%(20℃,65%RH)と高いので、成紙
中の水分を増加し、その結果互いに反応して塩基
飽和度を低下させるおそれがあるからである。従
つて、常温で固体であり事実上潮解性のない酸を
用いることが必要であり、また、これにより
CMC−Naが被覆され吸湿が抑制されることが望
ましい。
本発明水溶性シートは、水溶紙を基材として、
たとえば有機溶媒もしくは有機溶媒と水との混合
溶媒に前記特定の固体酸を溶解した溶液に該水溶
紙を含浸し、含浸工程においては前記した塩基飽
和度を一定水準以上に維持しつつ所定量の固体酸
を付着させ乾燥して製造される。滲透した酸は水
溶紙の網目状空隙を満たし一体となつている。そ
してこれを使用目的に応じた大きさ、形状に加工
してプロセスコントロール材として用いるとき
は、工程に発生したアルカリ液を吸収、保水しつ
つ自動的に中和するから、プロセスコントロール
材が外圧をうけない限り、崩壊せずに形態が保た
れ、他の工程を汚染するおそれがない。
かくして本発明によれば、繊維状カルボキシメ
チルセルロースもしくは繊維状カルボキシメチル
セルロースと製紙用繊維とから成る水溶性マトリ
ツクスに水溶性固体酸もしくは水溶性固体酸と水
溶性バインダーとが含浸もしくは塗布されて成る
ことを特徴とする塩基中和能力を有する水溶性シ
ートおよびその製造法が提供される。
以下に、本発明の構成を実験例を参照しつつ詳
細に設明する。
実験例 1
エタノール−水(1:1重量部)混合溶媒を用
い、酢酸(pKa4.756)の濃度を変えて基材を処
理し、塩基飽和度と酸処理紙の水溶性および保水
量との関係を調べて、第1表および第1図に示し
た。液体酸である酢酸を用いたのは、塩基飽和度
および保水量の測定が容易だからである。
基材としては、繊維状CMC−H(エーテル化度
0.43、ニチリン化学製)100%を用いて抄紙し、
炭酸ソーダ液を添加して製造した秤量80g/m2の
水溶紙を用いた。酸処理は各濃度の酢酸溶液50ml
に試料絶乾1gを浸し2時間撹拌した後別し、
残渣を常法により洗浄して残留する酢酸を除去し
た後、60℃で減圧乾燥した。
塩基交換容量および塩基飽和度の測定は次の如
く行なつた。
無処理水溶紙および前記の酸処理試料をそれぞ
れ絶乾0.5g採り、これに0.5N苛性ソーダ20mlを加
え、2時間撹拌後、純水10mlを加え、0.5N塩酸
で電位差滴定し、この滴定値をAmlとした。ブラ
ンク試験として、試料を用いずに同様の操作を行
ない、この滴定値をBmlとした。
塩基交換溶量および塩基飽和度は、次式で求め
た。
塩基交換容量(mg当量/g)=
(B−A)×0.5×f/1000
×1/W×1000
f:0.5N HClのフアクター
W:試料絶乾重量(g)
塩基飽和度(%)=塩基交換容量−交換性H+量/塩基
交換容量×100=交換性塩基量/交換性塩基量+交換性H
+量×100
水溶性は約1gの試験片を300mlの水中に投入
し、マグネチツクスターラーで回転させ、試験片
が溶解するまでの秒数を測定した。120秒経過し
ても繊維の小塊が残るものを難溶とし、シート形
態が崩れないものを不溶とした。
保水量は、絶乾試料1gを水200ml中に入れて30
秒間撹拌した後、重量既知のポリエステル製布袋
に移し、遠心分離機により770Gで1分間脱水した
あとの重量を求め、絶乾試料1gあたりの重量で
あらわした。
The present invention relates to a water-soluble sheet having base neutralization ability. More specifically, the present invention is a water-soluble sheet made by impregnating or coating a water-soluble base material made of fibrous carboxymethyl cellulose with a specific acid, which has dual functions of base neutralization ability and water retention ability. Regarding water-soluble sheets. Conventionally, water-soluble paper made of fibrous carboxymethyl cellulose (hereinafter referred to as CMC-Na) has been used for writing and printing confidential documents, labels, etc., and as an industrial material that is dissolved and washed away after use, as well as for the hygiene of women and infants. It is used for lumber. On the other hand, in the fields of various industrial equipment, fine chemical industry, etc. that use alkaline liquid, there is a need for a process control material that automatically neutralizes and retains used alkaline liquid. For this reason, special neutralized timing layer polymers have been developed, but they have been difficult to manufacture and expensive. It is also possible to use so-called water-absorbing resins, but they do not have neutralizing ability and therefore do not completely satisfy the above requirements. The present inventor believes that the characteristics that the process control material should have are (a) water absorption and water retention;
Focusing on the following points: (b) it has alkali neutralization ability, and (c) it has appropriate water retention even after alkali neutralization, it is possible to use water-soluble paper as a base material for process control materials. We considered gender. As a result, the water-soluble paper was found to have the ability to be used as a base material for process control materials, since both the amount of water absorbed and the amount of water retained were more than 50 times its own weight, fully satisfying the condition (a). Therefore, the present inventor used water-soluble paper as a base material and impregnated it with acid (B).
As a result of extensive research aimed at obtaining a process control material with the characteristics of The inventors have discovered that it is possible to obtain a process control material that has all of the characteristics of , (b), and (c), and have arrived at the present invention. Conventional water-soluble paper, as disclosed in Japanese Patent Publication No. 48-27605, is made from fibrous cellulose glycolic acid (hereinafter referred to as CMC-H), and the wet paper after the press part is coated with soda carbonate, caustic soda, etc. It is manufactured by coating and impregnating an alkaline solution, ion-exchanging it to make sodium salt (CMC-Na), dehydrating it, and drying it. And its base saturation is usually 100
%. In addition, regarding water absorption and water retention, for example, a paper made using 100% CMC-H (manufactured by Nichirin Chemical Co., Ltd.) with a degree of etherification of 0.43 has a weight of approx.
The water absorption amount of 80g/ m2 water-soluble paper is 77g/g, and the water retention amount is
High at 52g/g, the ratio of water retention and water absorption is 67.5%
It is. The dissolution process in water involves swelling and dissolution, and the degree of swelling is indicated by the amount of water retained in the present invention. However, as the Na + ions in CMC-Na are replaced by H + ions due to acid impregnation, the base saturation decreases and the dissolution state changes from a colloidal state to a dispersed state of a fibrous gel. Change. The amount of water retained also gradually decreases. When CMC-Na is completely replaced by H + ions, the base saturation of CMC-H becomes 0% and it becomes insoluble in water, with a water retention capacity of 1 to 2 of its own weight.
