JPH02293025A - Membrane module and its production thereof - Google Patents
Membrane module and its production thereofInfo
- Publication number
- JPH02293025A JPH02293025A JP11367789A JP11367789A JPH02293025A JP H02293025 A JPH02293025 A JP H02293025A JP 11367789 A JP11367789 A JP 11367789A JP 11367789 A JP11367789 A JP 11367789A JP H02293025 A JPH02293025 A JP H02293025A
- Authority
- JP
- Japan
- Prior art keywords
- porous membrane
- epoxy resin
- epoxy
- membrane module
- formula
- 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
- 239000012528 membrane Substances 0.000 title claims abstract description 48
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- -1 alicyclic amine Chemical class 0.000 claims abstract description 34
- 239000003822 epoxy resin Substances 0.000 claims abstract description 26
- 229920000647 polyepoxide Polymers 0.000 claims abstract description 26
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 24
- 239000000126 substance Substances 0.000 claims abstract description 18
- 238000004382 potting Methods 0.000 claims abstract description 15
- 125000003700 epoxy group Chemical group 0.000 claims abstract description 9
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims abstract description 6
- 229910052801 chlorine Inorganic materials 0.000 claims abstract description 5
- 239000004698 Polyethylene Substances 0.000 claims description 17
- 229920000573 polyethylene Polymers 0.000 claims description 17
- 229920005989 resin Polymers 0.000 claims description 13
- 239000011347 resin Substances 0.000 claims description 13
- 239000004743 Polypropylene Substances 0.000 claims description 7
- 229920001155 polypropylene Polymers 0.000 claims description 7
- 239000001257 hydrogen Substances 0.000 claims description 4
- 229910052739 hydrogen Inorganic materials 0.000 claims description 4
- 229920002492 poly(sulfone) Polymers 0.000 claims description 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 3
- 125000003277 amino group Chemical group 0.000 claims description 3
- 125000003118 aryl group Chemical group 0.000 claims description 3
- 125000001246 bromo group Chemical group Br* 0.000 claims description 3
- 239000000460 chlorine Substances 0.000 claims description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 2
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 abstract description 2
- 238000002156 mixing Methods 0.000 abstract description 2
- 239000000203 mixture Substances 0.000 abstract description 2
- 125000001424 substituent group Chemical group 0.000 abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 239000004593 Epoxy Substances 0.000 description 7
- 238000001914 filtration Methods 0.000 description 6
- 239000012510 hollow fiber Substances 0.000 description 6
- 238000011282 treatment Methods 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 5
- 238000002844 melting Methods 0.000 description 5
- 230000008018 melting Effects 0.000 description 5
- 150000001412 amines Chemical class 0.000 description 4
- 238000011156 evaluation Methods 0.000 description 3
- 230000020169 heat generation Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000011417 postcuring Methods 0.000 description 3
- 229920002803 thermoplastic polyurethane Polymers 0.000 description 3
- GQWWGRUJOCIUKI-UHFFFAOYSA-N 2-[3-(2-methyl-1-oxopyrrolo[1,2-a]pyrazin-3-yl)propyl]guanidine Chemical compound O=C1N(C)C(CCCN=C(N)N)=CN2C=CC=C21 GQWWGRUJOCIUKI-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000004695 Polyether sulfone Substances 0.000 description 2
- 229920000297 Rayon Polymers 0.000 description 2
- ZBCBWPMODOFKDW-UHFFFAOYSA-N diethanolamine Chemical compound OCCNCCO ZBCBWPMODOFKDW-UHFFFAOYSA-N 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 2
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 2
