JPH02111484A - Production of highly water absorptive sheet - Google Patents
Production of highly water absorptive sheetInfo
- Publication number
- JPH02111484A JPH02111484A JP63262538A JP26253888A JPH02111484A JP H02111484 A JPH02111484 A JP H02111484A JP 63262538 A JP63262538 A JP 63262538A JP 26253888 A JP26253888 A JP 26253888A JP H02111484 A JPH02111484 A JP H02111484A
- Authority
- JP
- Japan
- Prior art keywords
- sheet
- water
- compsn
- dose
- flexible sheet
- 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.)
- Pending
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title abstract description 60
- 238000010894 electron beam technology Methods 0.000 claims abstract description 28
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims abstract description 21
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims abstract description 21
- 239000000835 fiber Substances 0.000 claims abstract description 16
- 239000012298 atmosphere Substances 0.000 claims abstract description 10
- 239000002904 solvent Substances 0.000 claims abstract description 9
- 239000000203 mixture Substances 0.000 claims description 35
- 239000000463 material Substances 0.000 claims description 32
- 239000002250 absorbent Substances 0.000 claims description 23
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 claims description 16
- 239000004033 plastic Substances 0.000 claims description 4
- 229920003023 plastic Polymers 0.000 claims description 4
- 230000001678 irradiating effect Effects 0.000 claims description 3
- 239000000178 monomer Substances 0.000 abstract description 37
- 238000010521 absorption reaction Methods 0.000 abstract description 35
- 150000003839 salts Chemical class 0.000 abstract 2
- 238000013329 compounding Methods 0.000 abstract 1
- 239000002985 plastic film Substances 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 58
- 239000002585 base Substances 0.000 description 22
- 230000002745 absorbent Effects 0.000 description 18
- 229940048053 acrylate Drugs 0.000 description 15
- 239000000126 substance Substances 0.000 description 15
- 238000006243 chemical reaction Methods 0.000 description 13
- 238000006116 polymerization reaction Methods 0.000 description 13
- 239000000758 substrate Substances 0.000 description 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 238000004132 cross linking Methods 0.000 description 9
- 239000011358 absorbing material Substances 0.000 description 8
- 238000001035 drying Methods 0.000 description 7
- 230000008569 process Effects 0.000 description 7
- 239000011347 resin Substances 0.000 description 7
- 229920005989 resin Polymers 0.000 description 7
- 230000005855 radiation Effects 0.000 description 6
- 239000007864 aqueous solution Substances 0.000 description 5
- -1 divinyl compound Chemical class 0.000 description 5
- 239000003505 polymerization initiator Substances 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 4
- 239000002202 Polyethylene glycol Substances 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 238000005470 impregnation Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 239000012299 nitrogen atmosphere Substances 0.000 description 4
- 239000003504 photosensitizing agent Substances 0.000 description 4
- 229920001223 polyethylene glycol Polymers 0.000 description 4
- 229920000642 polymer Polymers 0.000 description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 230000001133 acceleration Effects 0.000 description 3
- 239000003638 chemical reducing agent Substances 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 230000006378 damage Effects 0.000 description 3
- 230000009257 reactivity Effects 0.000 description 3
- 238000007711 solidification Methods 0.000 description 3
- 230000008023 solidification Effects 0.000 description 3
- PQUXFUBNSYCQAL-UHFFFAOYSA-N 1-(2,3-difluorophenyl)ethanone Chemical compound CC(=O)C1=CC=CC(F)=C1F PQUXFUBNSYCQAL-UHFFFAOYSA-N 0.000 description 2
- 229910052783 alkali metal Inorganic materials 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 235000011187 glycerol Nutrition 0.000 description 2
- 230000002209 hydrophobic effect Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 239000004745 nonwoven fabric Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 229940047670 sodium acrylate Drugs 0.000 description 2
- VAPQAGMSICPBKJ-UHFFFAOYSA-N 2-nitroacridine Chemical compound C1=CC=CC2=CC3=CC([N+](=O)[O-])=CC=C3N=C21 VAPQAGMSICPBKJ-UHFFFAOYSA-N 0.000 description 1
- 244000205754 Colocasia esculenta Species 0.000 description 1
- 235000006481 Colocasia esculenta Nutrition 0.000 description 1
- 241000244206 Nematoda Species 0.000 description 1
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000003655 absorption accelerator Substances 0.000 description 1
- 229940124532 absorption promoter Drugs 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000003125 aqueous solvent Substances 0.000 description 1
- 229910052728 basic metal Inorganic materials 0.000 description 1
- 150000003818 basic metals Chemical class 0.000 description 1
- 230000001588 bifunctional effect Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 159000000007 calcium salts Chemical class 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 125000004386 diacrylate group Chemical group 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003623 enhancer Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 238000005338 heat storage Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003002 lithium salt Inorganic materials 0.000 description 1
- 159000000002 lithium salts Chemical class 0.000 description 1
- 159000000003 magnesium salts Chemical class 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000012766 organic filler Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 159000000001 potassium salts Chemical class 0.000 description 1
- 230000003449 preventive effect Effects 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000012925 reference material Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000011232 storage material Substances 0.000 description 1
- 229920000247 superabsorbent polymer Polymers 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 239000002562 thickening agent Substances 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N triethylene glycol Chemical compound OCCOCCOCCO ZIBGPFATKBEMQZ-UHFFFAOYSA-N 0.000 description 1
- KAKZBPTYRLMSJV-UHFFFAOYSA-N vinyl-ethylene Natural products C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Orthopedics, Nursing, And Contraception (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
- Coating Of Shaped Articles Made Of Macromolecular Substances (AREA)
- Laminated Bodies (AREA)
- Absorbent Articles And Supports Therefor (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は高吸水性シートの製法、さらに詳しくは初期吸
水能の優れた高吸水性シートの製法に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a method for producing a super absorbent sheet, and more particularly to a method for producing a super absorbent sheet with excellent initial water absorption capacity.
従来の技術
水を多量に吸収し膨潤するいわゆる高吸水性物質は紙お
むつ、生理用品を始め、使い捨て雑1か、農園芸用等の
保水剤として使用されており、さらには汚泥の凝固剤あ
るいは結露防止剤として土木、建築関係方面にもその用
途が拡大されつつある。Conventional technology So-called super absorbent substances that absorb a large amount of water and swell are used in disposable diapers, sanitary products, disposable miscellaneous items, water retention agents for agricultural and horticultural purposes, etc., and are also used as sludge coagulants and dew condensation agents. Its use as a preventive agent is also expanding to civil engineering and construction-related fields.
この高吸水性物質は種々の形態で使用し得るが、シート
として使用されることが最も多い。This superabsorbent material can be used in a variety of forms, but is most often used as a sheet.
