JPH0660262B2 - Method for treating porous body and apparatus for treating porous body - Google Patents
Method for treating porous body and apparatus for treating porous bodyInfo
- Publication number
- JPH0660262B2 JPH0660262B2 JP1170879A JP17087989A JPH0660262B2 JP H0660262 B2 JPH0660262 B2 JP H0660262B2 JP 1170879 A JP1170879 A JP 1170879A JP 17087989 A JP17087989 A JP 17087989A JP H0660262 B2 JPH0660262 B2 JP H0660262B2
- Authority
- JP
- Japan
- Prior art keywords
- porous body
- continuous pores
- polymer precursor
- filter paper
- gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title claims description 7
- 239000011148 porous material Substances 0.000 claims description 46
- 229920000642 polymer Polymers 0.000 claims description 38
- 239000002243 precursor Substances 0.000 claims description 24
- 239000003595 mist Substances 0.000 claims description 9
- 239000007788 liquid Substances 0.000 claims description 7
- 238000007664 blowing Methods 0.000 claims description 5
- 230000000379 polymerizing effect Effects 0.000 claims description 4
- 239000007789 gas Substances 0.000 description 12
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 9
- 239000007921 spray Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 239000004745 nonwoven fabric Substances 0.000 description 5
- 239000004744 fabric Substances 0.000 description 4
- 239000000178 monomer Substances 0.000 description 4
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 239000006260 foam Substances 0.000 description 3
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 description 2
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 2
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- MBHRHUJRKGNOKX-UHFFFAOYSA-N [(4,6-diamino-1,3,5-triazin-2-yl)amino]methanol Chemical compound NC1=NC(N)=NC(NCO)=N1 MBHRHUJRKGNOKX-UHFFFAOYSA-N 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- SUPCQIBBMFXVTL-UHFFFAOYSA-N ethyl 2-methylprop-2-enoate Chemical compound CCOC(=O)C(C)=C SUPCQIBBMFXVTL-UHFFFAOYSA-N 0.000 description 2
- 239000002657 fibrous material Substances 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- PQUXFUBNSYCQAL-UHFFFAOYSA-N 1-(2,3-difluorophenyl)ethanone Chemical compound CC(=O)C1=CC=CC(F)=C1F PQUXFUBNSYCQAL-UHFFFAOYSA-N 0.000 description 1
- OEPOKWHJYJXUGD-UHFFFAOYSA-N 2-(3-phenylmethoxyphenyl)-1,3-thiazole-4-carbaldehyde Chemical compound O=CC1=CSC(C=2C=C(OCC=3C=CC=CC=3)C=CC=2)=N1 OEPOKWHJYJXUGD-UHFFFAOYSA-N 0.000 description 1
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N Acrylic acid Chemical class OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- DKPFZGUDAPQIHT-UHFFFAOYSA-N Butyl acetate Natural products CCCCOC(C)=O DKPFZGUDAPQIHT-UHFFFAOYSA-N 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical compound CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 description 1
- BWGVNKXGVNDBDI-UHFFFAOYSA-N Fibrin monomer Chemical class CNC(=O)CNC(=O)CN BWGVNKXGVNDBDI-UHFFFAOYSA-N 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- VGGLHLAESQEWCR-UHFFFAOYSA-N N-(hydroxymethyl)urea Chemical class NC(=O)NCO VGGLHLAESQEWCR-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 229920005830 Polyurethane Foam Polymers 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 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
- 229920003180 amino resin Polymers 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000002781 deodorant agent Substances 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 238000011033 desalting Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000246 fibrin derivative Substances 0.000 description 1
- FUZZWVXGSFPDMH-UHFFFAOYSA-N hexanoic acid Chemical compound CCCCCC(O)=O FUZZWVXGSFPDMH-UHFFFAOYSA-N 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- FQPSGWSUVKBHSU-UHFFFAOYSA-N methacrylamide Chemical compound CC(=C)C(N)=O FQPSGWSUVKBHSU-UHFFFAOYSA-N 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- ZIUHHBKFKCYYJD-UHFFFAOYSA-N n,n'-methylenebisacrylamide Chemical compound C=CC(=O)NCNC(=O)C=C ZIUHHBKFKCYYJD-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- PNJWIWWMYCMZRO-UHFFFAOYSA-N pent‐4‐en‐2‐one Natural products CC(=O)CC=C PNJWIWWMYCMZRO-UHFFFAOYSA-N 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 239000003505 polymerization initiator Substances 0.000 description 1
- 239000011496 polyurethane foam Substances 0.000 description 1
- 229940047670 sodium acrylate Drugs 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- UBOXGVDOUJQMTN-UHFFFAOYSA-N trichloroethylene Natural products ClCC(Cl)Cl UBOXGVDOUJQMTN-UHFFFAOYSA-N 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
Landscapes
- Filtering Materials (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は濾紙、不織布、編織物、焼結体、発泡体等の連
続気孔を有する多孔体の処理方法に関するものであり、
該多孔体は主としてフィルターとして使用される。The present invention relates to a method for treating a porous body having continuous pores such as filter paper, non-woven fabric, knitted fabric, sintered body and foam.