- 229920006393 polyether sulfone Polymers 0.000 description 2
- 229920002635 polyurethane Polymers 0.000 description 2
- 239000004814 polyurethane Substances 0.000 description 2
- RSJKGSCJYJTIGS-UHFFFAOYSA-N undecane Chemical compound CCCCCCCCCCC RSJKGSCJYJTIGS-UHFFFAOYSA-N 0.000 description 2
- IGSBHTZEJMPDSZ-UHFFFAOYSA-N 4-[(4-amino-3-methylcyclohexyl)methyl]-2-methylcyclohexan-1-amine Chemical compound C1CC(N)C(C)CC1CC1CC(C)C(N)CC1 IGSBHTZEJMPDSZ-UHFFFAOYSA-N 0.000 description 1
- DZIHTWJGPDVSGE-UHFFFAOYSA-N 4-[(4-aminocyclohexyl)methyl]cyclohexan-1-amine Chemical compound C1CC(N)CCC1CC1CCC(N)CC1 DZIHTWJGPDVSGE-UHFFFAOYSA-N 0.000 description 1
- 229930185605 Bisphenol Natural products 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000008065 acid anhydrides Chemical class 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000003851 corona treatment Methods 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 208000028659 discharge Diseases 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- WGYKZJWCGVVSQN-UHFFFAOYSA-N propylamine Chemical group CCCN WGYKZJWCGVVSQN-UHFFFAOYSA-N 0.000 description 1
- 239000002964 rayon Substances 0.000 description 1
- 238000007788 roughening Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/02—Hollow fibre modules
- B01D63/021—Manufacturing thereof
- B01D63/022—Encapsulating hollow fibres
- B01D63/023—Encapsulating materials
Landscapes
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、液体および気体の濾過に用いる膜モジュール
およびその製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a membrane module used for filtration of liquids and gases and a method for manufacturing the same.
(従来の技術〕
近年、流体濾過能力を有する膜モジュールが、医療分野
、液体および気体処理分野などで多く用いられるように
なってきた。最近では、耐熱性、耐薬品性を要求される
分野への使用も拡がりつつある。(Prior Art) In recent years, membrane modules with fluid filtration capabilities have come to be widely used in the medical field, liquid and gas processing fields, etc.Recently, membrane modules with fluid filtration capabilities have been increasingly used in fields that require heat resistance and chemical resistance. The use of is also expanding.
例えば、耐熱性の膜としては、ポリエーテルスルホン、
ボリブロビレンなどを膜素材とするものが挙げられる。For example, heat-resistant membranes include polyether sulfone,
Examples include membrane materials such as boribropylene.
しかしながら、ポリエーテルスルホンを素材とした中空
糸膜は強伸度に劣るため、激しい液流の中では破断する
おそれがある。また、ボリブロビレン中空糸膜は、熱水
を長時間透水すると酸化劣化を起し脆化する。However, hollow fiber membranes made of polyether sulfone have poor strength and elongation, so there is a risk of them breaking in intense liquid flow. Further, when the polypropylene hollow fiber membrane passes through hot water for a long period of time, it undergoes oxidative deterioration and becomes brittle.
一方、ポリエチレンを素材とする多孔質膜は、熱水濾過
性、耐薬品性には優れているが、比較的低融点である。On the other hand, porous membranes made of polyethylene have excellent hot water filtration properties and chemical resistance, but have a relatively low melting point.
したがって、ウレタン樹脂は耐熱性、耐薬品性には劣る
ものの、硬化時の発熱が小さいのでポリエチレン多孔質
膜のボッティング剤として専ら使用されてきた。一方、
エポキシ樹脂は、耐熱性、耐薬品性に優れているものの
、例えば一般的に使用されているビスフェノール型樹脂
の場合には、硬化時の発熱温度がポリエチレンの融点近
傍以上となるためポリエチレン多孔質膜のポッティング
には使用できなかった。従って、ポリエチレン多孔質膜
をボッティングでき、耐熱性、耐薬品性に優れたボッテ
ィング剤の開発が望まれていた。Therefore, although urethane resin has poor heat resistance and chemical resistance, it has been used exclusively as a botting agent for polyethylene porous membranes because it generates little heat during curing. on the other hand,
Epoxy resins have excellent heat resistance and chemical resistance, but in the case of commonly used bisphenol resins, for example, the heat generation temperature during curing is higher than the melting point of polyethylene, so polyethylene porous membranes are It could not be used for potting. Therefore, it has been desired to develop a botting agent that can bott polyethylene porous membranes and has excellent heat resistance and chemical resistance.