従来、吸水性物質をシート化するための方法はいくつか
提案されている。これらの方法をシート化する時点で分
けると、吸水性物質を製造した後にこれをシート化する
方法、および吸水性物質の製造とシート化とを同時に行
う方法がある。また、吸水性物質の製造法で分けると、
化学的反応を用いる方法とエネルギー線照射による反応
を用いる方法とがある。従って、シート化時点と吸水性
物質の製造法とを種々に組み合せた方法が提案されてい
る訳である。Conventionally, several methods have been proposed for forming a water-absorbing substance into a sheet. When these methods are divided into sheets, there are two methods: a method in which a water-absorbing substance is produced and then it is made into a sheet, and a method in which the production of a water-absorbing substance and the production into a sheet are carried out simultaneously. In addition, when divided by the manufacturing method of water-absorbing substances,
There are methods using chemical reactions and methods using reactions caused by energy ray irradiation. Therefore, methods have been proposed in which various combinations of the sheet-forming time and the manufacturing method of the water-absorbing substance are used.
まず、吸水性物質を製造し、しかる後何らかの手段でこ
れをシート化する方法は2つに大別される。第1の方法
においては、基材と組み合せてシート化する。すなわち
、高分子吸水性物質を粉末状、粒子状等とし、これをシ
ート状の基材に付与して固着化処理を行う。第2の方法
においては、繊維状とした吸水性物質をシート化する。First, there are two methods for producing a water-absorbing material and then forming it into a sheet by some means. In the first method, it is combined with a base material to form a sheet. That is, the polymeric water-absorbing substance is made into powder, particles, etc., and is applied to a sheet-like base material to perform a fixing treatment. In the second method, a fibrous water-absorbing substance is formed into a sheet.
第1の方法の方がより一般的であり、この方法では吸水
性物質を製造する工程とそれをシート上に固着させろ工
程とを必要とする。固着方法としては、基材シートに粉
末状吸水性物質を散布し、これに別のシートを重ねてか
らエンボス加工を施す方法、若干量の水分を与えて粉末
状吸水性物質をわずかにゲル化してからエンボス加工し
、強固な固着を実現しようとするいわゆる湿式法(特開
昭54125293号、特開昭51−40497号、特
開昭54−141099号、および特開昭583645
2号参照)、あるいは高吸水性物質、樹脂バインダーお
よび溶媒よりなる樹脂配合物を幇材に塗布し、溶媒を揮
散させて該基材上に皮膜を形成するコーティング方法(
特開昭5111−1ot047号参照)などがある。し
かしながら、シート状吸水性物質を得るためのこれらの
方法にはいくつか問題点があった。例えば、第1の方法
においては、粉末状や粒子状の吸水性物質の製造工程お
よびシートの製造工程と別個の工程を必要とするために
工程が複雑になること、あるいはシート化工程における
加工が意外に困難であること、また、第2の方法におい
ては、コスト高となることあるいは得られる吸水性シー
トの吸水能が低いことなどが挙げられる。The first method is more common and requires the steps of manufacturing the water-absorbing material and fixing it onto the sheet. The fixing method is to sprinkle the powdered water-absorbing material onto the base sheet, layer it with another sheet, and then emboss it, or add a small amount of moisture to slightly gel the powdered water-absorbing material. The so-called wet method (JP-A-54125293, JP-A-51-40497, JP-A-54-141099, and JP-A-583645)
(see No. 2), or a coating method in which a resin compound consisting of a highly water-absorbent substance, a resin binder, and a solvent is applied to the roof material, and the solvent is evaporated to form a film on the base material (
(See Japanese Patent Application Laid-Open No. 5111-1ot047). However, these methods for obtaining sheet-like water-absorbing materials have some problems. For example, in the first method, the process becomes complicated because it requires separate processes from the manufacturing process of powdered or particulate water-absorbing material and the manufacturing process of the sheet, or the processing in the sheeting process is difficult. In addition, in the second method, the cost is high and the water absorbing capacity of the resulting water absorbent sheet is low.
次に、以上の方法とは異なり、シート状基材上で単量体
を直接重合することにより吸水性物質の製造とシート化
とを同時に行おうとする方法がいくつか提案されている
。例えば、アクリル酸塩系の単量体溶液を基材に含浸さ
せ、これにラノカル重合開始剤またはそれと還元剤との
混合物を霧状で添加して重合を行う方法がある(特開昭
60149609号参照)。しかしながら、この方法に
おいては重合開始剤の均2分散が困難であって均一な重
合物が得られず、その結果単量体が多く残存することに
なり品質に劣る。その他に、単量体、重合開始剤および
還元剤等を均一に混合し、これを基材に霧状で付与して
重合を行う方法(特開昭62−53309号参照)、同
様な方法において少債の架橋剤を用いる方法(特開昭6
2−62829号参照)、同様な方法において還元剤の
みを後から添加する方法(特開昭62−97979号参
照)などが提案されている。しかしながら、これらの方
法はいずれも次のような欠点を有する。Next, unlike the above-mentioned methods, several methods have been proposed in which the production of a water-absorbing substance and the formation of a sheet are simultaneously performed by directly polymerizing monomers on a sheet-like base material. For example, there is a method in which polymerization is carried out by impregnating a base material with an acrylate monomer solution and adding a Lanocal polymerization initiator or a mixture of it and a reducing agent in the form of a mist (Japanese Patent Laid-Open No. 60149609). reference). However, in this method, it is difficult to uniformly disperse the polymerization initiator, and a uniform polymer cannot be obtained. As a result, a large amount of monomer remains, resulting in poor quality. In addition, a method in which monomers, a polymerization initiator, a reducing agent, etc. are uniformly mixed and the mixture is applied to a base material in the form of a mist to perform polymerization (see JP-A No. 62-53309), and a similar method. Method using a crosslinking agent for small bonds (Japanese Patent Application Laid-Open No. 1983
2-62829), and a similar method in which only the reducing agent is added afterwards (see Japanese Patent Laid-Open No. 62-97979). However, all of these methods have the following drawbacks.
すなわち、重合開始剤(触媒)を用いるので重合後に重
合開始剤か残存し、また、単量体も多く残存する可能性
がある。加えて、これらの方法で利用する化学的反応は
一般に反応の制御が難しい。従って、本発明における如
く反応の制御を精度よ(行うことはできず、得られる吸
水性シートの吸水能を調節するのは困難である。That is, since a polymerization initiator (catalyst) is used, some of the polymerization initiator remains after polymerization, and there is a possibility that a large amount of monomer also remains. In addition, the chemical reactions utilized in these methods are generally difficult to control. Therefore, it is not possible to precisely control the reaction as in the present invention, and it is difficult to adjust the water absorption capacity of the resulting water absorbent sheet.