The porous body is mainly used as a filter.
濾紙、不織布、編織物、焼結体、発泡体等の連続気孔を
有する多孔体は主としてフィルターとして用いられてい
るが、上記多孔体の連続気孔の孔径は一般に5μ以上で
あるが、最近の電子工業等では更に微細な濾過を行なう
必要性が高まり、1μ以下更には0.1μ以下の微細孔
径の連続気孔を有する多孔体が要求されている。しかし
ながらこれら多孔体の連続気孔の孔径を小さくすること
は極めて困難であった。例えば濾紙、不織布、編織物等
の繊維材料では使用する繊維の径を小さくすればよい
が、繊維の径を小さくするには限度があるし、焼結体等
では焼結体を構成する粒子径を小さくすればよいが、粒
子径を小さくすることにも限度がある。また発泡体にお
いては連続気孔の径の調節は極めて困難である。したが
って微細濾過にあっては、止むを得ず価格の非常に高い
特殊な繊維素誘導体やプラスチックからなる微細連続気
孔を有する多孔体を使用しているのが現状である。Porous bodies having continuous pores such as filter paper, non-woven fabric, knitted fabric, sintered body, and foamed body are mainly used as filters. The pore diameter of the continuous pores of the porous body is generally 5 μm or more. In industry and the like, there is a growing need to carry out finer filtration, and a porous body having continuous pores with a fine pore size of 1 μm or less, further 0.1 μm or less is required. However, it is extremely difficult to reduce the pore size of the continuous pores of these porous bodies. For example, in the case of fibrous materials such as filter paper, non-woven fabric, knitted fabric, etc., the diameter of the fiber to be used can be made small, but there is a limit to making the diameter of the fiber small. Can be reduced, but there is also a limit to reducing the particle size. Further, in the foam, it is extremely difficult to control the diameter of the continuous pores. Therefore, in the fine filtration, the present situation is to use a porous body having fine continuous pores made of special fibrin derivative or plastic which is unavoidably expensive.
本発明は上記従来の課題を解決するための手段として、
連続気孔(2)を有する多孔体(1)に液状のポリマー前駆体
の霧滴(3)を混合して気体を圧送通過せしめ、該多孔体
(1)の連続気孔(2)の壁面(2)Aに該霧滴(3)を該気体の送
通圧によって流拡せしめることによって該ポリマー前駆
体を塗布した後、高分子化させてポリマーとすることに
よって該連続気孔(2)の孔径を縮小しかつ均一化する多
孔体(1)の処理方法を提供するものであり、更に多孔体
(1)が設置される処理室と、該処理室内に連絡する送風
手段(12)と、該多孔体(1)の送風手段(12)連絡側に挿着
されているポリマー前駆体の霧化手段(13)とからなる多
孔体(1)の処理装置を提供するものである。The present invention, as a means for solving the above conventional problems,
The porous body (1) having continuous pores (2) is mixed with mist droplets (3) of a liquid polymer precursor to force gas to pass therethrough, and the porous body
The polymer precursor is applied by spreading the fog droplets (3) on the wall surface (2) A of the continuous pores (2) A of (1) by the pressure of the gas, and then polymerized to give a polymer. By providing a method for treating a porous body (1), which reduces the pore size of the continuous pores (2) and makes the pores uniform.