本発明の目的は、ポリエチレン多孔質膜のボッティング
に適用できる、耐熱性、耐薬品性、耐衝撃性に優れたボ
ッティング用樹脂を提供することにある。An object of the present invention is to provide a resin for botting that has excellent heat resistance, chemical resistance, and impact resistance and can be applied to botting polyethylene porous membranes.
本発明の他の目的は、耐熱性、耐薬品性、耐衝撃性に優
れたボッティング部を有する膜モジュール、特にポリエ
チレン多孔質膜モジュールを提供することにある。Another object of the present invention is to provide a membrane module, particularly a polyethylene porous membrane module, which has a botting portion with excellent heat resistance, chemical resistance, and impact resistance.
すなわち、本発明は、モジュールケース内に収納された
多孔質膜の端部が、(a)下記一般式(i)Rl
(式中、R1〜R4はそれぞれ独立して水素またはメチ
ル基、Ar’〜Ar’はそれぞれ独立して2個までの塩
素または臭素置換基を有してもよい芳香環、kは0〜5
の整数を示す。)で表わされるエポキシ樹脂A、(b)
下記一般式(ii)
?a
千〇−CH2−CI−)7−0−C112−11;}I
−Cl+■(式中、85〜R8はそれぞれ独立して水素
またはメチル基、^r5〜Ar’はそれぞれ独立して2
個までの塩素、臭素置換基を有してもよい芳香環、mお
よびnは1〜3の整数を示す。)で表わされるエポキシ
樹脂B、および(C)脂環式アミンを含有し、エポキシ
樹脂Aとエポキシ樹脂Bのエポキシ基の数の比が0.2
〜3であるボツテイング剤を硬化させてポッティングさ
れてなる多孔質膜モジュールである。That is, in the present invention, the end portion of the porous membrane housed in the module case is formed by (a) the following general formula (i) Rl (wherein R1 to R4 are each independently hydrogen, a methyl group, Ar'~Ar' is an aromatic ring which may each independently have up to two chlorine or bromine substituents, k is 0 to 5
indicates an integer. ) Epoxy resin A, (b)
General formula (ii) below? a 1000-CH2-CI-)7-0-C112-11;}I
-Cl+■ (In the formula, 85 to R8 are each independently hydrogen or methyl group, ^r5 to Ar' are each independently 2
m and n represent integers from 1 to 3; ), and (C) contains an alicyclic amine, and the ratio of the number of epoxy groups in epoxy resin A and epoxy resin B is 0.2.
This is a porous membrane module made by curing and potting the bottling agent No. 3 to 3.
(作用)
本発明に用いるボッティング剤は、(a)前記一般式(
i)で表わされるエポキシ樹脂A、(b)前記一般式(
11)で表わされるエポキシ樹脂B、および(C)脂.
環式アミンを含有してなる。(Function) The botting agent used in the present invention has (a) the general formula (
i) Epoxy resin A represented by (b) the general formula (
Epoxy resin B represented by 11) and (C) resin.
Contains a cyclic amine.
ボッティング剤として、エポキシ樹脂Aと硬化剤とだけ
からなる組成物を用いると、硬化時の発熱温度が高くな
りすぎ、ボッテイング剤の温度がポリエチレン多孔質膜
の融点近傍以上となるため、ボッティングができない。If a composition consisting only of epoxy resin A and a curing agent is used as a botting agent, the exothermic temperature during curing will be too high, and the temperature of the botting agent will be close to or higher than the melting point of the polyethylene porous membrane, which may cause botting. I can't.
成分(a)として用いられるエポキシ樹脂Aは、前記一
般式(i)において、kがO〜5の整数であることが適
当である。5を超える場合には、粘度が高くなり過ぎる
。In the epoxy resin A used as component (a), in the general formula (i), k is suitably an integer of O to 5. If it exceeds 5, the viscosity becomes too high.