さらに、シート状基材上で単量体を化学的に重合した後
、放射線を照射することによって吸水性シートに残留す
る単量体を減少させようとする方法が提案されている(
特開昭63−10638号参照)。しかしながら、この
方法も用いる反応が化学的重合であるがゆえに触媒残存
等の欠点を有し、その上、放射線照射により単量体を減
少させることができても、放射線照射によって架橋反応
等が起こり化学的重合後の吸水能に変化が生じるなどし
て最終吸水性シートの品質をコントロールするのが困難
である。Furthermore, a method has been proposed in which monomers are chemically polymerized on a sheet-like substrate and then irradiated with radiation to reduce the monomers remaining on the water-absorbing sheet (
(See Japanese Patent Application Laid-open No. 10638/1983). However, since the reaction used in this method is chemical polymerization, it has drawbacks such as residual catalyst, and even if monomers can be reduced by radiation irradiation, crosslinking reactions etc. occur due to radiation irradiation. It is difficult to control the quality of the final water absorbent sheet due to changes in water absorption capacity after chemical polymerization.
化学的重合を用いる方法以外の方法としては、アクリル
酸塩とジビニル系化合物に光増感剤を添加し、紫外線を
照射して重合させるという方法が提案されている(特開
昭63−43912号参照)。As a method other than chemical polymerization, a method has been proposed in which a photosensitizer is added to an acrylate and a divinyl compound, and the mixture is polymerized by irradiation with ultraviolet light (Japanese Patent Laid-Open No. 63-43912). reference).
しかしながら、この方法では光増感剤が残存するという
難点があり、光増感剤の毒性が懸念される場合は、生理
用ナプキン、紙おむつなど身体に直接接触させて使用す
る用品への適用には大きな問題となる。However, this method has the disadvantage that the photosensitizer remains, and if there is a concern about the toxicity of the photosensitizer, it cannot be applied to products that are used in direct contact with the body, such as sanitary napkins and disposable diapers. It becomes a big problem.
最後に、シート状基打上で単m体を重合させるために放
射線照射による反応を用いる方法がある。Finally, there is a method in which a reaction by radiation irradiation is used to polymerize the monomer on a sheet-like substrate.
特表昭57−500546号には、アクリル酸系型m体
水溶液を繊維基材上に付与し、放射線を十分に照射して
これを高吸水性ポリマーに変化させる方法か開示されて
いる。この方法は、残存すると害を及ぼすおそれがある
触媒等を用いていない点、放射線を用いる点等に萌記諸
方法よりも進歩が認められる。しかしながら、「十分な
照射」を行うと一般に架橋反応が進んだものとなり、生
成する吸水性物質の膨潤を妨げることとなって結果的に
吸水能が著しく劣るものになり、いわゆる「高吸水性」
ソートは得られない。ましてや、この方法では本発明に
おける如く吸水能を任意の所望レベルに調節することは
できない。また、この方法においては単量体が多く残存
することら考えられる。Japanese Patent Publication No. 57-500546 discloses a method of applying an acrylic acid type m-form aqueous solution onto a fiber base material and converting it into a superabsorbent polymer by sufficiently irradiating it with radiation. This method is more advanced than the Moeki methods in that it does not use catalysts that may cause harm if they remain, and it uses radiation. However, when ``sufficient irradiation'' is performed, the crosslinking reaction generally progresses, which hinders the swelling of the resulting water-absorbing substance, resulting in a significantly inferior water-absorbing ability, resulting in what is called ``high water absorption''.
You don't get the sort. Furthermore, this method does not allow the water absorption capacity to be adjusted to any desired level as in the present invention. It is also considered that in this method, a large amount of monomer remains.
以上述べた如く、高吸水性シート製造に関する従来法は
、種々の問題点を有していた。As described above, the conventional methods for producing superabsorbent sheets have various problems.
かかる背景下、本発明者らは特定モル比範囲のアクリル
酸およびアクリル酸塩単量体を特定濃度範囲で含む該単
m体の水性組成物を、シート状の基材上で、特定線1範
囲の電子線照射によって重合・硬化させることよりなる
電子線照射を利用した高吸水性シートの優れた製法発明
を完成するに至り、既に特許出願した(特開昭63−1
05044号参照)。この方法においては、選択した特
定範囲の単量体モル比、単量体の組成物中濃度および電
子線照射条件を組み合せることにより始めて高吸水能が
得られるものであり、この吸水能は前記した粉末状吸水
性物質のシート化方法等と同等かまたはそれを上まわる
。また、この方法はほとんど単一工程であるので工程的
にも同じく粉末状吸水性物質のシート化方法等より優れ
ている。Against this background, the present inventors applied an aqueous composition containing acrylic acid and acrylate monomers in a specific molar ratio range in a specific concentration range to a specific line 1 on a sheet-like base material. We have completed the invention of an excellent manufacturing method for super absorbent sheets using electron beam irradiation, which involves polymerization and curing by electron beam irradiation within a range, and have already filed a patent application (Japanese Patent Laid-Open No. 63-1
(See No. 05044). In this method, high water absorption capacity can only be obtained by combining the selected specific range of monomer molar ratio, monomer concentration in the composition, and electron beam irradiation conditions. This method is equivalent to or better than the sheet-forming method of powdered water-absorbing material. Furthermore, since this method involves almost a single step, it is also superior in terms of process to the method of forming a powdery water-absorbing material into a sheet.
さらには、触媒・光増感剤を使用しないのでそれらが残
存するという問題ら全くないというものであった。Furthermore, since catalysts and photosensitizers are not used, there is no problem of their remaining.
特開昭63−105044号の製法はこのように優れた
ものであるが、結果的に高吸水能は達成されるものの、
吸水能を所望のレベルに精度よく調節することはできな
かった。そこで、本発明者らはかかる問題点を解決すべ
く研究を続行した結果、(線ff1)’/(線量率戸な
る制御因子を用いて照射条件を規定することに裏り目的
を達成できろことを見い出し、これについても既に特許
出願した(特願昭63−202236号)。The manufacturing method of JP-A No. 63-105044 is thus excellent, but although it achieves high water absorption capacity as a result,
It was not possible to precisely adjust the water absorption capacity to the desired level. Therefore, as a result of continuing research to solve this problem, the inventors of the present invention found that the purpose could be achieved by defining the irradiation conditions using the control factor of (line ff1)'/(dose rate). They discovered this and have already filed a patent application for this (Japanese Patent Application No. 1983-202236).
