JPH04326929A - Separation membrane - Google Patents

Separation membrane

Info

Publication number
JPH04326929A
JPH04326929A JP12471891A JP12471891A JPH04326929A JP H04326929 A JPH04326929 A JP H04326929A JP 12471891 A JP12471891 A JP 12471891A JP 12471891 A JP12471891 A JP 12471891A JP H04326929 A JPH04326929 A JP H04326929A
Authority
JP
Japan
Prior art keywords
membrane
fabric body
woven fabric
semipermeable membranes
semipermeable
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
Application number
JP12471891A
Other languages
Japanese (ja)
Inventor
Katsumori Nagura
克守 名倉
Kenichi Ikeda
健一 池田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nitto Denko Corp
Original Assignee
Nitto Denko Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nitto Denko Corp filed Critical Nitto Denko Corp
Priority to JP12471891A priority Critical patent/JPH04326929A/en
Publication of JPH04326929A publication Critical patent/JPH04326929A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To prevent the expansion of a semipermeable membrane due to negative pressure action by embedding the thick parts on both sides of a fabric body excepting the intermediate part thereof in the sponge like layer parts of respective semipermeable membranes and leaving the gap for a transmitted fluid path to the intermediate part of the fabric body. CONSTITUTION:Semipermeable membranes 2,2 are provided to both surfaces of a fabric body 1 having a three-dimensional structure and have skin layers on the surfaces thereof and the respective thick parts 11, 11 on both sides of the fabric body 1 excepting the intermediate part 10 thereof are embedded in the sponge like layer parts of the semipermeable membranes 2,2. Therefore, a gap for a transmitted fluid flow path is left to the intermediate part 10 of the fabric body 1. In this separation membrane, the outsides of the semipermeable membranes 2,2 are used as raw liquid sides and the solvent in a raw liquid is transmitted through the skin layers of the semipermeable membranes 2,2 and this transmitted liquid flows to the gap for the transmitted fluid flow path of the intermediate part 10 of the fabric body 10. In this case, even when the pressure of the gap for the transmitted fluid flow path of the intermediate part of the fabric body becomes higher than the outside pressure of the semipermeable membranes, since the semipermeable membranes are strongly embedded in and bonded to the fabric body, the outward expansion of the semipermeable membranes can be prevented.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は溶液から特定の液体の分
離、混合気体からの特定の気体の分離、液体又は気体か
らの固形分の分離、気体含有液体からの気体の分離等に
使用する分離膜に関するものである。
[Industrial Application Field] The present invention is used for the separation of a specific liquid from a solution, the separation of a specific gas from a mixed gas, the separation of solids from a liquid or gas, the separation of a gas from a gas-containing liquid, etc. It relates to separation membranes.

【0002】0002

【従来の技術】特定の液体の分離、混合気体からの特定
の気体の分離、液体又は気体からの固形分の分離、気体
含有液体からの気体の分離等に使用する半透膜において
は、膜自体の機械的強度が小さいので、通常、不織布等
の支持体上に膜を形成したもの(不織布上に製膜溶液を
塗布して膜を形成したもの)が使用されている。
[Prior Art] Semipermeable membranes used for separating specific liquids, separating specific gases from mixed gases, separating solids from liquids or gases, separating gases from gas-containing liquids, etc. Since its mechanical strength is low, a membrane formed on a support such as a non-woven fabric (a membrane formed by coating a membrane-forming solution on a non-woven fabric) is usually used.

【0003】この分離膜を使用した膜モジュ−ルによっ
て原液を処理するには、半透膜の表面側、即ちスキン層
側を原液側とし、半透膜の裏面側、即ち支持体側を透過
液側とし、原液側を高圧側にして膜間差圧を加えること
が必要である。この場合、半透膜の裏面側においては、
透過液通路部材の溝縁端又は穴縁端等に緊圧されるが、
支持体層の存在のために半透膜の損傷を防止できる。
In order to process a stock solution using a membrane module using this separation membrane, the surface side of the semipermeable membrane, ie, the skin layer side, is used as the stock solution side, and the back side of the semipermeable membrane, ie, the support side, is used as the permeate liquid side. It is necessary to apply transmembrane pressure with the stock solution side as the high pressure side. In this case, on the back side of the semipermeable membrane,
Although pressure is applied to the groove edge or hole edge of the permeate passage member,
Damage to the semipermeable membrane can be prevented due to the presence of the support layer.