また、成分(b)として用いられるエポキシ樹脂Bは、
前記一般式(ii)において、mおよびnが0〜3の整
数であることが適当である。3を超える場合には、やは
り粘度が高くなり過ぎる。In addition, epoxy resin B used as component (b) is
In the general formula (ii), m and n are suitably integers of 0 to 3. If it exceeds 3, the viscosity will become too high.
エポキシ樹脂Aとエポキシ樹脂Bの混合比は、エポキシ
樹脂Aのエポキシ基数とエポキシ樹脂Bのエポキシ基数
との比が0.2〜3となるように用いるのが好ましく、
0.3〜2がより好ましい。The mixing ratio of epoxy resin A and epoxy resin B is preferably used such that the ratio of the number of epoxy groups in epoxy resin A to the number of epoxy groups in epoxy resin B is 0.2 to 3.
0.3-2 is more preferable.
0.2未満であると耐熱性、耐薬品性が低下し好ましく
ない。3を超えると硬化時の発熱温度が高くなりすぎる
ため適当ではない。If it is less than 0.2, heat resistance and chemical resistance will deteriorate, which is not preferable. If it exceeds 3, the heat generation temperature during curing becomes too high, which is not appropriate.
上記成分(a)と成分(b)とを含有する混合エポキシ
樹脂の硬化剤としては、種々のアミン、アミド、酸無水
物等の使用が考えられるが、これら硬化剤の中で、脂環
式アミンがその硬化挙動(硬化時間、発熱温度等)にお
いて、特にポリエチレン多孔質膜のポッティング剤とし
て使用した場合に最も優れた特性を発揮する。Various amines, amides, acid anhydrides, etc. can be used as curing agents for the mixed epoxy resin containing the above components (a) and (b), but among these curing agents, alicyclic Amines exhibit the most excellent properties in terms of their curing behavior (curing time, exothermic temperature, etc.), especially when used as a potting agent for polyethylene porous membranes.
成分(C)として用いられる脂環式アミンとしては、メ
ンセンジアミン、インホロンジアミン、N一アミノエチ
ルビベラジン、3.9−ビス(3−アミノプロピル)
−2.4,8.10−テトラオキシスビ口(5.5)ウ
ンデカンアダクト、ビス(4−アミノー3−メチルシク
ロヘキシル)メタン、ビス(4一アミノシク口ヘキシル
)メタン、4−アミノー(2,2,6.8−テトラメチ
ル)ピベリジンなどが挙げられ、これらは単独でまたは
混合して用いられる。Alicyclic amines used as component (C) include menzendiamine, inphoronediamine, N-aminoethylbiverazine, and 3.9-bis(3-aminopropyl).
-2.4,8.10-tetraoxysub(5.5) undecane adduct, bis(4-amino-3-methylcyclohexyl)methane, bis(4-aminocyclohexyl)methane, 4-amino(2,2 , 6,8-tetramethyl)piveridine, etc., and these may be used alone or in combination.
脂環式アミン(C)の使用量は、成分(a)および成分
(b)中の合計エポキシ基数と成分(C}中のアなるよ
うに用いるのが好ましく、 0.4〜2.5となるよう
に用いるのかより好ましい。The amount of alicyclic amine (C) used is preferably such that the total number of epoxy groups in component (a) and component (b) is equal to the amount of epoxy groups in component (C}, and is 0.4 to 2.5. It is more preferable to use it as follows.
アミノ基が少ないと常温における硬化時間が長くなり、
アミノ基が多くなりすぎると未反応のアミンが残り、溶
出等の問題がおこる。If there are fewer amino groups, the curing time at room temperature will be longer.
If there are too many amino groups, unreacted amines will remain, causing problems such as elution.
本発明に用いる成分(a)〜(C)を含有するポッティ
ング剤の調製に際しては、これら成分の混合の順序はど
のように行ってもよい。When preparing a potting agent containing components (a) to (C) used in the present invention, these components may be mixed in any order.