発明か解決しようとする課題
前記の如く、本発明者らは基材上でアクリル酸およびア
クリル酸塩単量体に電子線を照射することをベースとす
る高吸水性シートの製法について一連の開発を行ってき
たが、特開昭63−105044号および特願昭612
02236号の製法には共通する未解決課題が存在して
いた。すなわち、両製法においては、主として水溶液よ
りなる水性組成物を基材に付与し、その状態で電子線を
照射するので、■かなりの水分が含まれているため、電
子線照射時に水分が蒸発し、それが照射設備内の冷却部
等で結露して被照射体に水滴が付着する恐れがある、■
水分にも電子線が吸収されるので余分な照射電圧および
線量が必要になるといった工程的問題点、あるいは水性
組成物が、基材が形成する間隙を埋めて保持された状態
で電子線が照射される結果、硬化・生成した樹脂も基材
が形成していた間隙を埋めることとなり、もともと基材
が有していた毛細管現象による吸水能が損なわれ、吸水
性シートとして使用する場合に吸水初期の吸水能力が劣
るといった品質的問題である。Invention or Problem to be Solved As mentioned above, the present inventors have made a series of developments regarding a method for producing a super absorbent sheet based on irradiating acrylic acid and acrylate monomers with electron beams on a substrate. 1986-105044 and Japanese Patent Application No. 612
The manufacturing method of No. 02236 had a common unresolved problem. In other words, in both manufacturing methods, an aqueous composition mainly consisting of an aqueous solution is applied to the substrate and the electron beam is irradiated in that state, so that the water content evaporates during the electron beam irradiation because it contains a considerable amount of water. , there is a risk that it may condense in the cooling section of the irradiation equipment and cause water droplets to adhere to the irradiated object.■
There are process problems such as the need for extra irradiation voltage and dose because the electron beam is absorbed by water, or the electron beam is irradiated with the aqueous composition filling the gap formed by the base material. As a result, the hardened and produced resin also fills the gaps formed by the base material, impairing the base material's original water absorption ability due to capillary action, and when used as a water absorbent sheet, the initial water absorption This is a quality problem such as poor water absorption ability.
課題を解決するための手段
かかる情況下、本発明者らはさらに鋭意研究を重ねた結
果、水性組成物を基材に付与した後、旦乾燥により溶媒
を除去することにより基材の間隙をある程度再生した形
態で組成物を固化仕しめ、次いで特定範囲の相対湿度下
で調湿して改めて水分を与え、しかる後に電子線を照射
すると、間隙を喪失することなく硬化反応が起こり、し
かも比表面積の大きな樹脂が硬化生成することを見い出
し、本発明を完成するに至った。Means for Solving the Problems Under these circumstances, the inventors of the present invention have conducted further intensive research and have found that after applying an aqueous composition to a substrate, the solvent can be removed by drying to reduce the gaps in the substrate to a certain extent. When the composition is solidified in the regenerated form, then rehydrated by controlling the relative humidity within a specific range, and then irradiated with an electron beam, the curing reaction occurs without loss of voids, and the specific surface area is reduced. It has been discovered that a resin with a large amount of resin is produced by curing, and the present invention has been completed.
すなわち、本発明は、(a)モル比50:50〜0:1
00のアクリル酸およびアクリル酸塩を主成分とする単
m体水性組成物を可撓性シートに付与し、
(b)該組成物の溶媒を実質的に除去して固化せしめ、
(c)相対湿度40〜98%の雰囲気中にて該固化物1
00重量部に対し3〜50重量部の水分を吸湿させ、次
いで
(d)該吸湿状態で(線量)3/(線量率)2が0,0
07〜5 、5 M rad−see2である電子線を
照射することにより硬化させることを特徴とする高吸水
性シートの製法を提供するものである。That is, the present invention provides (a) a molar ratio of 50:50 to 0:1;
00 acrylic acid and acrylate as main components to a flexible sheet, (b) substantially removing the solvent of the composition and solidifying it, (c) The solidified product 1 in an atmosphere with a humidity of 40 to 98%
00 parts by weight of moisture, and then (d) in this hygroscopic state, (dose) 3/(dose rate) 2 is 0.0.
The present invention provides a method for producing a highly water-absorbent sheet, characterized in that the sheet is cured by irradiation with an electron beam of 07-5, 5 M rad-see2.
本発明における基材たる可撓性シートとしては、可撓性
であって、単m体水性組成物を付与した後乾燥して固化
させた場合にある程度の間隙が再生できるように本来的
に間隙を有するものであればL)lれも使用できる。か
かる可撓性シートの例としては、繊維集合体、ゴムもし
くはプラスチックの多孔質シート、ゴムらしくはプラス
チックのネット、金属箔、金属のネット等が挙げられ、
ことに良好な間隙性と可撓性や強度等より繊維集合体が
好ましい。繊維には親水性繊維、疎水性繊維があるが、
吸水速度の観点からは親水性繊維の法が、吸水時のシー
トの強度の観点からは疎水性繊維の方がすぐれ、目的・
用途に応じて適宜選択できる。The flexible sheet serving as the base material in the present invention is flexible and inherently has gaps so that a certain amount of gaps can be regenerated when the monomolecular aqueous composition is applied and then dried and solidified. Any one having L) can be used. Examples of such flexible sheets include fiber aggregates, porous sheets of rubber or plastic, rubber-like plastic nets, metal foils, metal nets, etc.
In particular, fiber aggregates are preferable because of their good porosity, flexibility, strength, etc. Fibers include hydrophilic fibers and hydrophobic fibers,
The method using hydrophilic fibers is better from the viewpoint of water absorption speed, but the method using hydrophobic fibers is superior from the viewpoint of the strength of the sheet when water is absorbed.
It can be selected as appropriate depending on the purpose.
本発明の製法により得られる高吸水性シートは前記の如
き可撓性シートと吸水性樹脂とが不可分的に一体となっ
たものであるが、かかる高吸水性シートを製造するに当
っては、まず単量体水性組成物を調製する。ここに、本
明細書中にいう「単量体水性組成物」とは、特定の単量
体の水溶液あるいは所望によりこれに他の成分を加えた
しのである。従って、水性組成物における溶媒は水が主
体ではあるが、後記する乾燥・固化工程で水と共に除去
できる低沸点非水溶媒も混合して使用できる。The super absorbent sheet obtained by the manufacturing method of the present invention is an inseparable integral body of the above-described flexible sheet and water absorbent resin, but in manufacturing such a super absorbent sheet, First, a monomer aqueous composition is prepared. Here, the "monomer aqueous composition" as used herein refers to an aqueous solution of a specific monomer or to which other components are added as desired. Therefore, although water is the main solvent in the aqueous composition, a low-boiling non-aqueous solvent that can be removed together with water in the drying/solidification process described later can also be used in combination.