It decreases to twice as much. That is, the predetermined water retention amount that the water-soluble sheet of the present invention should have depends on its water-soluble property. Here, water-soluble usually refers to a state in which a solution exhibits a colloidal state when visually observed by the test method described below, but it may also be in a state in which fibrous gel is dispersed. The acid to be impregnated or applied to water-soluble paper must not interfere with water solubility; in other words, it must be a weak acid that can maintain the base saturation of CMC-Na above a certain level during impregnation or application. No. This is because as the degree of base saturation decreases, the dissolution time becomes longer, and eventually the solution becomes poorly soluble or insoluble, making it impossible to maintain a predetermined water retention amount. In the present invention, the predetermined water retention amount is set to 8 g/g or more, and the degree of base saturation that can maintain this water retention amount is set to 40% or more. In the present invention, the acid index in water (pKa) is used as an index of the acid to be selected. The acid index in water is the logarithm of the reciprocal of the dissociation constant of the electrolyte in water. The higher the acid index in water, the weaker the acid strength, and the base saturation of CMC-Na is less likely to decrease. In the present invention, the acid index in water (hereinafter referred to as acid index) is
Use an acid of 3.8 or higher. Further, even if the acid which is a constituent material of the water-soluble sheet of the present invention satisfies the above-mentioned requirements, it must not be deliquescent in nature. Since the water-soluble paper that is the base material is made of CMC-Na, its equilibrium moisture content is high at approximately 16% (20℃, 65%RH), so the moisture content in the paper is increased, and as a result, they react with each other and reduce the degree of base saturation. This is because there is a risk of deterioration. Therefore, it is necessary to use an acid that is solid at room temperature and virtually non-deliquescent;
It is desirable that CMC-Na be coated to suppress moisture absorption. The water-soluble sheet of the present invention uses water-soluble paper as a base material,
For example, the water-soluble paper is impregnated with a solution in which the specific solid acid is dissolved in an organic solvent or a mixed solvent of an organic solvent and water, and in the impregnation process, a predetermined amount of base saturation is maintained above a certain level. It is manufactured by attaching a solid acid and drying it. The seeped acid fills the mesh-like voids of the water-soluble paper and becomes a single piece. When processed into a size and shape according to the purpose of use and used as a process control material, the process control material absorbs alkaline liquid generated during the process, retains water, and automatically neutralizes it. Unless exposed to water, it will not disintegrate and maintain its shape, and there is no risk of contaminating other processes. Thus, according to the present invention, a water-soluble matrix comprising fibrous carboxymethyl cellulose or fibrous carboxymethyl cellulose and papermaking fibers is impregnated with or coated with a water-soluble solid acid or a water-soluble solid acid and a water-soluble binder. A water-soluble sheet having a characteristic base neutralizing ability and a method for producing the same are provided. The configuration of the present invention will be explained in detail below with reference to experimental examples. Experimental example 1 Using a mixed solvent of ethanol and water (1:1 parts by weight), the base material was treated with varying concentrations of acetic acid (pKa 4.756), and the relationship between base saturation and water solubility and water retention capacity of acid-treated paper was investigated. The relationship was investigated and shown in Table 1 and Figure 1. Acetic acid, which is a liquid acid, was used because it is easy to measure base saturation and water retention. As a base material, fibrous CMC-H (etherification degree
0.43, made by Nichirin Chemical Co., Ltd.), the paper is made using 100%
Water-soluble paper with a weight of 80 g/m 2 manufactured by adding a soda carbonate solution was used. For acid treatment, use 50ml of acetic acid solution of each concentration.
Soak 1 g of the bone-dry sample in the water, stir for 2 hours, then separate.
The residue was washed in a conventional manner to remove residual acetic acid, and then dried under reduced pressure at 60°C. Base exchange capacity and base saturation were measured as follows. Take 0.5g of the untreated water-soluble paper and the above acid-treated sample, respectively, add 20ml of 0.5N caustic soda, stir for 2 hours, add 10ml of pure water, perform potentiometric titration with 0.5N hydrochloric acid, and calculate the titration value. Aml. As a blank test, the same operation was performed without using a sample, and the titration value was taken as Bml. The amount of base exchanged solubility and the degree of base saturation were determined using the following formula. Base exchange capacity (mg equivalent/g) =
(B-A) x 0.5 x f/1000 x 1/W x 1000 f: 0.5N HCl factor W: Sample bone dry weight (g) Base saturation (%) = base exchange capacity - exchangeable H + amount / Base exchange capacity x 100 = exchangeable base amount / exchangeable base amount + exchangeable H
+ Amount x 100 Water solubility was determined by putting approximately 1 g of a test piece into 300 ml of water, rotating it with a magnetic stirrer, and measuring the number of seconds it took for the test piece to dissolve. Those with small fiber lumps remaining even after 120 seconds were classified as poorly soluble, and those whose sheet form did not collapse were classified as insoluble. The water retention capacity is determined by adding 1g of bone dry sample to 200ml of water.
After stirring for a second, the sample was transferred to a polyester cloth bag of known weight, dehydrated for 1 minute at 770 G using a centrifuge, and the weight was determined and expressed as the weight per 1 g of the bone-dried sample.
