JPS5953960B2 - Acid- and alkali-resistant paper with breathability and liquid permeability - Google Patents
Acid- and alkali-resistant paper with breathability and liquid permeabilityInfo
- Publication number
- JPS5953960B2 JPS5953960B2 JP3659681A JP3659681A JPS5953960B2 JP S5953960 B2 JPS5953960 B2 JP S5953960B2 JP 3659681 A JP3659681 A JP 3659681A JP 3659681 A JP3659681 A JP 3659681A JP S5953960 B2 JPS5953960 B2 JP S5953960B2
- Authority
- JP
- Japan
- Prior art keywords
- paper
- acid
- alkali
- fibers
- strong acid
- 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
Links
Landscapes
- Filtering Materials (AREA)
- Paper (AREA)
Description
【発明の詳細な説明】
この発明は、例えば所定紙厚範囲において適度の通気、
通液性を有する耐酸、耐アルカリ性紙に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION The present invention provides, for example, appropriate ventilation and
This paper relates to acid- and alkali-resistant paper that has liquid permeability.
近来紙類の用途が拡大され、種々の工業用途例えば工業
用フィルターなどに紙類が多く使用されている。BACKGROUND ART In recent years, the uses of paper have expanded, and paper is now widely used in various industrial applications, such as industrial filters.
周知のようにフィルターなどに用いられる紙類は、一般
のフィルムと異なり適度の通気性及び通液性を有するこ
とが要求されているが、近来その要求される特性も次第
に高水準化されている。As is well known, papers used in filters and the like are required to have appropriate air permeability and liquid permeability, unlike general films, and in recent years, the required properties have gradually become higher. .
例えばフィルター特性として定められた紙厚密度、紙層
を貫通する穴の大きさ、数等も厳しく定められ、これを
満足するものが要求されている。これに加えて廃酸、廃
アルカリ処理フィルター用紙又は電池のセパレーター用
紙等については強酸、強アルカリ液中で用いても殆んど
溶出しない強酸、強アルカリ性が要求されている。しか
し、従来のスパンボンデット紙、乾式不織布、湿式不織
布等の紙類中には耐強酸性、耐アルカリ性に加えて通気
性、通液性を有し、更に顧客の要求に応じて穴の大きさ
、数等を製造時に自在、且つ容易にコントロールできる
ものは見出せなかつた。For example, filter characteristics such as paper thickness density, size and number of holes penetrating the paper layer are strictly defined, and a filter that satisfies these requirements is required. In addition, waste acid and waste alkali treated filter paper, battery separator paper, etc. are required to have strong acidity or strong alkalinity, which hardly dissolves even when used in strong acid or strong alkaline solutions. However, conventional papers such as spunbond paper, dry nonwoven fabric, and wet nonwoven fabric have strong acid resistance and alkali resistance, as well as breathability and liquid permeability, and they also have hole sizes that can be adjusted according to customer requirements. We have not been able to find anything that allows us to freely and easily control the size, number, etc. during manufacturing.
即ち、一般に湿式抄紙法においてはウェットウェブ強度
の点から耐薬品性の高い合成繊維、例えばポリオレフィ
ン系繊維の単独抄紙又は異種オレフィン繊維との混合抄
紙ではウェットウェブ強度が低く抄紙が著しく困難であ
り、仮え抄紙できても著しく嵩高で、紙力特に湿潤時の
紙力が弱い。That is, in general, in the wet papermaking method, from the viewpoint of wet web strength, it is extremely difficult to make paper using synthetic fibers with high chemical resistance, such as polyolefin fibers, alone or mixed with different types of olefin fibers due to the low wet web strength. Even if paper can be made, it is extremely bulky and has poor paper strength, especially when wet.