本発明に用いる成分(a)〜(C)を含有するボッティ
ング剤は、初期粘度が(25℃)において2000〜2
0000cps、硬化時間が20hr以内で、常温硬化
が可能であり、発熱温度も小さく、低融点のポリエチレ
ン多孔質膜のボッティングにも使用できる。The botting agent containing components (a) to (C) used in the present invention has an initial viscosity of 2000 to 2 at (25°C).
0,000 cps, the curing time is within 20 hours, it can be cured at room temperature, the heat generation temperature is low, and it can also be used for botting polyethylene porous membranes with a low melting point.
また、室温における硬化後、更に後硬化を行うと架橋が
進行し、耐熱性、耐薬品性が向上するので好ましい。多
孔質膜としてポリエチレンを用いる場合、後硬化温度は
ポリエチレンの融点以下で行なう必要がある。Further, it is preferable to further perform post-curing after curing at room temperature because crosslinking progresses and heat resistance and chemical resistance are improved. When polyethylene is used as the porous membrane, the post-curing temperature must be below the melting point of polyethylene.
モジュールケースとしては、各種の樹脂や金属からなる
ものが使用できるが、樹脂の場合には耐熱水性、耐薬品
性の良好なポリブロビレン樹詣やポリスルホン樹脂を用
いることが好ましい。ポリプロピレン樹詣をモジュール
ケースとして用いる場合には、ボッティング剤との接着
性を向上させるためにケースの内表面を表面処理したも
のであることか望ましい。The module case can be made of various resins or metals, but in the case of resin, it is preferable to use polypropylene resin or polysulfone resin, which has good hot water resistance and chemical resistance. When polypropylene wood is used as a module case, it is desirable that the inner surface of the case be surface-treated to improve adhesion to the botting agent.
ポリプロピレン樹脂の表面処理としては、プラズマ放電
処理、コロナ放電処理、火炎処理、紫外線処理、オゾン
処理、クロム混酸処理、n−ヘキサン処理、ブライマー
塗付、表面粗面化等があり、これら処理が単独であるい
は併用して実施される。Surface treatments for polypropylene resin include plasma discharge treatment, corona discharge treatment, flame treatment, ultraviolet treatment, ozone treatment, chromium mixed acid treatment, n-hexane treatment, brusher coating, surface roughening, etc., and these treatments alone It is carried out with or in combination.
本発明に用いる多孔質膜としては、耐熱性、耐薬品性の
点から、ポリオレフィン、ポリスルホン等の膜が好まし
い。多孔質1漠の形態としては、中空糸膜でもよいし平
膜等のシート状膜でもよい。The porous membrane used in the present invention is preferably a membrane made of polyolefin, polysulfone, or the like from the viewpoint of heat resistance and chemical resistance. The form of the porous membrane may be a hollow fiber membrane or a sheet-like membrane such as a flat membrane.
また膜の多孔質化には、従来公知の各種方法によるもの
が使用できる。Furthermore, various conventionally known methods can be used to make the membrane porous.
ボッティング剤を使用して多孔質膜の端部をモジュール
ケース内にボッティングするには、従来公知の各種ボッ
ティング方法が採用できる。Various conventionally known botting methods can be employed to bott the end of the porous membrane into the module case using a botting agent.
以下、実施例により本発明を説明する。 The present invention will be explained below with reference to Examples.
実1例1
エポキシ樹脂Aとしてエビコート 828(油化シエル
エポキシ■製)380重量部、エポキシ樹脂Bとしてエ
ボライト3002(共栄社油脂化学工業■製)315重
量部および脂環式アミンとしてカヤボンド(:−950
(日本化薬■製) 114重量部からなるボッティ
ング剤を用い、ポリエチレン製多孔質膜(EHF410
(; 、商品名、三菱レイヨン■製)を中央部で曲げ、
U字状にし、モジュールケース内に収納し、ボッティン
グ剤を流し込みボッティングした。モジュールケースと
しては、ポリプロピレン製で、そのポッティング部の内
表面を火炎処理したものを使用した。Example 1 380 parts by weight of Ebicoat 828 (manufactured by Yuka Ciel Epoxy ■) as the epoxy resin A, 315 parts by weight of Evolite 3002 (manufactured by Kyoeisha Yushi Kagaku Kogyo ■) as the epoxy resin B, and Kayabond (:-950) as the alicyclic amine.