【表】
第1表によれば、水溶性は塩基飽和度が53%以
上では無処理水溶紙と変らず、それ以下ではやや
溶解速度がおそくなる。塩基飽和度が低いものほ
どその溶解液中には繊維状ゲルの分散が顕著であ
つた。保水量については35.3%以下のものは塩基
飽和度0%の0.5モル塩酸処理紙と殆んど同程度
まで低下した。第1表の結果を図示した第1図に
よれば、塩基飽和度が40%以下では保水量が殆ん
ど最低になるので、本発明においては保水量を
8g/g以上とし、これを維持し得る塩基飽和度
は40%以上とする。
実施例 2
本発明に用いる酸を特定するために、エーテル
化度0.43の繊維状セルロースグリコール酸(以
下、CMC−Hという)を100%用いて抄紙し、炭
酸ソーダ液を添加して製造した80g/m2の水溶紙
を基材とし、含浸液としては酸指数の異なる種々
の酸をエタノールに溶解して15重量%の溶液を調
製した。一定量の水溶紙をそれぞれの酸溶液に約
10秒浸漬して加圧脱水し、80℃で乾燥して供試試
料を作成した。試験項目および試験結果は、第2
表のとおりであつた。表中、酸指数は2塩基酸以
上の酸はpKa1を示した。また、3cm×5cmの大
きさに切断した試料を0.1N苛性カリウム溶液25
ml中に入れて5分間撹拌した後、残留している苛
性カリウムを0.1N塩酸を用いて滴定し、資料に
よる苛性カリウムの中和量を求め、これを塩基中
和能力とした。
なお、保水量の測定は実験例1に準じて行な
い、表示値は基材たる水溶紙1g当りの保水量と
し、第1表と比較できるようにした。[Table] According to Table 1, when the base saturation is 53% or higher, the water solubility is the same as that of untreated water-soluble paper, and when it is lower than that, the dissolution rate is slightly slower. The lower the degree of base saturation, the more pronounced the dispersion of fibrous gel in the solution. The amount of water retained was reduced to almost the same level as paper treated with 0.5M hydrochloric acid with a base saturation of 0% for papers with a water retention capacity of 35.3% or less. According to FIG. 1, which illustrates the results of Table 1, the water retention amount is almost the lowest when the degree of base saturation is 40% or less, so in the present invention, the water retention amount is
8 g/g or more, and the base saturation that can maintain this is 40% or more. Example 2 In order to specify the acid used in the present invention, 80 g of paper was made using 100% fibrous cellulose glycolic acid (hereinafter referred to as CMC-H) with a degree of etherification of 0.43, and a soda carbonate solution was added. /m 2 water-soluble paper was used as the base material, and various acids with different acid indices were dissolved in ethanol to prepare a 15% by weight solution as an impregnating liquid. Approximately a certain amount of water-soluble paper is added to each acid solution.
A test sample was prepared by immersing it for 10 seconds, dehydrating it under pressure, and drying it at 80°C. Test items and test results are shown in the second
It was as shown in the table. In the table, the acid index indicates pKa 1 for acids of dibasic acid or higher. In addition, a sample cut to a size of 3 cm x 5 cm was prepared using 0.1N caustic potassium solution 25
ml and stirred for 5 minutes, the remaining caustic potassium was titrated using 0.1N hydrochloric acid, the amount of neutralization of caustic potassium was determined from the data, and this was taken as the base neutralization ability. The water retention amount was measured according to Experimental Example 1, and the displayed value was the water retention amount per 1 g of water-soluble paper as the base material, so that it could be compared with Table 1.
【表】
第2表によれば、水溶性は酸指数によつて異な
るが、酸指数の高い酸の水溶性は無処理水溶紙と
全く変らない。グリコール酸(pKa3.831)では
溶解時間が遅くなり、リンゴ酸(pKa3.460)以
下の酸は不溶となる。保水量についても明瞭な分
岐点が見られ、リンゴ酸以下の酸では2g/g以
下となつた。酸の付着量は試料により差があつた
が、上記の傾向には殆んど影響していない。
従つて、前記第1図にあてはめると、この実験
においては、グリコル酸(pKa3.831)以上の酸
を用いることにより、塩基飽和度40%以上の本発
明水溶性シートが得られることが判明する。ま
た、本発明水溶性シートから付着した固体酸を溶
解除去して塩基飽和度を測定することは、繁雑な
実験操作を必要とするので、保水量を測定するこ
とにより、これを容易に推定することができる。
以上の結果から、本発明に用いる酸はpKaが
3.831以上の固体酸が好ましいが、水溶紙には通
常エーテル化度0.25〜0.65のCMC−Hを用いるこ
と、この実験には0.43のCMC−Hを用いたこと、
エーテル化度が大きいほど保水量が大で耐酸性も
増すこと等を考慮すれば、本発明に用いうる酸は
酸指数が3.8以上の固体酸であるということがで
きる。また、上記の要件を満たせば無機酸でもよ
い。
なお、この実験では乳酸(液体酸)についても
試験した(液体酸が本発明の目的達成のためには
不適当であることは既に説明した)が、その付着
量は8g/m2(基材の10重量%程度)が限度であ
り、また塩基中和能力も最大0.17当量/m2にすぎ
なかつた。従つて、本発明水溶性シートはこの程
度以上が望ましく、固体酸の付着量は基材の10重
量%以上、塩基中和能力は0.15g当量/m2以上が
実用的である。なお、本発明水溶性シートの溶解
試験の際の溶解液のPHはすべて3以下であつた。
付着量と塩基中和能力との関係については後述
する。
本発明の基材として用いる水溶紙は、繊維状カ
ルボキシメチルセルロースすなわちセルロースグ
リコール酸のナトリウム、カリウム等の1価金属
塩の短繊維から成る。通常、ナトリウム塩
(CMC−Na)が用いられる。CMC−Naから成
る水溶紙は、公知の他の繊維原料が配合されてい
てもよく、公知の方法により製造される。たとえ
ば、特公昭48−27605号に開示されているように、
CMC−H100%又はCMC−Hと40重量%以下の
晒クラフトパルプとの混合紙料を抄紙し、プレス
フエルト上の湿紙匹にアルカリ水溶液を添加して
CMC−Hを中和した後、脱水、乾燥して製造す
る。CHC−Hはエーテル化度が0.2〜1.0の範囲の
ものを用いる得るが、通常は0.25〜0.65のものを
用い、抄紙性、成紙の溶解性、強度等の点から、
0.40〜0.60のものが最もよく用いられる。0.65以
上になると繊維の膨潤が著しくなり抄造し難くな
るが、本発明の基材としては処理すべき酸の種類
によつては耐酸性を増すため0.65〜1.0のものを
用いる。0.25以下のCMC−Hは抄造し易いが、
製品の水溶性が劣る。
CMC−H以外の製紙用繊維としては、その種
類に特に制限はなく、一般のセルロスパルプ、レ
ーヨンなどの半合成繊維、ポリエチレンなどの合
成パルプ、アクリルニトリルなどの合成繊維等を
用い得るが、本発明の目的に対しては吸水性、保
水性のあるものが好ましく、通常は晒クラフトパ
ルプ、晒サルフアイトパルプ、溶解パルプ等のセ
ルロースパルプ及びレーヨンが用いられる。その
目的は、抄紙性の改善、本発明水溶性シートの強
度をあげ、また通気性を高め、吸水速度を速める
こと等にあるが、保水量は通常自重の1倍以下で
あるため多用は好ましくなく、CMC−Hの50重
量%以下を置換するにとどめる。
本発明に用いる酸溶液は、各種の有機溶媒もし
くは水と相溶性のある有機溶媒と水との混合溶媒
に所定量の固体酸を溶解するか、又は固体酸を粉
砕した微細粒子を難溶性もしくは不溶性の有機溶
媒中に分散し、この中に少量のバインダーを加え
て調製する。固体酸を溶解可能な有機溶媒として
は、メチルアルコール、エチルアルコール、プチ
ルアルコール、プロピルアルコールの如きアルコ
ール類、アセトン、エチルメチルケトン、メチル
プロピルケトンの如きケトン類、エチルエーテ
ル、イソプロピルエーテルの如きエーテル類を用
いることができる。水と相溶性のある有機溶媒と
しては、メチルアルコール、エチルアルコール、
ブチルアルコール、プロピルアルコールの如きア
ルコール類、アセトン、エチルメチルケトン、メ
チルプロピルケトンの如きケトン類を用いること
ができる。そして、通常は製造コストの点から、
メチルアルコール、エチルアルコール等の50重量
%混合水溶媒が用いられる。粉砕した固体酸の微
細粒子としては、たとえば250メツシユの標準篩
を通過した粉末を用いる。これを分散させる有機
溶媒としては、ベンゼン、トルエン、キシレン等
の芳香族炭化水素類、ヘプタン、ヘキサン等の脂
肪族炭化水素類、酢酸エチル、酢酸−n−ブチル
等のエステル類、クロロホルム、メチレンクロラ
イド、n−ブチルクロライド等の塩素化炭化水素
類を用いることができる。なお、これらにメタノ