【0004】0004

【発明が解決しようとする課題】しかしながら、膜モジ
ュ−ルを逆洗する場合においては、半透膜にその逆洗液
が逆方向圧力(負圧)として作用し、また、透過液室側
に透過液が溜っている状態で原液室から原液を排出する
ときは、その透過液の高低差圧力が負圧として作用し(
特に透過液タンクが高所に設置されていると、その負圧
が著しく大となる)、更にまた、原液を急峻に抜くと原
液室での空間の発生に膜を経ての透過液側からの給気が
追従せずに減圧空間が形成されて負圧が作用することが
あり、かかる負圧作用下では、半透膜のスキン層側が原
液通路用部材の溝縁端等に緊圧されてスキン層が損傷を
受ける畏れがある。
[Problems to be Solved by the Invention] However, when backwashing a membrane module, the backwash liquid acts on the semipermeable membrane as reverse pressure (negative pressure), and the permeate chamber side When discharging the stock solution from the stock solution chamber while the permeate has accumulated, the pressure difference between the heights of the permeate acts as negative pressure (
In particular, if the permeate tank is installed at a high place, the negative pressure will be extremely large).Furthermore, if the stock solution is withdrawn abruptly, a space will be created in the stock solution chamber and the permeate will pass through the membrane from the permeate side. A reduced pressure space may be formed without the supply air following, and negative pressure may act, and under such negative pressure, the skin layer side of the semipermeable membrane is compressed by the groove edge of the concentrate passage member, etc. There is a risk that the skin layer may be damaged.

【0005】本発明の目的は負圧が作用しても、半透膜
の損傷をよく防止できる分離膜を提供することにある。
An object of the present invention is to provide a separation membrane that can effectively prevent damage to the semipermeable membrane even when negative pressure is applied.

【0006】[0006]

【課題を解決するための手段】本発明の分離膜は表面に
スキン層を有する半透膜が織布体の両面に設けられ、各
半透膜のスポンジ状層部分に織布体中間部分を除く両側
の各厚み部分が埋設され、前記織布体中間部分に透過流
体流路用間隙が残存されていることを特徴とする構成で
ある。
[Means for Solving the Problems] In the separation membrane of the present invention, semipermeable membranes having skin layers on the surface are provided on both sides of a woven fabric body, and an intermediate portion of the woven fabric body is provided on the sponge-like layer portion of each semipermeable membrane. This structure is characterized in that each of the thickness portions on both sides except for the woven fabric body is buried, and a gap for a permeate fluid flow path remains in the intermediate portion of the woven fabric body.

【0007】[0007]

【作用】負圧が作用しても、即ち、織布体中間部分の透
過流体流路用間隙の圧力が半透膜外部の圧力よりも高圧
になっても、両半透膜のスポンジ層部分が織布体に埋着
結合されており、この結合強度が織布の繊維間隙へのス
ポンジ層の食い込みのために強力であって、各半透膜の
外側に向かう膨出が防止されるから、半透膜表面のスポ
ンジ層が原液通路用部材の溝縁端などと接触していても
、その接触箇所での緊圧をよく軽減でき、半透膜の損傷
を回避できる。
[Operation] Even if negative pressure is applied, that is, even if the pressure in the gap for the permeate fluid flow path in the middle part of the woven fabric becomes higher than the pressure outside the semipermeable membrane, the sponge layer of both semipermeable membranes is embedded and bonded to the woven fabric body, and this bonding strength is strong because the sponge layer bites into the fiber gaps of the woven fabric, preventing each semipermeable membrane from bulging outward. Even if the sponge layer on the surface of the semipermeable membrane contacts the edge of the groove of the liquid passage member, the pressure at the contact point can be effectively reduced, and damage to the semipermeable membrane can be avoided.