(manufactured by Nippon Kayaku ■) Using a botting agent consisting of 114 parts by weight, a polyethylene porous membrane (EHF410
(;, product name, made by Mitsubishi Rayon■) is bent at the center,
It was made into a U-shape, housed in a module case, and a botting agent was poured into it for botting. The module case was made of polypropylene, and the inner surface of the potting part was flame treated.
ポッティングは、遠心力作用下で行い、樹脂を室温で2
4時間放置した後、60℃で5時間、更に90℃で5時
間の後硬化を行った。その後、水圧をかけて漏れ検査を
行った。漏れ検査は1 kg/cm2の水圧を3分間か
け、漏れがない場合には水圧をlkg/cIm2きざみ
で上昇させ、各3分間の漏れ検査を水圧5 kg/cが
まで実施した。Potting was carried out under centrifugal force, and the resin was kept at room temperature for 2 hours.
After being left for 4 hours, post-curing was performed at 60°C for 5 hours and then at 90°C for 5 hours. Afterwards, water pressure was applied to check for leaks. A water pressure of 1 kg/cm2 was applied for 3 minutes to check for leaks, and if there was no leakage, the water pressure was increased in steps of 1 kg/cIm2, and leak tests were carried out for each 3 minutes until the water pressure reached 5 kg/c.
接着が不良の場合、モジュールケースとボツティング剤
の接着界面から水の漏れが生じるが、漏れは全く見られ
なかった。If the adhesion is poor, water leaks from the adhesive interface between the module case and the botting agent, but no leakage was observed.
また、ボッティング剤中に固定されたポリエチレン多孔
質膜は溶融しておらず、従来のウレタン樹脂によるポッ
ティングの場合と同様に良好にポッティングされていた
。Further, the polyethylene porous membrane fixed in the potting agent was not melted, and potting was performed well as in the case of conventional potting with urethane resin.
なお、このモジュールで90℃の温水を差圧1kg/c
m2で200時間濾過し、その後モジュールを乾燥させ
、同様の漏れ検査を行ったが水の漏れは全く見られなか
った.。In addition, with this module, 90℃ hot water can be heated at a differential pressure of 1kg/c.
After filtering with m2 for 200 hours, the module was dried and a similar leak test was performed, but no water leaks were found. .
実施例2〜8
第1表に示したエポキシ樹脂A、エポキシ樹脂Bおよび
脂環式アミンからなる各種ポッテイング剤を用い、実施
例1と同様にしてポリエチレン多孔質膜のU字状モジュ
ールを作成した。モジュールケースには、表面処理した
ボリブロビレン樹脂またはポリスルホン樹脂を用いた。Examples 2 to 8 U-shaped modules of polyethylene porous membranes were created in the same manner as in Example 1 using various potting agents consisting of epoxy resin A, epoxy resin B, and alicyclic amine shown in Table 1. . The module case is made of surface-treated polypropylene resin or polysulfone resin.
得られた中空糸膜モジュールの耐熱性の評価を、熱水濾
過またはスチーム滅菌により実施した。また、耐薬品安
定性評価は、酸、アルカリ、エタノールなどの各種薬液
を用いて、実施例1と同様の方法による漏れ検査を実施
することにより行った。中空糸膜モジュールの製造条件
および評価結果を第1表に示した。The heat resistance of the obtained hollow fiber membrane module was evaluated by hot water filtration or steam sterilization. Further, chemical resistance stability evaluation was performed by conducting a leakage test in the same manner as in Example 1 using various chemical solutions such as acid, alkali, and ethanol. Table 1 shows the manufacturing conditions and evaluation results of the hollow fiber membrane module.