ール、エタノール、n−プロパノール等のアルコ
ール類、アセトン、エチルメチルケトン等のケト
ン類を添加してもよい。固体酸の微細粒子の分散
溶液に添加するバインダーは固体酸および基材を
溶解しない有機溶媒に可溶で、かつ水およびアル
カリ水溶液にも可溶なバインダーでなければなら
ない。この要件が満たされない場合には、フイル
ム状でで残留し、水溶性および塩基中和作用が妨
げられるからである。
好適なバインダーとしては、ポリビニルピロリ
ドン、カルボキシ変性酢酸ビニル重合物、スチレ
ン−無水マレイン酸共重合物等が例示できる。バ
インダーの添加量は、上記と同様の趣旨から、酸
に対して5〜15%の範囲とする。
固体酸は上記溶液状もしくは分散液状で用いる
場合のほか、融点が200℃以下の固体酸たとえば
アゼライン酸(106.5℃)、アジピン酸(153℃)、
コハク酸(185℃)、グルタル酸(97℃)などの場
合には、その溶融液に基材を含浸し、冷却して製
造することもできる。
上記した酸の溶液、分散液、溶融液を基材に適
用するには、含浸槽、塗布ロール等を有する通常
の含浸機、塗工機を用いる。酸溶液の濃度は高い
方が好ましく、たとえアゼライン酸の10重量%濃
度のメタノール−水(1:1重量部)混合溶液に
基材を含浸し、余剰をドクターで掻き取り80〜
100℃で乾燥する。この方法で基材の100重量%ま
で付着させることができる。100重量%以上では
粉落ちが大となり、また吸水速度が遅くなる。固
体酸の分散液は、塗工機を用いて基材に塗布す
る。塗布法では150重量%まで可能であり、また
溶融法では120重量%まで固体酸を付着させるこ
とができる。
次に、酸の付着量(g/m2)と塩基中和能力と
の関係を知るために、溶液含浸法、塗工法、溶融
含浸法とに別けて試料を作成し、比較を行なつ
た。基材とした水溶紙は、秤量約120gでエーテ
ル化度0.43のCMC−Na100%から成るものであ
る。溶液含浸法では、アゼライン酸およびアジビ
ン酸をそれぞれエタノール−水混合溶媒(1:1
重量部)に溶解した10重量%濃度の溶液を用い
た。塗工法では、コハク酸を粉砕して250メツシ
ユ標準篩通過分を100重量部調整し、またバイン
ダーとしてポリビニルピロリドン10重量部をクロ
ロホルム150重量部に溶解した溶液を調製し、粉
砕したコハク酸をこの溶液中に分散させた。ま
た、溶融含浸法では、アゼライン酸の溶融物を用
いた。これらの方法では、何れも、1回以上含浸
もしくは塗布を行なつて試料を作成した。酸の付
着量は含浸、塗布前後の試料の重量差により求
め、塩基中和能力は前記した方法により測定し
た。その結果を第2図に示した。図中、1はアゼ
ライン酸の溶液含浸法、2はアジピン酸の溶液含
浸法、3はコハク酸の塗工法、4はアゼライン酸
の溶融含浸法の場合のデーターである。なお、各
試料とも溶解性、保水量とも満足できるものであ
る。
第2図によれば、酸の付着量と塩基中和能力と
の間には比例関係があり、たとえば塩基中和能力
が約0.9g当量/m2の本発明水溶紙を得たい場合
には、アゼライン酸の溶液含浸法によれば75g/
m2付着させればよく、同じ溶融含浸法によれば68
g/m2付着させればよく、また、コハク酸の塗工
法によれば75g/m2を塗布すればよいことにな
る。図に溶液含浸法の例として示したアジピン酸
とアゼライン酸の直線は、付着させる方法が同じ
であれば平行することを示し、その直線の高さの
差は上記二塩基酸の場合、分子量の差を示し、分
子量の小さいアジピン酸の方が同一塩基中和能力
を得るのに付着量が少なくて済むことが判る。な
お、この実験においては、試料の測定水分(20
℃,65%RH)は最低6.8%、最高10.8%であり、
基材が固体酸によつて被覆され防湿効果が生じて
いると考えられた。
以上説明した如く、本発明水溶性シートは、塩
基中和能力を水溶紙が本来的に有する保水性を生
かしつつ水溶紙に付与するにあたつて、特定の条
件、即ち特定の酸を用い且つ基材への適用方法を
選ぶことによつて、CMC−Naという高分子塩と
酸との反応のバランスをとつて製造し得た新規な
水溶性シートであり、製造法もまた新規なもので
ある。本発明水溶性シートは、通常0.1Nないし
1N程度のアルカリ液の処理を目的とするプロセ
スコントロール材として利用されるが、この範囲
の濃度に限られるものではなく、またすべての無
機塩基、有機塩基その他弱酸と強塩基の塩などの
アルカリ性溶液に対しても広く用いることができ
る。また、その使用の態様としては、本発明水溶
性シートを通常のパルプ、紙やプラスチツクフイ
ルム等に積層して固定し、いわゆる中和タイミン
グ層として用いる場合のほか、単独にプロセスコ
ントロール材として用いることもできる。
以下に実施例をあげて本発明をさらに詳細に説
明するが、本発明はこれらに限定されるものでは
ない。
なお、実施例には基材に他の製紙用繊維を配合
したものも挙げたが、この場合の溶解性は溶解分
散性として表示した。また、1N−NaOH溶液を
用いた保水量も例示したが、水を用いた場合と異
なり、繊維状ゲルを含まない完全なゲルとなつて
遠心脱水法では測定できないので、次の吸引過
法に従つた。すなわち、試料絶乾0.5gを所定の
アルカリ溶液100g中に入れて30秒間撹拌した後、
ポリエステル製布を敷いたブフナーロート上に注
ぎ、6.7mmHgで吸引別し、式
吸引過法保水量g/g=100−液重量/試料絶乾
重量
に従つて保水量を算出した。
実施例 1
エーテル化0.43のCMC−H(ニチリン化学製)
80重量部、溶解パルプ20重量部より成る紙料を用
いて公知の方法により秤量130g/m2の水溶紙を
製造した。固体酸としてはアゼライン酸
(pKa4.523)をエタノールに溶解して10重量%の
溶液を調製した。これを含浸機の含浸槽に移し水
溶紙を通した後70℃で熱風乾燥した。含浸工程の
含浸時間とプレスロールのニツプ圧を変えること
により酸付着量の異なる本発明水溶紙を3種類製
造した。第3表に夫々の特性値を示した。[Table] According to Table 2, water solubility differs depending on the acid index, but the water solubility of acids with high acid indexes is no different from that of untreated water-soluble paper. Glycolic acid (pKa 3.831) slows down the dissolution time, and acids below malic acid (pKa 3.460) become insoluble. A clear branching point was also observed for water retention, with acids below malic acid reaching 2g/g or less. Although the amount of acid adhering varied depending on the sample, it had little effect on the above trend. Therefore, applying to Figure 1 above, it is found that in this experiment, by using an acid of glycolic acid (pKa 3.831) or higher, a water-soluble sheet of the present invention with a base saturation of 40% or higher can be obtained. . Furthermore, since measuring the degree of base saturation by dissolving and removing adhering solid acids from the water-soluble sheet of the present invention requires complicated experimental operations, this can be easily estimated by measuring the amount of water retained. be able to. From the above results, the acid used in the present invention has a pKa of
A solid acid of 3.831 or higher is preferred, but CMC-H with an etherification degree of 0.25 to 0.65 is usually used for water-soluble paper, and CMC-H with a degree of 0.43 was used in this experiment.
Considering that the higher the degree of etherification, the greater the water retention capacity and the higher the acid resistance, it can be said that the acid that can be used in the present invention is a solid acid with an acid index of 3.8 or more. Further, an inorganic acid may be used as long as it satisfies the above requirements. In this experiment, lactic acid (liquid acid) was also tested (it has already been explained that liquid acid is inappropriate for achieving the purpose of the present invention), and the amount of adhesion was 8g/m 2 (substrate The maximum base neutralization ability was only 0.17 equivalent/m 2 ). Therefore, it is desirable for the water-soluble sheet of the present invention to have a solid acid adhesion of 10% by weight or more of the base material, and a practical base neutralization ability of 0.15 g equivalent/m 2 or more. In addition, the pH of the dissolving solution during the dissolution test of the water-soluble sheet of the present invention was all 3 or less. The relationship between the adhesion amount and base neutralization ability will be described later. The water-soluble paper used as the base material of the present invention is composed of short fibers of fibrous carboxymethyl cellulose, that is, a monovalent metal salt such as sodium or potassium of cellulose glycolate. Usually, the sodium salt (CMC-Na) is used. The water-soluble paper made of CMC-Na may contain other known fiber raw materials and is produced by a known method. For example, as disclosed in Special Publication No. 48-27605,