【0008】[0008]

【実施例】図1は本発明の実施例を示す説明図である。 図1において、1は織布体であり、三次元構造を有して
いる。2,2は織布体1の両面に設けた半透膜であり、
表面にスキン層を有し、織布体1の中間部分10を除く
両側の各厚み部分11,11が各半透膜2,2のスポン
ジ状層部分に埋設されている。従って、織布体中間部分
10には透過流体流路用間隙が残存されている。
Embodiment FIG. 1 is an explanatory diagram showing an embodiment of the present invention. In FIG. 1, numeral 1 is a woven fabric body having a three-dimensional structure. 2, 2 are semipermeable membranes provided on both sides of the woven fabric body 1;
It has a skin layer on its surface, and each thick portion 11, 11 on both sides of the woven fabric body 1 except for the middle portion 10 is embedded in the sponge-like layer portion of each semipermeable membrane 2, 2. Therefore, a gap for the permeate fluid flow path remains in the intermediate portion 10 of the woven fabric body.

【0009】この分離膜においては、各半透膜の外側が
原液側として使用され、各半透膜のスキン層を原液中の
溶媒が透過し、該透過液が織布体中間部分には透過流体
流路用間隙を流れていく。この場合、負圧が作用しても
、即ち、織布体中間部分の透過流体流路用間隙の圧力が
半透膜の外側の圧力よりも高くなっても、各半透膜が織
布体に強固に埋着結合されているから、半透膜の外方向
膨出が阻止され、半透膜表面が原液通路用部材の溝縁端
等のエッジに接触していても、その接触圧を充分に低く
保持できるから、半透膜表面の損傷をよく防止できる。
In this separation membrane, the outside of each semipermeable membrane is used as the stock solution side, and the solvent in the stock solution permeates through the skin layer of each semipermeable membrane, and the permeate passes through the middle part of the woven fabric. It flows through the gap for the fluid flow path. In this case, even if a negative pressure acts, that is, even if the pressure in the gap for the permeate fluid flow path in the middle part of the woven fabric becomes higher than the pressure on the outside of the semipermeable membrane, each semipermeable membrane remains in the woven fabric. Since the semipermeable membrane is firmly embedded and bonded to the membrane, outward expansion of the semipermeable membrane is prevented, and even if the semipermeable membrane surface contacts an edge such as a groove edge of the concentrate passage member, the contact pressure is suppressed. Since the temperature can be kept sufficiently low, damage to the surface of the semipermeable membrane can be well prevented.

【0010】本発明の分離膜においては、使用する高分
子材料に応じ、逆浸透膜、限外濾過膜、精密濾過膜とし
て使用でき、更に、本発明の分離膜を支持膜として用い
ることにより機械的強度の優れた逆浸透複合膜、ガス分
離膜、パ−ベ−パレイション膜を製作することも可能で
ある。
The separation membrane of the present invention can be used as a reverse osmosis membrane, an ultrafiltration membrane, or a precision filtration membrane depending on the polymer material used.Furthermore, by using the separation membrane of the present invention as a support membrane, mechanical It is also possible to produce reverse osmosis composite membranes, gas separation membranes, and pervaporation membranes with excellent mechanical strength.

【0011】本発明において使用する膜素材は、製膜性
のある高分子ポリマーであれば、特に限定されないが、
例えば、ポリスルホン系ポリマー,親水性ポリオレフィ
ン系ポリマー,ポリフッ化ビニリデン、ポリアクリロニ
トリル系ポリマー,酢酸セルロース,ポリイミド,ポリ
アミド酸等、これらの混合物,或いは、これらにスルホ
ン酸基,カルボキシル基,アミノ基等の荷電基を導入し
たものを使用できる。
[0011] The membrane material used in the present invention is not particularly limited as long as it is a polymer with film-forming properties;
For example, polysulfone-based polymers, hydrophilic polyolefin-based polymers, polyvinylidene fluoride, polyacrylonitrile-based polymers, cellulose acetate, polyimide, polyamic acid, etc., mixtures thereof, or charged sulfonic acid groups, carboxyl groups, amino groups, etc. Those into which groups have been introduced can be used.