単量体としてはアクリル酸とアクリル酸塩を用いろ。ア
クリル酸塩としてはナトリウム塩、カリウム塩、リチウ
ム塩の如きアルカリ金属塩、カルシウム塩、マグネシウ
ム塩の如きアルカリ土類金属塩等が挙げられるが、好ま
しくはアルカリ金属塩を用いる。単量体の水性組成物は
所定量のアクリル酸、アクリル酸塩および水を混合する
ことによって調製できる。あるいは所定量のアクリル酸
、塩基性金属水酸化物および水を混合し、アクリル酸の
一部を中和してアクリル酸塩に変換することによっても
調製できる。また、この水性組成物に別種の単量体を少
量添加して後の電子線照射時における硬化反応を調整す
ることも可能である。かかる調整用型In体としては、
水性組成物に対して混和適性をaするらのであればよく
、とりわけ水溶性の二官性単量体、例えばポリエチレン
グリコールノアクリレート、N、N”−メチレンビスア
クリルアミド等が好適に用いられる。さらには、所望に
より、着色剤や無機もしくは有機充填剤等を添加4−ろ
ことらてきるし、水性組成物の液性を改iりして基材へ
の付与を容易とする目的でポリビニルアルコール、ポリ
エチレンオキサイドの如き増粘剤やあるいは界面活性剤
を添加することしできろ。Use acrylic acid and acrylate as monomers. Examples of the acrylate include alkali metal salts such as sodium salts, potassium salts, and lithium salts, alkaline earth metal salts such as calcium salts and magnesium salts, and preferably alkali metal salts are used. Aqueous compositions of the monomers can be prepared by mixing amounts of acrylic acid, acrylate, and water. Alternatively, it can also be prepared by mixing predetermined amounts of acrylic acid, a basic metal hydroxide, and water, and neutralizing a portion of the acrylic acid to convert it into an acrylate. It is also possible to add a small amount of another type of monomer to this aqueous composition to adjust the curing reaction during subsequent electron beam irradiation. As such an In body for adjustment,
Any water-soluble bifunctional monomer may be used as long as it has miscibility with the aqueous composition, and water-soluble difunctional monomers such as polyethylene glycol noacrylate, N,N''-methylenebisacrylamide, etc. are particularly preferably used. If desired, colorants, inorganic or organic fillers, etc. may be added to the aqueous composition, and polyvinyl alcohol may be added to change the liquid properties of the aqueous composition to make it easier to apply to the substrate. , thickeners such as polyethylene oxide, or surfactants may be added.
水性組成物を調製するに当っては、主として後記する電
子線照射時の反応性からの要請により、アクリル酸とア
クリル酸塩のモル比は50:50〜O:100の範囲と
する。アクリル酸の割合がこの範囲より大きいと、後の
乾燥工程にてアクリル酸の蒸発量が増加して不適当であ
る。なお、モル比が98〜100では反応性が相対的に
低下するので、かかるモル比は70〜98の範囲が好ま
しい。In preparing the aqueous composition, the molar ratio of acrylic acid and acrylate is in the range of 50:50 to 0:100, mainly due to the reactivity during electron beam irradiation described later. If the proportion of acrylic acid is larger than this range, the amount of evaporation of acrylic acid will increase in the subsequent drying process, which is inappropriate. In addition, since the reactivity is relatively reduced when the molar ratio is 98 to 100, the molar ratio is preferably in the range of 70 to 98.
次に、かく調製した単量体水性組成物を基材たろ可撓性
シートに付与する。付与方法としては、塗布法、含浸法
、スプレー法、プリンティング法等が挙げられるが、空
隙性の基材ゆえに殊に含浸法が好ましい。The monomer aqueous composition thus prepared is then applied to the base taro flexible sheet. Examples of the application method include a coating method, an impregnation method, a spray method, and a printing method, but the impregnation method is particularly preferred because of the porous base material.
かかる付与後、乾燥して実質的に溶媒を除去する。乾燥
は通常加熱法による。溶媒除去により同化が起こるが、
固化に際して組成物の体積が減少して基材が元来有して
いた間隙がある程度復元される。観察すると、例えば基
材が繊維である場合、固化物は1本1本の繊維に沿って
粒状の形状をなし、一部結晶状となっているのが認めら
れる。After such application, drying substantially removes the solvent. Drying is usually done by heating. Assimilation occurs due to solvent removal;
Upon solidification, the volume of the composition decreases and some of the original porosity of the substrate is restored. When observed, for example, when the base material is fiber, it is observed that the solidified material has a granular shape along each fiber, and some portions are crystalline.
固化に続いて、相対湿度40〜98%の雰囲気中で調湿
し、固化物に改めて水分を付与する。このように水分付
与は気相にて行ない、固化物の形態を損う恐れのある水
中浸漬は適当でない。固化組成物に含有させるべき水分
mは該固化組成物100重量部に対して3〜50重量部
、好ましくは5〜40重量部の範囲とする。3重1部未
満だと電子線照射時の反応性が低下して目的を達成する
ことができなくなり、一方、501量部を越えると潮解
現象により固化物の空隙を保持した形態が崩れて液状に
近い状態となり不適当である。Following solidification, the humidity is controlled in an atmosphere with a relative humidity of 40 to 98% to rehydrate the solidified product. In this way, moisture is added in the gas phase, and immersion in water is not appropriate as it may damage the form of the solidified product. The amount of water m to be contained in the solidified composition is in the range of 3 to 50 parts by weight, preferably 5 to 40 parts by weight, based on 100 parts by weight of the solidified composition. If the amount of triplex is less than 1 part, the reactivity during electron beam irradiation will decrease, making it impossible to achieve the purpose.On the other hand, if it exceeds 501 parts, the solidified material will lose its void-retaining form due to deliquescence and become liquid. This is inappropriate because the situation is close to .
なお、調湿時間については、用いるアクリル酸塩の種類
により、乾燥後の吸湿能にかなりの差があるので注意を
要する。すなわち、アクリル酸カリウムの場合は吸湿能
が高いので、通常の雰囲気(20〜30℃、相対湿度5
0〜70%)で数分〜十数分、高湿度雰囲気(30〜4
0℃、相対湿度80〜95%)では数分以内の放置で十
分である。Note that with regard to the humidity conditioning time, care must be taken as the moisture absorption capacity after drying varies considerably depending on the type of acrylate used. In other words, potassium acrylate has a high hygroscopic ability, so it can be used in a normal atmosphere (20-30°C, relative humidity 5.
0 to 70%) for several minutes to more than ten minutes in a high humidity atmosphere (30 to 4%).
At 0° C. and relative humidity of 80 to 95%), it is sufficient to leave it for a few minutes or less.