Paper is made from a mixed paper stock of 100% CMC-H or CMC-H and 40% by weight or less of bleached kraft pulp, and an alkaline aqueous solution is added to the wet paper web on the press felt.
It is produced by neutralizing CMC-H, then dehydrating and drying it. CHC-H can have an etherification degree of 0.2 to 1.0, but it is usually 0.25 to 0.65.
A value between 0.40 and 0.60 is most commonly used. If the value is 0.65 or more, the fibers will swell significantly and become difficult to form into paper, but depending on the type of acid to be treated, the base material used in the present invention may have a value of 0.65 to 1.0 to increase acid resistance. CMC-H of 0.25 or less is easy to make, but
The product has poor water solubility. There are no particular restrictions on the type of papermaking fibers other than CMC-H, and general cellulosic pulp, semi-synthetic fibers such as rayon, synthetic pulps such as polyethylene, synthetic fibers such as acrylonitrile, etc. can be used, but the present invention For this purpose, materials with water absorption and water retention properties are preferred, and cellulose pulps such as bleached kraft pulp, bleached sulfite pulp, and dissolving pulp, and rayon are usually used. The purpose of this is to improve paper-making properties, increase the strength of the water-soluble sheet of the present invention, increase air permeability, and speed up water absorption. However, since the amount of water retained is usually less than 1 times its own weight, it is preferable not to use it frequently. No, only 50% by weight or less of CMC-H is replaced. The acid solution used in the present invention can be prepared by dissolving a predetermined amount of a solid acid in various organic solvents or a mixed solvent of water and an organic solvent that is compatible with water, or by adding fine particles obtained by pulverizing a solid acid to a sparsely soluble or It is prepared by dispersing it in an insoluble organic solvent and adding a small amount of binder therein. Examples of organic solvents that can dissolve solid acids include alcohols such as methyl alcohol, ethyl alcohol, butyl alcohol, and propyl alcohol, ketones such as acetone, ethyl methyl ketone, and methyl propyl ketone, and ethers such as ethyl ether and isopropyl ether. can be used. Organic solvents that are compatible with water include methyl alcohol, ethyl alcohol,
Alcohols such as butyl alcohol and propyl alcohol, and ketones such as acetone, ethyl methyl ketone and methyl propyl ketone can be used. And usually from the point of view of manufacturing costs,
A 50% by weight mixed water solvent such as methyl alcohol and ethyl alcohol is used. As the fine particles of the pulverized solid acid, for example, a powder that has passed through a standard sieve of 250 mesh is used. Organic solvents for dispersing this include aromatic hydrocarbons such as benzene, toluene, and xylene, aliphatic hydrocarbons such as heptane and hexane, esters such as ethyl acetate and n-butyl acetate, chloroform, and methylene chloride. , n-butyl chloride and the like can be used. Note that alcohols such as methanol, ethanol, and n-propanol, and ketones such as acetone and ethyl methyl ketone may be added to these. The binder added to the dispersion solution of fine solid acid particles must be soluble in an organic solvent that does not dissolve the solid acid and the base material, and must also be soluble in water and aqueous alkaline solutions. If this requirement is not met, it will remain in the form of a film, impeding water solubility and base neutralization. Examples of suitable binders include polyvinylpyrrolidone, carboxy-modified vinyl acetate polymers, and styrene-maleic anhydride copolymers. The amount of binder added is in the range of 5 to 15% based on the acid, for the same purpose as above. In addition to the cases where solid acids are used in the form of solutions or dispersions mentioned above, solid acids with a melting point of 200°C or lower, such as azelaic acid (106.5°C), adipic acid (153°C),
In the case of succinic acid (185°C), glutaric acid (97°C), etc., it can also be produced by impregnating the base material with the melt and cooling it. In order to apply the above-mentioned acid solution, dispersion, or melt to the substrate, a conventional impregnation machine or coating machine having an impregnation tank, a coating roll, etc. is used. The higher the concentration of the acid solution, the better. Even if the base material is impregnated with a methanol-water (1:1 parts by weight) mixed solution of azelaic acid having a concentration of 10% by weight, the excess is scraped off with a doctor.