【0012】製膜液には、素材としての高分子ポリマー
を溶剤で溶解したものを用い、そのポリマー濃度は、ポ
リマーの分子量や種類によって異なるが、通常、5〜4
0%、好ましくは10〜30%である。
[0012] The film-forming solution uses a material in which a high molecular weight polymer is dissolved in a solvent, and the polymer concentration varies depending on the molecular weight and type of the polymer, but is usually 5 to 4.
0%, preferably 10-30%.

【0013】製膜溶液として用いる溶剤には、高分子ポ
リマーを溶解し、且つ水と混合し得るものを使用する必
要があり、N,N−ジメチルアセトアミド,N,N−ジ
メチルホルムアミド、N−メチル−2−ピロリドン、ジ
メチルスルホキシド、アセトン、IPA、THF、ジオ
キシサン等の極性溶剤を使用できる。
[0013] The solvent used as the membrane forming solution must be one that can dissolve the high molecular weight polymer and be miscible with water, such as N,N-dimethylacetamide, N,N-dimethylformamide, N-methyl Polar solvents such as -2-pyrrolidone, dimethyl sulfoxide, acetone, IPA, THF, dioxane, etc. can be used.

【0014】製膜溶液中に加える添加剤としては、例え
ば、塩化リチウム,過塩素酸マグネシウム等の無機塩や
エチレングリコール,ポリエチレングリコール,ポリビ
ニルピロリドン,アセトン、ホルムアミドのような有機
物を使用できる。この添加剤の濃度は、ポリマーの種類
や添加剤の種類によって異なるが、通常、ポリマ−10
0重量部に対して1〜200重量部、好ましくは5〜1
50重量部である。
As additives to be added to the membrane forming solution, for example, inorganic salts such as lithium chloride and magnesium perchlorate, and organic substances such as ethylene glycol, polyethylene glycol, polyvinylpyrrolidone, acetone, and formamide can be used. The concentration of this additive varies depending on the type of polymer and the type of additive, but it is usually
1 to 200 parts by weight, preferably 5 to 1 parts by weight
It is 50 parts by weight.

【0015】本発明において用いる織布体としては、製
膜溶液の含浸が可能なものであること、適当な厚みを有
し厚み中間部に透過液通路となり得る間隙があること、
原液の加圧下において透過液通路用間隙を保持し得る耐
圧潰強度を有すること、含浸した製膜溶液が凝固液中で
凝固する際の膜の収縮下でも透過液通路用間隙を保持し
得ること等の要件を充足するものが使用される。
The woven fabric used in the present invention must be capable of being impregnated with a membrane-forming solution, have an appropriate thickness, and have a gap in the middle of the thickness that can serve as a permeate passage.
It must have a crushing strength that can maintain the gap for the permeate passage under the pressure of the raw solution, and it must be able to maintain the gap for the permeate passage even when the membrane shrinks when the impregnated membrane-forming solution coagulates in the coagulation liquid. Those that satisfy the following requirements are used.

【0016】織布体の構造としては、全体が3次元的に
均一に織られた織布、表面が密に織られ中間が粗に織ら
れた織布、芯材となる基布の表面に繊維を織り込んだ織
布などを使用できる。織布の厚みを余り薄くすると織布
の表面のみに製膜溶液を含浸させて透過液通路用間隙を
確保することが困難になり、他方、織布の厚みを余り厚
くすると、膜モジュ−ル単位体積あたりの膜面積が小と
なり、また、透過液通路用の非含浸部分が必要以上に厚
くなって加圧時の耐圧強度を保証し難くなるので、織布
の厚みは、通常、0.1mm〜10mm、好ましくは、
0.3mm〜5mmとすることが望ましい。
The structure of the woven fabric includes a woven fabric whose entire surface is woven three-dimensionally uniformly, a woven fabric whose surface is densely woven and a coarsely woven fabric in the middle, and a woven fabric whose surface is woven uniformly in three dimensions; Woven fabrics with fibers woven into them can be used. If the thickness of the woven fabric is too thin, it will be difficult to impregnate only the surface of the woven fabric with the membrane-forming solution and ensure a gap for the permeate passage.On the other hand, if the woven fabric is too thick, the membrane module The membrane area per unit volume is small, and the non-impregnated part for the permeate passage becomes thicker than necessary, making it difficult to guarantee pressure resistance when pressurized, so the thickness of the woven fabric is usually 0. 1 mm to 10 mm, preferably
It is desirable to set it as 0.3 mm - 5 mm.