比較例1〜5
ボッティング剤としてウレタン樹脂を用いたもの(比較
例1、2)、エポキシ樹脂Aを単独で用いたもの(比較
例3)、エポキシ樹脂Bを単独で用いたもの(比較例4
)、硬化剤として脂肪族アミンを用いたもの(比較例5
)を使用したことを除いては、実施例1と全く同様にし
て中空糸膜モジュールを作成した。膜モジュールの製造
条件および評価結果を第1表に示した。Comparative Examples 1 to 5 Urethane resin was used as a botting agent (Comparative Examples 1 and 2), epoxy resin A was used alone (Comparative Example 3), epoxy resin B was used alone (Comparative Example 4
), using an aliphatic amine as a curing agent (Comparative Example 5)
) A hollow fiber membrane module was produced in exactly the same manner as in Example 1, except that the following was used. The manufacturing conditions and evaluation results of the membrane module are shown in Table 1.
エピコート 828:油化シエルエポキシ■製、エポキ
シ当量190
エピコート834:油化シエルエポキシ■製、エポキシ
当量250
コロネート4403 +日本ポリウレタン■製エポライ
ト3302 :共栄社油脂化学工業■製エポキシ当量3
15
カヤボンドC−950 :日本化薬■製、アミン当量3
8カヤボンドG−900 :日本化薬■製、アミン当1
45ニッポラン4221:日本ポリウレタン■製エピキ
ュアT−1:油化シェルエポキシ■製、アミン当量70
、脂肪族アミン
〔発明の効果〕
以上の説明から明らかなように、本発明によれば、耐熱
性、耐薬品性に優れた多孔質膜モジュール、特にポリエ
チレン製の多孔質膜モジュールが提供され、その意義は
大きい。Epicoat 828: Made by Yuka Ciel Epoxy ■, epoxy equivalent: 190 Epicoat 834: Made from Yuka Ciel Epoxy ■, epoxy equivalent: 250 Coronate 4403 + Epolite 3302, manufactured by Nippon Polyurethane ■: Epoxy equivalent: 3, manufactured by Kyoeisha Yushi Kagaku Kogyo ■
15 Kayabond C-950: Nippon Kayaku ■, amine equivalent 3
8 Kayabond G-900: Manufactured by Nippon Kayaku ■, 1 per amine
45 Nipporan 4221: Made by Nippon Polyurethane ■ Epicure T-1: Made by Yuka Shell Epoxy ■, amine equivalent 70
, aliphatic amine [Effects of the Invention] As is clear from the above description, according to the present invention, a porous membrane module having excellent heat resistance and chemical resistance, particularly a porous membrane module made of polyethylene, is provided. Its significance is great.
特許出願人 三菱レイヨン株式会社Patent applicant: Mitsubishi Rayon Co., Ltd.
Claims (4)
が、(a)下記一般式(i) ▲数式、化学式、表等があります▼(i) (式中、R^1〜R^4はそれぞれ独立して水素または
メチル基、Ar^1〜Ar^4はそれぞれ独立して2個
までの塩素または臭素置換基を有してもよい芳香環、k
は0〜5の整数を示す。)で表わされるエポキシ樹脂A
、(b)下記一般式(ii) ▲数式、化学式、表等があります▼(ii) (式中、R^5〜R^8はそれぞれ独立して水素または
メチル基、Ar^5〜Ar^6はそれぞれ独立して2個
までの塩素または臭素置換基を有してもよい芳香環、m
およびnは1〜3の整数を示す。)で表わされるエポキ
シ樹脂B、および(c)脂環式アミンを含有し、エポキ
シ樹脂Aとエポキシ樹脂Bのエポキシ基の数の比が0.