Dry at 100℃. With this method, up to 100% by weight of the substrate can be deposited. If it exceeds 100% by weight, powder will fall off significantly and the water absorption rate will be slow. The solid acid dispersion is applied to the substrate using a coating machine. With the coating method, it is possible to deposit up to 150% by weight, and with the melting method, it is possible to deposit up to 120% by weight. Next, in order to understand the relationship between the amount of acid attached (g/m 2 ) and the base neutralization ability, samples were prepared and compared using the solution impregnation method, coating method, and melt impregnation method. . The water-soluble paper used as the base material was made of 100% CMC-Na with a weight of about 120 g and a degree of etherification of 0.43. In the solution impregnation method, azelaic acid and adivic acid were each mixed in an ethanol-water mixed solvent (1:1
A 10% strength by weight solution was used. In the coating method, 100 parts by weight of succinic acid was pulverized to pass through a 250-mesh standard sieve, and a solution was prepared by dissolving 10 parts by weight of polyvinylpyrrolidone in 150 parts by weight of chloroform as a binder. Dispersed in solution. Furthermore, in the melt impregnation method, a melt of azelaic acid was used. In all of these methods, samples were prepared by impregnation or coating one or more times. The amount of acid attached was determined by the difference in weight of the sample before and after impregnation and coating, and the base neutralization ability was measured by the method described above. The results are shown in Figure 2. In the figure, 1 is data for the azelaic acid solution impregnation method, 2 is the adipic acid solution impregnation method, 3 is the succinic acid coating method, and 4 is the data for the azelaic acid melt impregnation method. It should be noted that each sample had satisfactory solubility and water retention. According to FIG. 2 , there is a proportional relationship between the amount of acid attached and the base neutralization ability. , 75g/according to the azelaic acid solution impregnation method.
m 2 deposited, and according to the same melt impregnation method 68
g/m 2 , and according to the succinic acid coating method, it is sufficient to apply 75 g/m 2 . The straight lines of adipic acid and azelaic acid shown in the figure as an example of the solution impregnation method are parallel if the method of attachment is the same, and the difference in the height of the straight lines is the difference in molecular weight in the case of the above dibasic acid. It can be seen that adipic acid, which has a smaller molecular weight, requires a smaller amount of adhesion to obtain the same base neutralization ability. In this experiment, the measured moisture content of the sample (20
℃, 65%RH) is minimum 6.8% and maximum 10.8%,
It was thought that the base material was coated with the solid acid, resulting in a moisture-proofing effect. As explained above, the water-soluble sheet of the present invention requires specific conditions, that is, using a specific acid and This is a new water-soluble sheet that can be manufactured by balancing the reaction between CMC-Na polymer salt and acid by selecting the application method to the base material, and the manufacturing method is also new. be. The water-soluble sheet of the present invention is usually 0.1N to
It is used as a process control material for the purpose of treating alkaline solutions of about 1N, but is not limited to concentrations within this range, and can also be used for alkaline solutions such as all inorganic bases, organic bases, and salts of weak acids and strong bases. It can also be widely used for In addition, the water-soluble sheet of the present invention can be laminated and fixed on ordinary pulp, paper, plastic film, etc., and used as a so-called neutralization timing layer, as well as used alone as a process control material. You can also do it. The present invention will be explained in more detail with reference to Examples below, but the present invention is not limited thereto. In addition, in Examples, examples in which other papermaking fibers were blended with the base material were also listed, but the solubility in this case was expressed as dissolution and dispersibility. We also gave an example of the water retention capacity using a 1N-NaOH solution, but unlike when using water, it becomes a complete gel that does not contain fibrous gels and cannot be measured using the centrifugal dehydration method. I obeyed. That is, after putting 0.5 g of an absolutely dry sample into 100 g of a specified alkaline solution and stirring for 30 seconds,
The mixture was poured onto a Buchner funnel lined with polyester cloth, and the mixture was suctioned at 6.7 mmHg, and the water retention amount was calculated according to the formula: Water retention amount by suction method g/g = 100 - weight of liquid/absolutely dry weight of sample. Example 1 Etherification 0.43 CMC-H (manufactured by Nichirin Chemical Co., Ltd.)
A water-soluble paper having a weight of 130 g/m 2 was produced by a known method using a paper stock consisting of 80 parts by weight of dissolving pulp and 20 parts by weight of dissolving pulp. As a solid acid, azelaic acid (pKa 4.523) was dissolved in ethanol to prepare a 10% by weight solution. This was transferred to an impregnating tank of an impregnation machine, passed through water-soluble paper, and then dried with hot air at 70°C. By changing the impregnation time in the impregnation step and the nip pressure of the press rolls, three types of water-soluble papers of the present invention with different amounts of acid adhesion were manufactured. Table 3 shows the respective characteristic values.