A processing chamber in which (1) is installed, a blowing means (12) communicating with the processing chamber, and atomization of a polymer precursor inserted on the blowing means (12) communication side of the porous body (1) A treatment device for a porous body (1) comprising means (13) is provided.
本発明で用いられる連続気孔(2)を有する多孔体(1)と
は、上記したように濾紙、不織布、編織物等の繊維材
料、焼結体のような粒子固結体、無機あるいは有機の発
泡体である。The porous body (1) having continuous pores (2) used in the present invention is, as described above, a filter paper, a non-woven fabric, a fiber material such as a knitted fabric, a particle solidified body such as a sintered body, an inorganic or organic material. It is a foam.
本発明に用いられるポリマー前駆体とはメチルメタクリ
レート、エチルメタクリレート、メチルアクリレート、
エチルアクリレート、アクリル酸塩類、メタクリルアミ
ド、アクリルアミド、スチレン、アクリロニトリル、塩
化ビニル、塩化ビニリデン、酢酸ビニル等のビニル単量
体やメチロールメラミン、メチル化メチロール尿素等の
アミノプラスト単量体等の単量体、上記単量体のオリゴ
マー、フェノールプレポリマー、エポキシプレポリマ
ー、ウレタンプレポリマー等のプレポリマーである。The polymer precursor used in the present invention is methyl methacrylate, ethyl methacrylate, methyl acrylate,
Monomers such as ethyl acrylate, acrylic acid salts, methacrylamide, acrylamide, styrene, acrylonitrile, vinyl chloride, vinylidene chloride, vinyl acetate and other vinyl monomers and methylolmelamine, methylated methylolurea and other aminoplast monomers. And prepolymers such as oligomers of the above monomers, phenol prepolymers, epoxy prepolymers, and urethane prepolymers.
上記ポリマー前駆体は液状のものはそのまゝ、あるいは
トルオール、キシロール、酢酸エチル、酢酸ブチル、ア
セトン、メチルエチルケトン、メタノール、エタノー
ル、トリクロルエチレン、n−ヘキサン、水等の溶剤の
単独または二種以上の混合溶剤に溶解させた溶液として
用いられる。上記例示は本発明を限定するものではな
く、本発明においては広範囲なポリマー前駆体および溶
剤が用いられる。The above-mentioned polymer precursor is a liquid one as it is, or a solvent such as toluene, xylol, ethyl acetate, butyl acetate, acetone, methyl ethyl ketone, methanol, ethanol, trichloroethylene, n-hexane, water, etc., alone or in combination of two or more kinds. It is used as a solution dissolved in a mixed solvent. The above examples are not meant to limit the invention and a wide range of polymer precursors and solvents are used in the invention.
更に上記ポリマー前駆体には重合開始剤、硬化剤、増感
剤等が添加され、その他可塑剤、染料、あるいは目的に
よって消臭剤、還元剤、酸化剤等の処理剤を混合しても
よい。Furthermore, a polymerization initiator, a curing agent, a sensitizer, etc. may be added to the above-mentioned polymer precursor, and a plasticizer, a dye, or a treating agent such as a deodorant, a reducing agent or an oxidizing agent may be mixed depending on the purpose. .
本発明においては連続気孔(2)を有する多孔体(1)に空
気、窒素、アルゴン等の望ましくは不活性な気体を送通
し、該気体にスプレー(13)等によりポリマー前駆体の霧
滴(3)を混合する。In the present invention, air, nitrogen, preferably an inert gas such as argon is passed through the porous body (1) having continuous pores (2), and the gas (spray (13) or the like of the polymer precursor is sprayed to the gas (13). Mix 3).
このようにして該多孔体(1)の連続気孔(2)の壁面(2)A
にはポリマー前駆体が塗布されるが、該ポリマー前駆体
は加熱、光照射、水分接触等の高分子化手段によってポ
リマーとされる。In this way, the wall surface (2) A of the continuous pores (2) of the porous body (1)
A polymer precursor is applied to the polymer precursor, and the polymer precursor is made into a polymer by a polymerizing means such as heating, light irradiation, and water contact.