また熱プレスを行なつた場合フィルム状を呈し、通気、
通液性を満足させることができない。これを改質するた
めに湿潤強力樹脂の加工、熱加工などが一般に利用され
ているが、樹脂の内添加工では嵩高性の問題が解消せず
、含浸加工のような後加工では加工度即ち耐薬品性と通
気、通液性の間に二律背反の関係があり不適当であつた
。一方乾式抄紙においては一般に湿式抄紙に比べて使用
する繊維の繊維長も長く、嵩高でありそのま・でま紙力
が著しく弱くなるので樹脂含浸等の加工が一般に施され
ているが、このため前記湿式抄紙の樹脂加工のところで
述べたように耐薬品性と通気、通液性との二律背反関係
により容易、且つ自在に通気、通液性をコントロールす
ることは不可能であつた。この発明は上記実情に鑑み、
所定の紙厚範囲において穴の大きさ、数等を容易に、且
つ自在にコントロールして適度の通気性、通液性と有す
ることができるようにした耐酸、耐アルカリ性紙を提案
するものである。In addition, when heat-pressed, it becomes film-like, allowing ventilation,
Liquid permeability cannot be satisfied. In order to modify this, wet strong resin processing and thermal processing are generally used, but additive processing within the resin does not solve the problem of bulkiness, and post-processing such as impregnation processing reduces the degree of processing. It was inappropriate because there was a trade-off between chemical resistance, ventilation, and liquid permeability. On the other hand, in dry papermaking, the fibers used are generally longer and bulkier than in wet papermaking, which significantly weakens the strength of straight and loose paper, so treatments such as resin impregnation are generally applied. As mentioned above in the resin processing of wet papermaking, it has been impossible to easily and freely control ventilation and liquid permeability due to the trade-off relationship between chemical resistance and air permeability and liquid permeability. This invention was made in view of the above circumstances.
This paper proposes an acid- and alkali-resistant paper that can easily and freely control the size, number, etc. of holes within a given paper thickness range to have appropriate air permeability and liquid permeability. .
この発明において強酸可溶性繊維としてはその・ 目的
に応じて適当な繊維長、径を有する針葉樹、広葉樹等か
らなる通常のセルロース系パルプ、マニラ麻パルプ、リ
ンターパルプ、バガスパルプ等を使用することができ、
また強酸及び強アルカリ非溶解繊維としてはポリエチレ
ン、ポリプロピレン等のポリオレフイン繊維、ポリ塩化
ビニリデン系繊維、ポリ塩化ビニル系繊維等を使用する
ことができる。In this invention, the strong acid-soluble fibers can be ordinary cellulose pulp made of softwood, hardwood, etc., having fiber length and diameter appropriate depending on the purpose, Manila hemp pulp, linter pulp, bagasse pulp, etc.
Further, as the strong acid- and strong alkali-insoluble fibers, polyolefin fibers such as polyethylene and polypropylene, polyvinylidene chloride fibers, polyvinyl chloride fibers, etc. can be used.
上記強酸可溶性繊維と強酸及び強アルカリ非溶解繊維と
は0.5〜90重量部、10〜99.5重量部の範囲で
混合して通常の抄紙法で抄紙し、得られた紙葉に熱処理
を施した後、この紙葉を強酸と作用させて紙葉中の強酸
可溶性繊維を溶解除去し、紙葉,中に適当な大きさの穴
又はミゾを形成することができる。The above-mentioned strong acid-soluble fibers and strong acid- and strong alkali-insoluble fibers are mixed in a range of 0.5 to 90 parts by weight, 10 to 99.5 parts by weight, and paper is made using a normal papermaking method, and the resulting paper sheets are heat-treated. After applying this process, the paper sheet is treated with a strong acid to dissolve and remove the strong acid-soluble fibers in the paper sheet, thereby forming holes or grooves of an appropriate size in the paper sheet.
そして紙葉中に形成させる穴等の大きさは混合抄紙した
強酸可溶性繊維の大きさによつてコントロールされ、穴
等の数は強酸可溶性繊維の配合割合によつてコントロー
ルされる。The size of the holes formed in the paper sheets is controlled by the size of the strong acid-soluble fibers mixed into paper, and the number of holes is controlled by the blending ratio of the strong acid-soluble fibers.
例えばセルロース繊維の一種である温帯針葉樹パルプの
平均繊維長は2.7〜3.6mm、平均径は32〜43
μであり、同じく温帯広葉樹パルプのそれは0.7〜1
.6mm、20〜40μであるが、これらを使い分ける
ことによつて容易、且つ自在にミクロン単位の穴等をコ
ントロールしながら形成することも可4能である。For example, temperate softwood pulp, a type of cellulose fiber, has an average fiber length of 2.7 to 3.6 mm and an average diameter of 32 to 43 mm.