【表】
第3表によればアゼライン酸のエタノール溶液
を含浸した本発明水溶性シートは秤量、厚さ、密
度および外観から一般の白色含浸加工紙に類似す
る。そして酸付着量は29〜60重量%であつた。こ
の範囲の付着量では水中および0.1N−NaOH溶
液中での溶解分散時間に殆んど差はなく何れも速
やかに溶解分散した。また保水量は17〜29g/g
であり、酸付着量が著しく多くなると減少するこ
とが判つた。しかし第1図によれば
本発明水溶性シート中のCMC−Naの塩基飽和
度は50%を確保していることが判る。0.1N−
NaOH溶液の保水量も水の場合と殆んど変らな
かつた。
1N−NaOH溶液を用いた試験では溶解分散時
間は水、0.1N−NaOH溶液の場合と殆んど異な
らなかつたが完全にゲル化し著しい膨潤を示し吸
引過法による保水量は何れも24g/gであつ
た。
塩基中和能力は0.32〜0.90g当量/m2と広い範
囲のものを得ることができた。なお、これらの水
溶性シートはシート水分(20℃,65%RH)が7
〜10%であり、基材の16%に比べると激減した。
このことはろう状のアゼライン酸が基材を被覆し
たことを示し、吸湿による塩基飽和度の低下、即
ち溶解分散法および保水性の低下を防止する効果
を有する。
実施例 2
実施例1の溶解パルプにかえてレイヨン20重量
部を用い、他は同様にして秤量130g/m2の水溶
紙を製造した。
アゼライン酸(pKa4.523、融点106.5℃)の溶
融含浸法により本発明水溶性シートを製造する。
含浸機の加熱含浸槽内で115℃に加熱したアゼラ
イン酸の溶融液中を通紙した後、放冷、固化し
67.3g/m2の付着量を有する秤量197.3g/m2の
本発明水溶紙を得た。このものは厚さ224μm、密
度0.881g/cm3、塩基中和能力0.92g当量/m2で
あつた。また溶解分散時間は水中で39秒、0.1N
NaOH溶液中で44秒であつた。溶解分散時間が
長いのは溶融含浸法では実施例1の溶液含浸法に
比しシート密度がかなり大きくなつたので液体が
滲透しにくいためと思われる。しかし保水量は18
g/g、吸引過法による1N−NaOH溶液保水
量は実施例1と同じ24g/gであつた。
実施例 3
実施例1と同様にして製造した秤量130g/m2
の水溶液を基材としてコハク酸(pKa4.207)の
塗工法により本発明水溶性シートを製造する。
250メツシユ標準篩を通過したコハク酸微細粉末
を準備した。またクロロホルム150重量部にポリ
ビニルピロリドン10重量部を溶解した溶液を作
り、これに上記コハク酸微粉末100重量部を投入
して塗工用分散液を調製した。この分散液をアプ
リケーターバーにより基材に塗布し75℃の熱風で
乾燥し、付着量の異なる2種類の本発明水溶性シ
ートを得た。その物性を第4表に示した。[Table] According to Table 3, the water-soluble sheet of the present invention impregnated with an ethanol solution of azelaic acid is similar to general white impregnated paper in terms of weight, thickness, density and appearance. The amount of acid attached was 29 to 60% by weight. In this range of coating weight, there was almost no difference in dissolution and dispersion time in water and in 0.1N-NaOH solution, and dissolution and dispersion occurred quickly in both cases. Also, the water retention amount is 17-29g/g
It was found that this decreases when the amount of acid adhesion increases significantly. However, according to FIG. 1, it can be seen that the base saturation of CMC-Na in the water-soluble sheet of the present invention is maintained at 50%. 0.1N−
The water retention capacity of the NaOH solution was almost the same as that of water. In the test using 1N-NaOH solution, the dissolution and dispersion time was almost the same as that of water and 0.1N-NaOH solution, but it completely gelled and swelled significantly, and the water retention amount by suction method was 24g/g in both cases. It was hot. A wide range of base neutralization abilities could be obtained, ranging from 0.32 to 0.90 g equivalent/m 2 . In addition, these water-soluble sheets have a sheet moisture content (20℃, 65%RH) of 7.
~10%, which is a sharp decrease compared to 16% for the base material.
This indicates that waxy azelaic acid coated the base material, which has the effect of preventing a decrease in base saturation due to moisture absorption, that is, a decrease in dissolution and dispersion method and water retention. Example 2 A water-soluble paper having a weight of 130 g/m 2 was produced in the same manner as in Example 1 except that 20 parts by weight of rayon was used instead of the dissolving pulp of Example 1. The water-soluble sheet of the present invention is produced by a melt impregnation method with azelaic acid (pKa 4.523, melting point 106.5°C).
After passing the paper through the azelaic acid melt heated to 115℃ in the heated impregnation tank of the impregnation machine, it was left to cool and solidify.
A water-soluble paper of the present invention having a weight of 197.3 g/m 2 and a coating weight of 67.3 g/m 2 was obtained. This product had a thickness of 224 μm, a density of 0.881 g/cm 3 , and a base neutralization capacity of 0.92 g equivalent/m 2 . The dissolution and dispersion time in water is 39 seconds and 0.1N.
It took 44 seconds in NaOH solution. The reason why the dissolution and dispersion time is long is thought to be that in the melt impregnation method, the sheet density was considerably higher than in the solution impregnation method of Example 1, so that it was difficult for the liquid to penetrate. However, the water retention capacity is 18
g/g, and the water retention amount of the 1N-NaOH solution by suction filtration method was 24 g/g, the same as in Example 1. Example 3 Produced in the same manner as Example 1, weighing 130 g/m 2
The water-soluble sheet of the present invention is produced by a coating method using succinic acid (pKa 4.207) using an aqueous solution of as a base material.
A fine succinic acid powder that passed through a 250 mesh standard sieve was prepared. Further, a solution was prepared by dissolving 10 parts by weight of polyvinylpyrrolidone in 150 parts by weight of chloroform, and 100 parts by weight of the above-mentioned fine succinic acid powder was added to the solution to prepare a coating dispersion. This dispersion was applied to a substrate using an applicator bar and dried with hot air at 75°C to obtain two types of water-soluble sheets of the present invention with different amounts of adhesion. Its physical properties are shown in Table 4.
【表】
第4表によればコハク酸の微細粒子分散液を基
材に塗工するにあたり有機溶媒およびバインダー
を選択することにより、水および0.1N−NaOH
溶液中における溶解分散時間が基材と全く変らな
いものを得ることができる。従つて塗工法による
ものは塩基中和の速さが要求されるプロセスに好
適である。なお、このものの保水量は何れも17〜
18g/gであつた。
実施例 4
エーテル化度0.65のCMC−H(ニチリン化学
製)を100%用いて製造した秤量130g/m2の水溶
紙を基材とし、含浸液としてはアジピン酸
(pKa4.430)の15重量%エタノール溶液を用い
た。これを含浸機の含浸槽に移し含浸速度2m/
minで水溶紙を通した後70℃で熱風乾燥し秤量
160.4g/m2の本発明水溶紙を得た。アジピン酸
付着量30g/m2、塩基中和能力0.60g当量/m2、
溶解性は水中で27秒、0.1N−NaOH溶液中で22
秒、保水量は28g/gであり、1N−NaOH溶液
の吸引過法による保水量は28gであつた。
なお水分は10.8%としたので在庫中に製品が変
質するおそれはない。[Table] According to Table 4, by selecting the organic solvent and binder when applying the fine particle dispersion of succinic acid to the substrate, water and 0.1N-NaOH
It is possible to obtain a material whose dissolution and dispersion time in a solution is completely the same as that of the base material. Therefore, the coating method is suitable for processes that require rapid base neutralization. In addition, the water retention capacity of these items is 17~
It was 18g/g. Example 4 Aqueous paper with a weight of 130 g/m 2 manufactured using 100% CMC-H (manufactured by Nichirin Chemical Co., Ltd.) with a degree of etherification of 0.65 was used as the base material, and 15% of adipic acid (pKa 4.430) was used as the impregnating liquid. % ethanol solution was used. Transfer this to the impregnating tank of the impregnating machine and impregnate at a speed of 2 m/
After passing through water-soluble paper for min., dry with hot air at 70℃ and weigh.