本発明の作用を第1図〜第3図により説明する。図にお
いて(1)は多孔体、(2)は該多孔体(1)の連続気孔であ
る。該多孔体(1)に第1図に示すように矢印方向から気
体を圧送通過せしめる。該気体にはポリマー前駆体の霧
滴(3)を混合すると、該霧滴(3)は多孔体(1)の連続気孔
(2)の入口に付着するが、第2図に示すように気体の送
通圧に押されて連続気孔(2)内に流拡して該連続気孔(2)
の壁面(2)A(例えば濾紙であれば濾紙を構成するパル
プ繊維の周壁面)に液膜を形成する。その後該高分子化
手段によってポリマー前駆体の液膜を高分子化してポリ
マーとすれば、第3図に示すように多孔体(1)の連続気
孔(2)の壁面(2)Aはポリマー層(5)に被覆され、したが
って多孔体(1)の連続気孔(2)の径は縮小されるポリマー
層(5)の厚さは気体に対する霧滴(3)の混合量や該霧滴
(3)を混合した気体の送通量で調節され得るから連続気
孔(2)の孔径を所望の径に縮小することが出来る。そし
て多孔体(1)の連続気孔(2)の孔径は一般にバラツキがあ
るけれども、連続気孔(2)の孔径の大きなものは気体の
通過抵抗が小さいから優先的に霧滴(3)を混合した気体
が通過し、その結果孔径の大きな連続気孔(2)から壁面
(2)Aに液膜が形成されて行く。かくして連続気孔(2)は
孔径を縮小されるとともにバラツキが均一化されるので
ある。The operation of the present invention will be described with reference to FIGS. In the figure, (1) is a porous body and (2) is continuous pores of the porous body (1). Gas is forced to pass through the porous body (1) in the direction of the arrow as shown in FIG. When the polymer precursor mist droplets (3) are mixed with the gas, the mist droplets (3) form continuous pores of the porous body (1).
Although it adheres to the inlet of (2), it is pushed by the gas transmission pressure and spreads into the continuous pores (2) as shown in FIG.
A liquid film is formed on the wall surface (2) A (for example, in the case of a filter paper, the peripheral wall surface of the pulp fibers constituting the filter paper). After that, when the liquid film of the polymer precursor is polymerized by the polymerizing means to form a polymer, the wall surface (2) A of the continuous pores (2) of the porous body (1) is a polymer layer as shown in FIG. The diameter of the continuous pores (2) of the porous body (1) is reduced by being covered with (5), and the thickness of the polymer layer (5) is the mixing amount of the mist droplets (3) with respect to the gas or the mist droplets.
Since the amount of gas mixed with (3) can be adjusted, the diameter of the continuous pores (2) can be reduced to a desired diameter. And the pore diameter of the continuous pores (2) of the porous body (1) generally varies, but the large pore diameter of the continuous pores (2) has a small gas passage resistance, so the fog droplets (3) are preferentially mixed. As a result of the passage of gas, the continuous pores (2) with a large pore size are
(2) A liquid film is formed on A. Thus, the diameter of the continuous pores (2) is reduced and the variations are made uniform.
したがって本発明においては、多孔体の連続気孔の孔径
をポリマー層によって所定の径に縮小しかつ均一化する
ことが極めて容易に可能であり、微細濾過用の多孔質体
を非常に安価に提供出来る。また多孔体がポリマー層に
よって補強されかつ耐薬品性を向上させたり脱臭作用、
脱塩作用、イオン交換作用等を与えることも出来る。Therefore, in the present invention, it is possible to extremely easily reduce the pore size of the continuous pores of the porous body to a predetermined diameter by the polymer layer and make it uniform, and it is possible to provide the porous body for microfiltration at a very low cost. . In addition, the porous body is reinforced by the polymer layer and improves chemical resistance and deodorizing action,
It can also provide a desalting action, an ion exchange action, and the like.