これに対し、アクリル酸ナトリウムの場合は、吸湿能が
低く、単量体組成物に吸湿促進剤を添加しておくのが好
ましい。かかる吸湿促進剤としては、イオン性のものは
得られる吸水性シートの吸水能に影響を与えるので非イ
オン性のものが好ましい。On the other hand, in the case of sodium acrylate, the moisture absorption ability is low, and it is preferable to add a moisture absorption promoter to the monomer composition. As such a moisture absorption accelerator, a nonionic one is preferable since an ionic one affects the water absorption ability of the resulting water absorbent sheet.
非イオン性の吸湿促進剤の例としては、グリセリン、エ
ヂレングリコール、トリエチレングリコールまたはポリ
エチレングリコール等のごとき6機物、シリカゲルまた
は活性アルミナ等のごとき無機粉末が挙げられる。Examples of nonionic moisture absorption enhancers include glycerin, ethylene glycol, triethylene glycol, polyethylene glycol, and the like, and inorganic powders such as silica gel and activated alumina.
、1llll湿が終了すると、水分を保持させた状態で
電子線を照射する、照射条件は、(線量)3/(線量率
)′が0.007〜5,5Mrad−sec”の範囲内
で選択する。特願昭63−202236号において詳細
に述べられている如く、(線量)3/(線m率)2の制
御因子により、硬化後に得られる吸水性シートの吸水能
レベルを任意に変更することができる。この場合、線量
が同一でも、線量率が高い場合よりも低い場合の方が重
合および架橋反応が起こり、吸水性は低くなるという関
係にある。ここに、線量率は単位時間当たりの線量であ
り(連続照射の場合は線1を被照射物が電子線帯を通過
する時間、すなわち照射時間で除した値で表わす)V時
間の単位として秒を用いると、線型率−線量/時間[M
rad/sec]であるから、(線ff1)3/(線量
率)1[Mrad3/ (M rad/ 5ec)’l
−= (線f!り’/(線量7時間戸(線量)・(時
間)’[Mrad−sec’lと書き換えることができ
る。従って、線量と照射時間とで制御すると考えてもよ
い。, After 1llll wetness is completed, electron beam is irradiated with moisture retained.The irradiation conditions are selected within the range of (dose) 3/(dose rate)' from 0.007 to 5.5 Mrad-sec. As described in detail in Japanese Patent Application No. 63-202236, the water absorbing capacity level of the water absorbent sheet obtained after curing is arbitrarily changed by the control factor of (dose) 3/(linear m ratio) 2. In this case, even if the dose is the same, polymerization and crosslinking reactions occur more when the dose rate is low than when the dose rate is high, resulting in lower water absorption.Here, the dose rate is (In the case of continuous irradiation, it is expressed as the value obtained by dividing the ray 1 by the time it takes for the irradiated object to pass through the electron beam band, that is, the irradiation time.) If seconds are used as the unit of V time, linear rate - dose / Time [M
rad/sec], so (line ff1)3/(dose rate)1[Mrad3/ (M rad/ 5ec)'l
-= (line f!ri'/(dose 7 hours (dose)·(time)'[Mrad-sec'l). Therefore, it may be considered that the dose and irradiation time are controlled.
具体的な値との関係を言えば、(線ff1)3/(線量
率)!の値が0.007未満であると硬化が不十分とな
り、一方、5.5を越えると架橋が進みすぎて吸水能が
低下してくるのみならず基材に損傷を与える恐れがある
ので不適当である。しかしながら、照射速度を重視する
場合は線量を少し高く設定してその分だけ線量を高く、
すなわち照射速度を高くしてやればよい。以上より、電
子線照射に当っては、l)アクリル酸塩の種類、2)ア
クリル酸とアクリル酸塩の比率、3)吸湿水分率、4)
架橋促進用添加剤の種類および量等の吸水能に関与する
要因を考慮して条件設定すべきである。なお、照射電圧
は特に限定されるものではないが、一般には150〜3
000KVの範囲とする。基材を含めた被照射物の厚み
等に応じ、それを十分に透過するような電圧を前記範囲
から選択すればよい。The relationship with specific values is (line ff1)3/(dose rate)! If the value is less than 0.007, curing will be insufficient, while if it exceeds 5.5, crosslinking will proceed too much, which will not only reduce the water absorption capacity but also cause damage to the base material. Appropriate. However, if irradiation speed is important, set the dose a little higher and increase the dose accordingly.
In other words, the irradiation speed may be increased. From the above, in electron beam irradiation, the following factors are considered: l) type of acrylate, 2) ratio of acrylic acid to acrylate, 3) moisture absorption rate, 4)
Conditions should be set in consideration of factors related to water absorption capacity, such as the type and amount of the crosslinking promoting additive. Note that the irradiation voltage is not particularly limited, but is generally 150 to 3
000KV range. Depending on the thickness of the object to be irradiated including the base material, a voltage that sufficiently transmits the object may be selected from the above range.
照射雰囲気は大気中でしよいが、好ましくは不活性ガス
、例えば窒素雰囲気中で行う。The irradiation atmosphere may be in the air, but is preferably carried out in an inert gas, for example, nitrogen atmosphere.
電子線照射により単重体の重合・架橋が起こる。Polymerization and crosslinking of single polymers occur due to electron beam irradiation.
アクリル酸およびアクリル酸塩単量体は一官能性であり
、通常の重合反応では水可溶性の線状ポリマーしか得ら
れない。従って、水によって膨潤する程度の高吸水性ポ
リマーを得るには重合以外に架橋が必要であり、高吸水
性が実現されるにはかかる重合と架橋との間の適度なバ
ランスが必須である。本発明において高吸水性のシート
が得られるのは、比較的低線虫における前記条件での電
子線照射により、この重合と架橋とがバランスよく起こ
っていること、および反応に発熱が伴わず、反応を制御
性よく行うことができるためであろう。Acrylic acid and acrylate monomers are monofunctional, and conventional polymerization reactions yield only water-soluble linear polymers. Therefore, in order to obtain a highly water-absorbent polymer that swells with water, crosslinking is required in addition to polymerization, and an appropriate balance between such polymerization and crosslinking is essential to achieve high water absorbency. In the present invention, a highly water-absorbent sheet can be obtained because the polymerization and crosslinking occur in a well-balanced manner by electron beam irradiation under the above conditions in a relatively low nematode population, and the reaction does not generate heat. This is probably because the reaction can be carried out with good controllability.
かくして、電子線照射後に得られる高吸水性シートは、
ある程度の空隙を残存さ仕っつ硬化した樹脂が基材と一
体となったものであり、その結果比表面積が大きく、使
用に当っては初期の吸水能にすぐれるという特徴を有す
る。Thus, the superabsorbent sheet obtained after electron beam irradiation is
The resin is cured with a certain amount of voids remaining and is integrated with the base material, resulting in a large specific surface area and an excellent initial water absorption capacity during use.