μ, and that of temperate hardwood pulp is 0.7 to 1
.. 6 mm and 20 to 40 μm, but by using these appropriately, it is possible to easily and freely form holes in micron units, etc. while controlling the size.
また強酸可溶性繊維の配合割合を0.5〜90重量部の
範囲内で適宣に選択することによつて穴の数を適当にコ
ントロールすることが可能である。Further, by appropriately selecting the blending ratio of the strong acid-soluble fiber within the range of 0.5 to 90 parts by weight, it is possible to appropriately control the number of holes.
なお強酸可溶性繊維の配合割合が0.5重量部以下では
一般に穴形成の効果が殆んどなくなり、また強酸及び強
アルカリ非溶解繊維の配合割合が10重量部以下では一
般に強酸処理後のネツトワークが形成しにくい。また強
酸処理としては例えば75%(重量)硫酸浴中に混抄紙
を浸漬して行うことができ、濃硫酸処理後水洗し中和し
て硫酸を除去すればよい。If the blending ratio of strong acid-soluble fibers is less than 0.5 parts by weight, the hole-forming effect will generally be almost lost, and if the blending ratio of strong acid- and strong alkali-insoluble fibers is less than 10 parts by weight, the network after strong acid treatment will generally become weak. is difficult to form. The strong acid treatment can be carried out, for example, by immersing the mixed paper in a 75% (by weight) sulfuric acid bath, and after the concentrated sulfuric acid treatment, the sulfuric acid can be removed by washing with water and neutralizing it.
更に硫酸の水洗後ポリオレフイン繊維等からなる強酸及
び強アルカリ非溶解繊維のネツトワーク又はフイルムは
繊維の性質から水と馴じみにく・なるが、この場合は目
的に応じて界面活性剤を使用して紙葉表面の親水性を高
めるようにすればよい以上要するに、この発明によれば
強酸可溶性繊維の大きさ、配合割合を適宣に選択して配
合することにより穴の大きさ、数等を容易に、且つ自在
にコントロールすることができるので、適度の通気、通
液性を有する耐酸、耐アルカリ性紙葉を製造することが
できる。Furthermore, after washing with sulfuric acid, a network or film of strong acid- and strong alkali-insoluble fibers made of polyolefin fibers etc. will not be compatible with water due to the nature of the fibers, but in this case, a surfactant may be used depending on the purpose. In short, according to the present invention, the size and number of holes can be controlled by appropriately selecting and blending the size and blending ratio of strong acid-soluble fibers. Since it can be easily and freely controlled, it is possible to produce acid- and alkali-resistant paper sheets with appropriate ventilation and liquid permeability.
なおセルロース系パルプ等の強酸可溶性繊維と強酸及び
強アルカリ非溶解繊維との混抄紙を熱処理し、酸処理前
に一般のセルロース系パルプ鑑別用染色液例えばSel
leger染色液で染色すると、セルロース系パルプの
み染着してネツト状又はフイルム状となつたオレフイン
系繊維と容易に識別できる。Note that a mixed paper of strong acid-soluble fibers such as cellulose pulp and strong acid- and strong alkali-insoluble fibers is heat-treated, and before the acid treatment, a general staining solution for cellulose-based pulp identification, such as Sel.
When dyed with leger staining solution, it can be easily distinguished from olefin fibers, which are made of net-like or film-like fibers by dyeing only cellulose pulp.
これを酸処理すると、セルロース系パルプは除去され、
跡にパルプ繊維と概ね同じ大きさの穴又はミゾが顕微鏡
下で観察される。したがつて上記方法によれば強酸処理
によつて形成される穴の大きさ、数等をあらかじめ確認
することができる。以下、この発明の実施例を示す。When this is treated with acid, the cellulose pulp is removed,
Holes or grooves approximately the same size as the pulp fibers are observed under the microscope in the traces. Therefore, according to the above method, the size, number, etc. of holes formed by strong acid treatment can be confirmed in advance. Examples of this invention will be shown below.
実施例 1
ポリオレフイン系繊維(商品名SWPE−400、三井
ゼラパツク)85%(重量)と漂白広葉樹パルプ15%
(重量)を濃度0.02%で手抄シートマシンを用いて
目標坪量30g/m霊で抄紙した。Example 1 85% (by weight) polyolefin fiber (trade name SWPE-400, Mitsui Zerapack) and 15% bleached hardwood pulp
(weight) was made into paper using a hand sheet machine with a concentration of 0.02% and a target basis weight of 30 g/m.