本発明を第4図に示す一実施例によって説明すれば、(1
1)は内部に処理室を形成したガイド筒であり、該ガイド
筒(11)の根端部には送風手段である送風機(12)が配さ
れ、中間には霧化手段であるスプレーガン(13)が挿入さ
れ、先端部にはクリップ(14)が取付けられ、該クリップ
(14)に多孔体(1)が支持される。そして該送風機(12)を
作動させて矢印に示すように空気を該多孔体(1)に送通
し、スプレーガン(13)より該空気中にポリマー前駆体の
霧滴(3)を混合する。このようにして多孔体(1)に霧滴
(3)を混合した空気を送通すると第1図〜第3図に示す
プロセスによって多孔体(1)の連続気孔(2)の壁面(2)A
にポリマー層(5)が形成される。The present invention will be described with reference to an embodiment shown in FIG.
Reference numeral 1) is a guide cylinder having a processing chamber formed therein, a blower (12) which is a blower is arranged at the root end of the guide cylinder (11), and a spray gun (atomizing means) is provided in the middle. 13) is inserted, and the clip (14) is attached to the tip,
The porous body (1) is supported by (14). Then, the blower (12) is operated to blow air through the porous body (1) as shown by the arrow, and the spray gun (13) mixes the mist droplets (3) of the polymer precursor into the air. In this way, fog droplets are formed on the porous body (1).
When the air mixed with (3) is passed through, the wall surface (2) A of the continuous pores (2) of the porous body (1) is processed by the process shown in FIGS. 1 to 3.
A polymer layer (5) is formed on the surface.
上記多孔体(1)としては例えば下記のものが採用され
る。For example, the following is adopted as the porous body (1).
濾紙 ポリエステル不織布 アルミナ焼結体 ポリウレタン発泡体 上記ポリマー前駆体としては例えば下記のものが採用さ
れる。Filter Paper Polyester Nonwoven Fabric Alumina Sintered Body Polyurethane Foam Body As the polymer precursor, for example, the following ones are adopted.
(a) ウレタンプレポリマー 50 重量部 メチルエチルケトン 50 〃 (b) メチロールメラミン 25 重量部 硬化剤 0.5 〃 メタノール 60 〃 水 14.5〃 (c) エチルメタクリレート 80 重量部 酢酸エチル 20 〃 アゾビスイソブチロニトリル 0.3 〃 (d) エリスリットテトラメタクリレート 30 重量部 増感剤 0.3 〃 メチルエチルケトン 70 〃 (e) アクリル酸ソーダ 30 重量部 澱粉 10 重量部 N-Nメチレンビスアクリルアミド 0.3 〃 アンモニウムパースルフェイト 0.3 〃 水 60 〃 上記ポリマー前駆体を多孔体(1)の連続気孔(2)の壁面
(2)Aに塗布したあと、(a)は乾燥後水分を接触させ、
(b)は70℃で20分加熱し、(c)は常温でアニリンの霧滴
を混合した気体を送通し、(d)は乾燥後紫外線を照射
し、(e)は80℃で10分加熱して各々高分子化せしめ
られる。なお(e)のポリマー層は吸水性を有し吸水層と
して使用される。(a) Urethane prepolymer 50 parts by weight Methyl ethyl ketone 50 〃 (b) Methylol melamine 25 parts by weight Curing agent 0.5 〃 Methanol 60 〃 Water 14.5 〃 (c) Ethyl methacrylate 80 parts by weight Ethyl acetate 20 〃 Azobisisobuty Ronitrile 0.3 〃 (d) Erislit tetramethacrylate 30 parts by weight Sensitizer 0.3 〃 Methyl ethyl ketone 70 〃 (e) Sodium acrylate 30 parts by weight Starch 10 parts by weight NN Methylenebisacrylamide 0.3 〃 Ammonium Perth Fate 0.3 〃 Water 60 〃 The above polymer precursor is added to the wall of the continuous pores (2) of the porous body (1)
(2) After applying to A, (a) is dried and then contacted with water,
(b) is heated at 70 ℃ for 20 minutes, (c) is a gas mixed with mist drops of aniline at room temperature, (d) is irradiated with ultraviolet rays after drying, (e) is at 80 ℃ for 10 minutes Each is polymerized by heating. The polymer layer (e) has a water absorbing property and is used as a water absorbing layer.