本発明の製法による高吸水性シートは空隙性基材の種類
を適宜選択することによって種々の形態のシートとする
ことができ、生理用品、おむつ、使い捨て雑巾を始め、
農園芸材料、建築関係材料、土木関係材料、保冷・蓄熱
材料等、幅広い分野に使用することができる。The superabsorbent sheet produced by the manufacturing method of the present invention can be made into sheets of various shapes by appropriately selecting the type of porous base material, and can be used for sanitary products, diapers, disposable rags, etc.
It can be used in a wide range of fields, including agricultural and horticultural materials, construction-related materials, civil engineering-related materials, and cold and heat storage materials.
以下に実施例を挙げて本発明をさらに詳しく説明する。The present invention will be explained in more detail with reference to Examples below.
実施例
実施例!
アクリル酸72.0gと水酸化カリウム53.2gを含
む水酸化カリウム水溶液144.2gとを混合すること
により単量体水溶液を調製した。この単量体水溶液にお
いては、アクリル酸とアクリル酸塩とのモル比は5:9
5、全単量体濃度は50重1%である。Examples Examples! An aqueous monomer solution was prepared by mixing 72.0 g of acrylic acid and 144.2 g of an aqueous potassium hydroxide solution containing 53.2 g of potassium hydroxide. In this monomer aqueous solution, the molar ratio of acrylic acid and acrylate is 5:9.
5. The total monomer concentration is 50% by weight.
次いで、繊維長56m1.3デニールの部分融着した目
付40g/m”のポリエステル繊維よりなる不織布の基
材に対し、調製した単量体水溶液を含浸させて付着11
41g/m”とした。Next, a nonwoven fabric base material made of partially fused polyester fibers with a fiber length of 56 m and a 1.3 denier and a basis weight of 40 g/m'' was impregnated with the prepared monomer aqueous solution and attached 11
41 g/m''.
含浸後、105℃の乾燥器内で8分間乾燥して単量体組
成物を繊維基材上で固化せしめ、次いで20℃、相対湿
度65%の雰囲気中に10分間放置して吸湿させ、その
状態で直ちに日新ハイボルテージ(株)製エリアビーム
型電子線加速装置を用い、窒素雰囲気中にて、加速電圧
200KV、線量2Mrad、線量率12 、8 M
rad/ sec、 (線量)3/(線量率)”= 0
、049 Mrad−see”の条件で電子線照射を
行って高吸水性シートを得た。なお、照射直前の固化物
の水分量は乾燥した単量体組成物の重量に対して41%
であった。After impregnation, the monomer composition was dried for 8 minutes in a dryer at 105°C to solidify it on the fiber substrate, and then left in an atmosphere of 20°C and 65% relative humidity for 10 minutes to absorb moisture. Immediately, using an area beam type electron beam accelerator manufactured by Nissin High Voltage Co., Ltd., in a nitrogen atmosphere, the acceleration voltage was 200 KV, the dose was 2 Mrad, and the dose rate was 12.8 M.
rad/sec, (dose)3/(dose rate)”=0
, 049 Mrad-see'' conditions to obtain a super absorbent sheet.The water content of the solidified product immediately before irradiation was 41% of the weight of the dried monomer composition.
Met.
かくして得られた本発明の製法による高吸水性シートは
吸水能がシート全体に対し350倍、高吸水性物質に対
し680倍であり、しかも初期吸水能にすぐれた高品質
のものであった(吸水能で用いる倍率は基準物重重に対
して吸水された水の重量が何倍であるかを表わすもので
ある)。また、電子線照射時に結露は認められなかった
。The superabsorbent sheet produced by the method of the present invention thus obtained had a water absorption capacity of 350 times that of the entire sheet and 680 times that of the superabsorbent material, and was of high quality with excellent initial water absorption capacity ( The magnification used in water absorption capacity indicates how many times the weight of absorbed water is relative to the weight of the reference material.) Further, no dew condensation was observed during electron beam irradiation.
実施例2
アクリル酸72.0g、水酸化ナトリウム38゜Ogを
含む水酸化ナトリウム水溶113111.3g。Example 2 72.0 g of acrylic acid and 113111.3 g of an aqueous sodium hydroxide solution containing 38° Og of sodium hydroxide.
分子量600のポリエヂレングリコールジアクリレート
02gおよびグリセリン10.5gとを混合することに
より単量体水性組成物を調製した。この単量体水性組成
物においては、アクリル酸とアクリル酸ナトリウムとの
モル比は5:95、全単量体濃度は35重量%である。A monomer aqueous composition was prepared by mixing 02 g of polyethylene glycol diacrylate having a molecular weight of 600 and 10.5 g of glycerin. In this monomer aqueous composition, the molar ratio of acrylic acid to sodium acrylate is 5:95, and the total monomer concentration is 35% by weight.
この組成物を実施例1と同じ基材に付着量として62g
/11’となるように含浸させ、105℃の乾燥器内で
10分間乾燥して該組成物を繊維基材上で固化せしめ、
次いで20℃、相対湿度65%の雰囲気中で30分間吸
湿させ、その状態で直ちに日新ハイボルテージ(昧)製
エリアビーム型電子線加速装置を用い、窒素雰囲気中に
て、加速電圧200KV、線量5Mrac!、線量率3
2 、1 Mrad/sec、(線m)3/(線量率)
”= 0 、 I 22 Mrad ・sec’の条件
にて電子線照射を行って高吸水性シートを得た。なお、
照射直前の固化物の水分量は乾燥した単量体組成物重量
に対して17.6%であった。This composition was deposited on the same substrate as in Example 1 in an amount of 62 g.
/11' and dried in a dryer at 105° C. for 10 minutes to solidify the composition on the fiber base material,
Next, moisture was absorbed for 30 minutes in an atmosphere of 20°C and relative humidity of 65%, and in that state, the area beam type electron beam accelerator manufactured by Nissin High Voltage was immediately used in a nitrogen atmosphere at an acceleration voltage of 200 KV and a dose 5 Mrac! , dose rate 3
2, 1 Mrad/sec, (line m)3/(dose rate)
A super absorbent sheet was obtained by electron beam irradiation under the conditions of "= 0, I 22 Mrad sec'.
The moisture content of the solidified product immediately before irradiation was 17.6% based on the weight of the dried monomer composition.