次に105℃の円筒ドライヤーで乾燥して得られた紙葉
を120〜130℃の円筒ドライヤーにて熱プレスした
。これを75%硫酸浴中に投入し、60秒間放置した後
水洗して硫酸を除き、目的とする耐酸、耐アルカリ紙を
得ることができる。Next, the paper sheets obtained by drying with a cylindrical dryer at 105°C were hot pressed with a cylindrical dryer at 120 to 130°C. This is placed in a 75% sulfuric acid bath, left for 60 seconds, and then washed with water to remove the sulfuric acid, thereby obtaining the desired acid- and alkali-resistant paper.
この紙の性質は次の通りであつた。The properties of this paper were as follows.
註1JISP8124に記載される方法で測定註2JI
SP8118に記載される方法で測定註3JISP81
18に記載される方法で測定註4JISP8117に記
載される方法で測定註5K0H50%、70℃液中に2
時間浸漬註6H2S0475%、20℃液中に1時間浸
漬実施例 2ポリオレフイン系繊維(一般抄紙用ポリプ
ロピレン繊維2dX10mm)40%(重量)と漂白針
葉樹パルプ60%(重量)を円網抄紙機を用いて目標坪
量55g/m霊で抄造した。Note 1 Measured by the method described in JISP8124 Note 2 JI
Measured by the method described in SP8118 Note 3 JISP81
Measured by the method described in 18 Note 4 Measured by the method described in JISP8117 Note 5
Time Soaking Note 6 Soaking in 75% H2S04 solution at 20°C for 1 hour Example 2 40% (weight) of polyolefin fiber (polypropylene fiber for general paper making, 2 d x 10 mm) and 60% (weight) of bleached softwood pulp were mixed using a cylinder paper machine. The paper was made with a target basis weight of 55 g/m.
この紙を約165℃の2本の熱ロールで圧着して熱処理
を行ない、次いで75%濃硫酸中に3分間浸漬したのち
、水洗を行ない硫酸を除去した。得られた紙は荒い網状
を呈しており、優れた耐酸性と耐アルカリ性を有してい
た。この紙の性質は次の通りであった。なお紙質試験方
法は、実施例1と同様な方法で行なつた。This paper was heat-treated by pressing it with two heated rolls at about 165°C, then immersed in 75% concentrated sulfuric acid for 3 minutes, and then washed with water to remove the sulfuric acid. The obtained paper had a rough mesh shape and had excellent acid resistance and alkali resistance. The properties of this paper were as follows. Note that the paper quality test method was the same as in Example 1.
Claims (1)
ルカリ非溶解繊維10〜99.5重量部を混合抄紙し、
更に熱処理を施した後、強酸を作用させて強酸可溶性繊
維を溶解、除去してなる通気、通液性を有する耐酸、耐
アルカリ性紙。1. Making paper by mixing 0.5 to 90 parts by weight of strong acid-soluble fibers and 10 to 99.5 parts by weight of strong acid- and strong alkali-insoluble fibers,
After further heat treatment, a strong acid is applied to dissolve and remove the strong acid-soluble fibers to produce acid- and alkali-resistant paper with air permeability and liquid permeability.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3659681A JPS5953960B2 (en) | 1981-03-16 | 1981-03-16 | Acid- and alkali-resistant paper with breathability and liquid permeability |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3659681A JPS5953960B2 (en) | 1981-03-16 | 1981-03-16 | Acid- and alkali-resistant paper with breathability and liquid permeability |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57154498A JPS57154498A (en) | 1982-09-24 |
| JPS5953960B2 true JPS5953960B2 (en) | 1984-12-27 |
Family
ID=12474159
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3659681A Expired JPS5953960B2 (en) | 1981-03-16 | 1981-03-16 | Acid- and alkali-resistant paper with breathability and liquid permeability |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5953960B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63165598A (en) * | 1986-12-25 | 1988-07-08 | 株式会社 巴川製紙所 | Fluorocarbon fiber paper and its production |
-
1981
- 1981-03-16 JP JP3659681A patent/JPS5953960B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57154498A (en) | 1982-09-24 |
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