A water-soluble paper of the present invention weighing 160.4 g/m 2 was obtained. Adipic acid adhesion amount 30g/m 2 , base neutralization ability 0.60g equivalent/m 2 ,
Solubility is 27 seconds in water and 22 seconds in 0.1N NaOH solution.
Second, the water retention amount was 28 g/g, and the water retention amount by suction filtration method of 1N-NaOH solution was 28 g. The moisture content was set at 10.8%, so there is no risk of the product deteriorating in quality while in stock.
第1図は保水量と塩基飽和度との関係を示す図
表であり、第2図は酸の付着量と塩基中和能力と
の関係を示す図表である。
第2図において、1はアゼライン酸の溶液含浸
法、2はアジピン酸の溶液含浸法、3はコハク酸
の塗工法、4はアゼライン酸の溶融含浸法の各場
合を示す。
FIG. 1 is a chart showing the relationship between water retention amount and base saturation degree, and FIG. 2 is a chart showing the relationship between acid adhesion amount and base neutralization ability. In FIG. 2, 1 shows the azelaic acid solution impregnation method, 2 the adipic acid solution impregnation method, 3 the succinic acid coating method, and 4 the azelaic acid melt impregnation method.
Claims (1)
維状カルボキシメチルセルロースと製紙用繊維と
から形成された水溶性マトリツクスに水溶性固体
酸または水溶性固体酸と水溶性バインダーとが含
浸または塗布されて成ることを特徴とする塩基中
和能力を有する水溶性シート。 2 水溶性固体酸の水中酸指数が3.8以上である
特許請求の範囲第1項記載の塩基中和能力を有す
る水溶性シート。 3 塩基中和能力が0.15g当量/m2以上である特
許請求の範囲第1項または第2項に記載の塩基中
和能力を有する水溶性シート。 4 繊維状カルボキシメチルセルロースから成る
水溶紙または繊維状カルボキシメチルセルロース
に製紙用繊維を混合して成る水溶紙を基材とし、
これに水中酸指数が3.8以上で事実上潮解性のな
い水溶性固体酸を含浸または塗布し、且つ前記含
浸または塗布した紙匹中の繊維状カルボキシメチ
ルセルロースの塩基飽和度を40%以上に維持しつ
つ、該水溶性固体酸を該基材に対し乾物として10
重量%以上付着させることを特徴とする塩基中和
能力を有する水溶性シートの製造法。 5 水溶性固体酸を有機溶媒または有機溶媒と水
との混合溶媒に溶解した溶液の形で含浸または塗
布する特許請求の範囲第4項記載の塩基中和能力
を有する水溶性シートの製造法。 6 水溶性固体酸を溶融物の形で含浸または塗布
する特許請求の範囲第4項記載の塩基中和能力を
有する水溶性シートの製造法。 7 水溶性固体酸を水およびアルカリ可溶性バイ
ンダーとともに有機溶媒中に分散した分散液の形
で含浸または塗布する特許請求の範囲第4項記載
の塩基中和能力を有す水溶性シートの製造法。[Scope of Claims] 1 A water-soluble matrix formed from fibrous carboxymethyl cellulose or fibrous carboxymethyl cellulose and papermaking fibers is impregnated with or coated with a water-soluble solid acid or a water-soluble solid acid and a water-soluble binder. A water-soluble sheet having base neutralizing ability, characterized by: 2. The water-soluble sheet having base neutralization ability according to claim 1, wherein the water-soluble solid acid has an acid index in water of 3.8 or more. 3. The water-soluble sheet having a base neutralizing ability according to claim 1 or 2, which has a base neutralizing ability of 0.15 g equivalent/m 2 or more. 4 The base material is water-soluble paper made of fibrous carboxymethyl cellulose or water-soluble paper made of fibrous carboxymethyl cellulose mixed with papermaking fibers,
This is impregnated or coated with a water-soluble solid acid having a water acid index of 3.8 or higher and virtually non-deliquescent, and the degree of base saturation of the fibrous carboxymethylcellulose in the impregnated or coated paper web is maintained at 40% or higher. At the same time, the water-soluble solid acid was added to the base material as a dry substance for 10 minutes.
A method for producing a water-soluble sheet having a base neutralizing ability, characterized by adhering the base in an amount of at least % by weight. 5. The method for producing a water-soluble sheet having base neutralization ability according to claim 4, which comprises impregnating or coating a water-soluble solid acid in the form of a solution dissolved in an organic solvent or a mixed solvent of an organic solvent and water. 6. A method for producing a water-soluble sheet having base neutralization ability according to claim 4, which comprises impregnating or coating a water-soluble solid acid in the form of a melt. 7. A method for producing a water-soluble sheet having base neutralization ability according to claim 4, which comprises impregnating or coating a water-soluble solid acid in the form of a dispersion in an organic solvent together with water and an alkali-soluble binder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24535083A JPS60139389A (en) | 1983-12-28 | 1983-12-28 | Water-soluble sheet having base neutralizing capacity and its preparation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24535083A JPS60139389A (en) | 1983-12-28 | 1983-12-28 | Water-soluble sheet having base neutralizing capacity and its preparation |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60139389A JPS60139389A (en) | 1985-07-24 |
| JPH0311831B2 true JPH0311831B2 (en) | 1991-02-18 |
Family
ID=17132362
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24535083A Granted JPS60139389A (en) | 1983-12-28 | 1983-12-28 | Water-soluble sheet having base neutralizing capacity and its preparation |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60139389A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006102705A (en) * | 2004-10-08 | 2006-04-20 | Noda:Kk | Cement draining sheet and cement draining treatment method |
| GB201317035D0 (en) * | 2013-09-26 | 2013-11-06 | Bcuk Aquatics Ltd | Water treatment |
-
1983
- 1983-12-28 JP JP24535083A patent/JPS60139389A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60139389A (en) | 1985-07-24 |
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