【0017】繊維の材質は、機械的強度と製膜溶液の溶
剤に対する耐性を備えていれば、特に限定されないが、
例えば、ポリエステル、ポリプロピレン、ポリエチレン
、ポリアミド、ガラス繊維等を使用できる。
The material of the fiber is not particularly limited as long as it has mechanical strength and resistance to the solvent of the film forming solution.
For example, polyester, polypropylene, polyethylene, polyamide, glass fiber, etc. can be used.

【0018】本発明の分離膜の製造には、製膜溶液を織
布体の両表面のみに含浸させ、この織布体をギャップを
調整した2本のロ−ルの間に垂直に通して織布両表面の
製膜溶液層の厚みをほぼ等厚に調整し、製膜溶液層表面
からの溶剤蒸発によりスキン層を形成し、次いで、凝固
液に浸漬し膜内部の溶剤を含んだ溶液状態の部分を凝固
させてスポンジ層に相転移させる方法を使用できる。ま
た、溶剤を蒸発させずに、凝固液中でスキン層とスポン
ジ層とを形成する方法を使用することもでる。
To produce the separation membrane of the present invention, only both surfaces of a woven fabric are impregnated with a membrane-forming solution, and the woven fabric is passed perpendicularly between two rolls with an adjusted gap. The thickness of the film-forming solution layer on both surfaces of the woven fabric is adjusted to be approximately equal, and a skin layer is formed by evaporation of the solvent from the surface of the film-forming solution layer.Then, it is immersed in a coagulation solution to remove the solvent-containing solution inside the film. A method can be used in which a portion of the state is solidified and undergoes a phase transition into a sponge layer. It is also possible to use a method of forming a skin layer and a sponge layer in a coagulating solution without evaporating the solvent.

【0019】本発明の分離膜は、スパイラル型膜モジュ
−ル、プレ−ト&フレ−ム型膜モジュ−ルの膜として使
用される。プレ−ト&フレ−ム型膜モジュ−ルや回転円
盤型モジュ−ルのように、膜支持板を使用しているもの
に対しては、織布体に、織布の多間隙性を充分に保持で
きる程度に樹脂等(樹脂等には透過液への溶出のないも
のが使用される)で固め強度を高めたものを使用すれば
、膜支持板を省略できる。
The separation membrane of the present invention is used as a membrane for a spiral type membrane module or a plate and frame type membrane module. For those that use a membrane support plate, such as plate & frame type membrane modules and rotating disk type modules, the woven fabric should have sufficient porous properties. If a membrane support plate is used, the membrane support plate can be omitted by using a material hardened with resin or the like (resin or the like is used that does not elute into the permeate) to the extent that the membrane can be maintained.

【0020】本発明の分離膜においては、両面の半透膜
が織布体に結着されており、これら半透膜間の圧力が半
透膜外の圧力より高くなっても半透膜の膨出を防止でき
る。この場合、次ぎの実施例からも明らかなように、織
布体と半透膜との結着強度が著しく大であることが、極
めて重要な役割を果たしている。
In the separation membrane of the present invention, the semipermeable membranes on both sides are bonded to the woven fabric body, and even if the pressure between these semipermeable membranes becomes higher than the pressure outside the semipermeable membrane, the semipermeable membranes Can prevent bulges. In this case, as is clear from the following examples, it plays an extremely important role that the bonding strength between the woven fabric body and the semipermeable membrane is extremely high.