2〜3であるポッティング剤を硬化させてポッティング
されてなる多孔質膜モジュール。(1) The end of the porous membrane stored in the module case is (a) The following general formula (i) ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ (i) (In the formula, R^1 ~ R^ 4 is each independently a hydrogen or methyl group, Ar^1 to Ar^4 are each independently an aromatic ring which may have up to two chlorine or bromine substituents, k
represents an integer from 0 to 5. ) Epoxy resin A represented by
, (b) General formula (ii) below ▲ Numerical formulas, chemical formulas, tables, etc. ▼ (ii) (In the formula, R^5 to R^8 are each independently hydrogen or a methyl group, Ar^5 to Ar^ 6 is an aromatic ring which may each independently have up to two chlorine or bromine substituents, m
and n represents an integer of 1 to 3. ) and (c) an alicyclic amine, and the ratio of the number of epoxy groups in the epoxy resin A and the epoxy resin B is 0.
A porous membrane module potted by curing the potting agent according to No. 2 or 3.
面処理されたポリプロピレン樹脂である請求項1記載の
多孔質膜モジュール。(2) The porous membrane module according to claim 1, wherein the module case is made of polysulfone resin or surface-treated polypropylene resin.
記載の多孔質膜モジュール(3) Claim 1, wherein the porous membrane is a polyethylene porous membrane.
Porous membrane module described
と成分(c)のアミノ基数の比(▲数式、化学式、表等
があります▼/−NH_2)が0.25〜4である請求
項1記載のポッティング剤を用いて、多孔質膜の端部を
モジュールケース内にポッティングすることを特徴とす
る多孔質膜モジュールの製造方法。(4) Claim that the ratio of the total number of epoxy groups in component (a) and component (b) to the number of amino groups in component (c) (▲There are mathematical formulas, chemical formulas, tables, etc.▼/-NH_2) is 0.25 to 4. Item 2. A method for producing a porous membrane module, comprising potting an end of the porous membrane in a module case using the potting agent according to item 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11367789A JPH02293025A (en) | 1989-05-08 | 1989-05-08 | Membrane module and its production thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11367789A JPH02293025A (en) | 1989-05-08 | 1989-05-08 | Membrane module and its production thereof |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02293025A true JPH02293025A (en) | 1990-12-04 |
Family
ID=14618369
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11367789A Pending JPH02293025A (en) | 1989-05-08 | 1989-05-08 | Membrane module and its production thereof |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02293025A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1174175A4 (en) * | 1999-04-02 | 2002-11-06 | Mitsubishi Rayon Co | Hollow yarn membrane module, potting agent therefor and method for deaeration of liquid chemicals |
EP1837365A1 (en) * | 2005-01-07 | 2007-09-26 | Asahi Kasei Kabushiki Kaisha | Porous cured epoxy resin |
EP3479890A4 (en) * | 2016-06-29 | 2020-02-26 | DIC Corporation | Hollow fiber membrane module and production method therefor, and epoxy resin used in hollow fiber membrane and production method |
-
1989
- 1989-05-08 JP JP11367789A patent/JPH02293025A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1174175A4 (en) * | 1999-04-02 | 2002-11-06 | Mitsubishi Rayon Co | Hollow yarn membrane module, potting agent therefor and method for deaeration of liquid chemicals |
US6648945B1 (en) | 1999-04-02 | 2003-11-18 | Mitsubishi Rayon Co., Ltd. | Hollow yarn membrane module, potting agent therefor and method for deaeration of liquid chemicals |
EP1837365A1 (en) * | 2005-01-07 | 2007-09-26 | Asahi Kasei Kabushiki Kaisha | Porous cured epoxy resin |
EP1837365A4 (en) * | 2005-01-07 | 2011-04-20 | Emaus Kyoto Inc | Porous cured epoxy resin |
US8186519B2 (en) | 2005-01-07 | 2012-05-29 | Emaus Kyoto, Inc. | Porous cured epoxy resin |
EP3479890A4 (en) * | 2016-06-29 | 2020-02-26 | DIC Corporation | Hollow fiber membrane module and production method therefor, and epoxy resin used in hollow fiber membrane and production method |
US11478753B2 (en) | 2016-06-29 | 2022-10-25 | Dic Corporation | Hollow fiber membrane module and production method therefor, and epoxy resin used in hollow fiber membrane and production method |
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