上記実施例において多孔体(1)もを面積1m2、孔径6
μの連続気孔(2)を有する濾紙を用い、ポリマー前駆
体(a)を用いた場合、本発明の処理によって濾紙の連
続気孔の孔径は下表のように縮小される。In the above embodiment, the porous body (1) also has an area of 1 m 2 and a pore size of 6
When a filter paper having μ continuous pores (2) is used and the polymer precursor (a) is used, the pore size of the continuous pores of the filter paper is reduced by the treatment of the present invention as shown in the table below.
本発明において多孔体(1)として濾紙を用いる場合には
通常第5図に示すようなサポーター(21)を用いる。該サ
ポーター(21)は多孔筒体(22)と該多孔筒体(22)の両端に
形成されるフランジ(23),(24)とからなる。該サポータ
ー(21)には第6図に示すようにつづら折りした濾紙(1)
が支持され、該サポーター(21)の多孔筒体(22)の一端に
は栓(25)が嵌着される。したがって本発明の処理方法は
第7図に示すように多孔体である濾紙(1)をサポーター
(21)に支持した状態で実施されてもよい。即ち濾紙(1)
を支持したサポーター(21)を複数個内部に処理室を形成
したチャンバー(31)内に収容し、該サポーター(21)の開
口端をチャンバー(31)の支板(32)の連絡口(33)にセット
して送風手段である送風ポンプ(35)の吸引側に連絡する
吸引経路(34)とチャンバー(31)の底部に接続し、該送風
ポンプ(35)の吐出側に連絡する送風経路(36)はチャンバ
ー(31)の側面に接続し、該送風経路(36)の途中には霧化
手段であるポリマー前駆体のスプレーガン(37)が挿入さ
れる。 When a filter paper is used as the porous body (1) in the present invention, a supporter (21) as shown in FIG. 5 is usually used. The supporter (21) comprises a porous cylinder (22) and flanges (23) and (24) formed at both ends of the porous cylinder (22). The supporter (21) has a filter paper (1) folded and folded as shown in FIG.
Is supported, and a plug (25) is fitted to one end of the porous cylindrical body (22) of the supporter (21). Therefore, according to the treatment method of the present invention, as shown in FIG. 7, the filter paper (1) which is a porous body is supported.
It may be carried out while being supported by (21). That is, filter paper (1)
A plurality of supporters (21) supporting the above are housed in a chamber (31) having a processing chamber formed therein, and the open ends of the supporters (21) are connected to a communication port (33) of a support plate (32) of the chamber (31). ) And a suction path (34) communicating with the suction side of the blower pump (35) which is a blowing means, and a ventilation path connected to the bottom of the chamber (31) and communicating with the discharge side of the blower pump (35) (36) is connected to the side surface of the chamber (31), and a spray gun (37) of a polymer precursor, which is an atomizing means, is inserted in the air passage (36).
上記構成において送風ポンプ(35)を作動させればチャン
バー(31)内の空気はサポーター(21)に支持されている濾
紙(1)を通してサポーター(21)内に流入し吸引経路(34)
を介して送風ポンプ(35)の吸収側に吸引され、送風側よ
り吐出されて送風経路(36)を介してチャンバー(31)に送
風される。このように濾紙(1)を通して空気をチャンバ
ー(31)、吸引経路(34)、送風ポンプ(35)、送風経路(36)
と循環させつゝ送風経路(36)のスプレーガン(37)からポ
リマー前駆体をスプレーしてポリマー前駆体の霧滴(3)
を該空気に混合する。かくして第1図〜第3図に示すよ
うな機構で濾紙(1)の連続気孔(2)の壁面(2)Aにポリマ
ー前駆体を塗布した後所定の高分子化手段によりポリマ
ー層が形成成される。When the blower pump (35) is operated in the above structure, the air in the chamber (31) flows into the supporter (21) through the filter paper (1) supported by the supporter (21) and the suction path (34).