【0021】実施例ポリスルホン18重量%をN−メチ
ル−2−ピロリドンに溶解し製膜溶液として調整した。 この製膜溶液を、厚み中央部に透過水流路となる間隙を
有し、両表面が密に織られた厚さ2.5mmの織布の表
面にのみ含浸させ、この織布をギャップを有する2本の
ロ−ル間に通し、これを水に浸漬して両面に半透膜を形
成した。この膜は限外濾過膜としての性能を呈し、ポリ
エチレングリコ−ル20,000の阻止率は62%であ
った。
Example 18% by weight of polysulfone was dissolved in N-methyl-2-pyrrolidone to prepare a film forming solution. This membrane-forming solution is impregnated only on the surface of a 2.5 mm thick woven fabric with a gap in the center of the thickness that serves as a permeate flow path, and both surfaces are densely woven. It was passed between two rolls and immersed in water to form semipermeable membranes on both sides. This membrane exhibited performance as an ultrafiltration membrane, with a rejection rate of polyethylene glycol 20,000 of 62%.

【0022】また、不織布上に同一の製膜液を塗布し、
水に浸漬して得た分離膜の透過液側からの加圧で不織布
と半透膜間とが剥離した圧力の2倍の圧力を実施例品の
透過水流路に加えたが、なんら異常は観られなかった。
[0022] Also, the same film forming solution was applied on the nonwoven fabric,
A pressure twice as high as the pressure at which the nonwoven fabric and the semipermeable membrane were separated by applying pressure from the permeate side of the separation membrane obtained by immersing it in water was applied to the permeate flow path of the example product, but no abnormality was observed. I couldn't watch it.

【0023】[0023]

【発明の効果】本発明の分離膜は上述した通りの構成で
あり、織布体の両面に半透膜が埋着され、織布体の中間
に透過液通路用間隙が確保されているから、負圧が作用
しても、半透膜の膨出を防止でき、半透膜と原液通路部
材の溝縁端エッヂとの負圧下での緊圧をよく回避でき、
半透膜の損傷を防止できる。
[Effects of the Invention] The separation membrane of the present invention has the structure as described above, and semipermeable membranes are embedded on both sides of the woven fabric body, and a gap for the permeate passage is secured in the middle of the woven fabric body. Even if negative pressure is applied, the semipermeable membrane can be prevented from swelling, and the tension between the semipermeable membrane and the groove edge of the stock solution passage member can be well avoided under negative pressure.
Damage to the semipermeable membrane can be prevented.

【図面の簡単な説明】[Brief explanation of drawings]

【図1】本発明の実施例を示す説明図である。FIG. 1 is an explanatory diagram showing an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1      織布体 10    織布体の厚中間部分 2      半透膜 1 Woven fabric 10   Thickness middle part of woven fabric body 2 Semi-permeable membrane

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】表面にスキン層を有する半透膜が織布体の
両面に設けられ、各半透膜のスポンジ状層部分に織布体
中間部分を除く両側の各厚み部分が埋設され、前記織布
体中間部分に透過流体流路用間隙が残存されていること
を特徴とする分離膜。
Claim 1: A semipermeable membrane having a skin layer on the surface is provided on both sides of a woven fabric body, and each thickness portion on both sides of the woven fabric body except for an intermediate portion is embedded in a sponge-like layer portion of each semipermeable membrane, A separation membrane characterized in that a gap for a permeate fluid flow path remains in the intermediate portion of the woven fabric body.
JP12471891A 1991-04-25 1991-04-25 Separation membrane Pending JPH04326929A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12471891A JPH04326929A (en) 1991-04-25 1991-04-25 Separation membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12471891A JPH04326929A (en) 1991-04-25 1991-04-25 Separation membrane

Publications (1)

Publication Number Publication Date
JPH04326929A true JPH04326929A (en) 1992-11-16

Family

ID=14892388

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12471891A Pending JPH04326929A (en) 1991-04-25 1991-04-25 Separation membrane

Country Status (1)

Country Link
JP (1) JPH04326929A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005032699A1 (en) 2003-09-19 2005-04-14 Poromedia Gmbh Filter medium
WO2014115687A1 (en) * 2013-01-25 2014-07-31 住友ベークライト株式会社 Pervaporation membrane and method for concentrating phenol

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005032699A1 (en) 2003-09-19 2005-04-14 Poromedia Gmbh Filter medium
US8393477B2 (en) 2003-09-19 2013-03-12 X-Flow B.V. Filter medium
WO2014115687A1 (en) * 2013-01-25 2014-07-31 住友ベークライト株式会社 Pervaporation membrane and method for concentrating phenol

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