かくして本発明の製法により得られた高吸水性シートは
吸水能がシート全体に対し125倍、高吸水性物質に対
し350倍であり、しかし初期吸水能にすぐれた高品質
のものであった。また、電子線照射時に結露は認められ
なかった。Thus, the superabsorbent sheet obtained by the manufacturing method of the present invention had a water absorption capacity of 125 times that of the entire sheet and 350 times that of the superabsorbent material, but was of high quality with excellent initial water absorption capacity. Further, no dew condensation was observed during electron beam irradiation.
比較例1(乾燥せずに溶液状で照射した場合)実施例2
と同一の不織布を用い、これに下記組成の単量体水溶液
を付着量が60g/m”となるように含浸させた。Comparative example 1 (when irradiated in solution form without drying) Example 2
Using the same nonwoven fabric as above, it was impregnated with an aqueous monomer solution having the following composition so that the amount of adhesion was 60 g/m''.
成分 量
アクリル酸 72g水酸化ナトリ
ウム 32gポリエチレングリコール
ジアク 0.2gリレート(分子量600)
水 1 1
og含浸後直ちに実施例1と同じ電子線照射装置を用い
、窒素雰囲気中で、加速電圧200KV、線ffi 2
M rad、線量率5 、38 Mrad/see、
(線量)3/(線ff141)”= 0 、27 M
rad−see’の条件下テ電子線を照射し、次いで1
05℃で3分間乾燥して高吸水性シートを得た。このも
のはシート全体に対して120倍の吸水能を有するもの
であった。Ingredients Quantity Acrylic acid 72g Sodium hydroxide 32g Polyethylene glycol diac 0.2g Lylate (molecular weight 600) Water 1 1
Immediately after the og impregnation, using the same electron beam irradiation device as in Example 1, in a nitrogen atmosphere, an acceleration voltage of 200 KV, a beam ffi 2
Mrad, dose rate 5, 38 Mrad/see,
(Dose) 3/(line ff141)” = 0, 27 M
irradiation with electron beam under rad-see' conditions, then 1
It was dried at 05°C for 3 minutes to obtain a super absorbent sheet. This material had a water absorption capacity 120 times that of the entire sheet.
本発明の製法による実施例2のシートと比較例1のシー
トとはほぼ同程度の吸水能を有する。しかしながら、添
付図面の第1図から明らかなごとく、本発明の製法によ
る実施例2のシートは、比較例1のシートよりも初期吸
水速度が大きく、初期吸水能に優れることが判明した。The sheet of Example 2 produced by the manufacturing method of the present invention and the sheet of Comparative Example 1 have approximately the same water absorption capacity. However, as is clear from FIG. 1 of the accompanying drawings, the sheet of Example 2 produced by the manufacturing method of the present invention had a higher initial water absorption rate than the sheet of Comparative Example 1, and was found to be superior in initial water absorption capacity.
発明の効果
本発明の製法により、基材に対し高吸水性物質が粒状に
付着して間隙が多くなるため初期吸水能にすぐれ、かつ
所望する吸水能レベルの高吸水性シートが得られるよう
になり、また、電子tajjl射時に設備内における結
露がなく、余分な水の蒸発エネルギーか不要となって照
射効率が向上するという工程的改善もなされた。Effects of the Invention By the manufacturing method of the present invention, the superabsorbent substance adheres to the base material in granular form, increasing the number of gaps, so that it is possible to obtain a superabsorbent sheet that has excellent initial water absorption ability and has the desired water absorption ability level. Furthermore, process improvements have been made in that there is no dew condensation within the equipment during electron irradiation, eliminating the need for extra water evaporation energy, and improving irradiation efficiency.
第1図は本発明の製法による実施例2の吸水性シートと
比較例1の対照シートについて、吸水量の時間変化を比
較したグラフである。FIG. 1 is a graph comparing the change in water absorption amount over time for the water absorbent sheet of Example 2 produced by the manufacturing method of the present invention and the control sheet of Comparative Example 1.
Claims (4)
酸およびアクリル酸塩を主成分とする単1体水性組成物
を可撓性シートに付与し、(b)該組成物の溶媒を実質
的に除去して固化せしめ、(c)相対湿度40〜98%
の雰囲気中にて該固化物100重量部に対し3〜50重
量部の水分を吸湿させ、次いで(d)該吸湿状態にて(
線量)^3/(線量率)^2が0.007〜5.5Mr
ad・sec^2である電子線を照射することにより硬
化させることを特徴とする高吸水性シートの製法。(1) (a) Applying a single aqueous composition containing acrylic acid and acrylate as main components in a molar ratio of 50:50 to 0:100 to a flexible sheet, and (b) providing a solvent for the composition. (c) a relative humidity of 40 to 98%;
3 to 50 parts by weight of moisture is absorbed per 100 parts by weight of the solidified material in an atmosphere of (d) in the hygroscopic state (
Dose)^3/(dose rate)^2 is 0.007 to 5.5Mr
A method for producing a highly water-absorbent sheet, characterized by curing it by irradiating it with an electron beam of ad.sec^2.
する特許請求の範囲第(1)項記載の製法。(2) The manufacturing method according to claim (1), wherein the flexible sheet is a fiber aggregate.
シートであることを特徴とする特許請求の範囲第(1)
項記載の製法。(3) Claim No. (1) characterized in that the flexible sheet is a porous sheet of rubber or plastic.
Manufacturing method described in section.
であることを特徴とする特許請求の範囲第(1)項記載
の製法。(4) The manufacturing method according to claim (1), wherein the flexible sheet is a rubber or plastic net.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63262538A JPH02111484A (en) | 1988-10-18 | 1988-10-18 | Production of highly water absorptive sheet |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63262538A JPH02111484A (en) | 1988-10-18 | 1988-10-18 | Production of highly water absorptive sheet |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02111484A true JPH02111484A (en) | 1990-04-24 |
Family
ID=17377198
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63262538A Pending JPH02111484A (en) | 1988-10-18 | 1988-10-18 | Production of highly water absorptive sheet |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02111484A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6807702B2 (en) | 1999-11-12 | 2004-10-26 | Kimberly-Clark Worldwide, Inc. | Cleaning system and apparatus |
| WO2018037816A1 (en) * | 2016-08-25 | 2018-03-01 | デクセリアルズ株式会社 | Method for producing hydrous water absorbent sheet |
-
1988
- 1988-10-18 JP JP63262538A patent/JPH02111484A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6807702B2 (en) | 1999-11-12 | 2004-10-26 | Kimberly-Clark Worldwide, Inc. | Cleaning system and apparatus |
| WO2018037816A1 (en) * | 2016-08-25 | 2018-03-01 | デクセリアルズ株式会社 | Method for producing hydrous water absorbent sheet |
| JP2018030308A (en) * | 2016-08-25 | 2018-03-01 | デクセリアルズ株式会社 | Method for producing water-containing water-absorbent sheet |
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