The air is sucked into the absorption side of the blower pump (35) through the air blower, is discharged from the blower side, and is blown into the chamber (31) through the blower path (36). In this way, air is passed through the filter paper (1) into the chamber (31), the suction path (34), the blower pump (35), and the blower path (36).
Spray the polymer precursor from the spray gun (37) of the air flow path (36) to spray the polymer precursor (3)
Is mixed with the air. Thus, after applying the polymer precursor to the wall surface (2) A of the continuous pores (2) of the filter paper (1) by the mechanism shown in FIGS. 1 to 3, the polymer layer is formed by a predetermined polymerizing means. To be done.
第1図〜第3図はポリマー層形成過程の説明図であり、
第1図は霧滴付着状態、第2図は液膜形成状態、第3図
はポリマー層形成状態を示し、第4図は本発明に用いら
れる装置の一実施例の説明図、第5図は濾紙サポーター
の斜視図、第6図は該サポーターに濾紙を取付けた状態
の斜視図、第7図は濾紙を取付けたサポーターに本発明
の処理を行なう場合の説明図である。 図中、(1)……多孔体、(2)……連続気孔、(2)A……壁
面、 (3)……霧滴、(5)……ポリマー層 (12),(35)……送風手段(送風機) (13),(37)……霧化手段(スプレーガン)1 to 3 are explanatory views of the polymer layer forming process,
FIG. 1 shows a state in which fog droplets are attached, FIG. 2 shows a state in which a liquid film is formed, FIG. 3 shows a state in which a polymer layer is formed, and FIG. 4 is an explanatory view of an embodiment of an apparatus used in the present invention, and FIG. FIG. 6 is a perspective view of a filter paper supporter, FIG. 6 is a perspective view of the supporter with a filter paper attached, and FIG. 7 is an explanatory view when the treatment of the present invention is performed on the supporter with a filter paper attached. In the figure, (1) ... porous body, (2) ... continuous pores, (2) A ... wall surface, (3) ... fog, (5) ... polymer layer (12), (35) ... … Blower means (blower) (13), (37) …… Atomizing means (spray gun)
Claims (2)
前駆体の霧滴を混合した気体を圧送通過せしめ、該多孔
体の連続気孔の壁面に該霧滴を該気体の送通圧によって
流拡せしめることによって該ポリマー前駆体を塗布した
後、高分子化させてポリマーとすることによって該連続
気孔の孔径を縮小しかつ均一化することを特徴とする多
孔体の処理方法1. A gas in which mist droplets of a liquid polymer precursor are mixed is forced to pass through a porous body having continuous pores, and the mist droplets are caused to flow on the wall surface of the continuous pores of the porous body by the feeding pressure of the gas. A method for treating a porous body, which comprises applying the polymer precursor by spreading and then polymerizing the polymer to reduce the diameter of the continuous pores and make the pores uniform.
に連絡する送風手段と、該多孔体の送風手段連絡側に挿
着されているポリマー前駆体の霧化手段とからなること
を特徴とする多孔体の処理装置2. A processing chamber in which a porous body is installed, an air blowing unit that communicates with the processing chamber, and a polymer precursor atomizing unit that is inserted into the air blowing unit connecting side of the porous body. Of porous material
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1170879A JPH0660262B2 (en) | 1989-06-30 | 1989-06-30 | Method for treating porous body and apparatus for treating porous body |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1170879A JPH0660262B2 (en) | 1989-06-30 | 1989-06-30 | Method for treating porous body and apparatus for treating porous body |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0335035A JPH0335035A (en) | 1991-02-15 |
| JPH0660262B2 true JPH0660262B2 (en) | 1994-08-10 |
Family
ID=15913009
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1170879A Expired - Lifetime JPH0660262B2 (en) | 1989-06-30 | 1989-06-30 | Method for treating porous body and apparatus for treating porous body |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0660262B2 (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5644098B2 (en) * | 1973-12-28 | 1981-10-17 | ||
| JPH0316626A (en) * | 1989-06-14 | 1991-01-24 | Asahi Chem Ind Co Ltd | Hydrophilic porous film |
-
1989
- 1989-06-30 JP JP1170879A patent/JPH0660262B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0335035A (en) | 1991-02-15 |
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