JP2007111674A - Spiral separation membrane element - Google Patents

Spiral separation membrane element Download PDF

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JP2007111674A
JP2007111674A JP2005308347A JP2005308347A JP2007111674A JP 2007111674 A JP2007111674 A JP 2007111674A JP 2005308347 A JP2005308347 A JP 2005308347A JP 2005308347 A JP2005308347 A JP 2005308347A JP 2007111674 A JP2007111674 A JP 2007111674A
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separation membrane
water collecting
collecting pipe
membrane element
spiral
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Masashi Beppu
雅志 別府
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Nitto Denko Corp
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Nitto Denko Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a spiral separation membrane element in which the pressure loss to be caused when permeated water flows in a water collection pipe can be decreased without changing the outside and inside diameters of the water collection pipe. <P>SOLUTION: The spiral separation membrane element is formed by spirally winding a separation membrane 1, a supply-side flow passage material 2 and a permeated water-side flow passage material 3 around the perforated water collection pipe 5 in a laminated state. A plurality of grooves 5a each extending along the axial direction of the water collection pipe 5 are arranged on the inner peripheral surface of the water collection pipe 5. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、液体中に存在している成分を分離するスパイラル型分離膜エレメントに関し、詳しくは集水管内の透過水流れの際の圧力損失を小さくするために、集水管の内周面に溝を有するスパイラル型分離膜エレメントに関する。   The present invention relates to a spiral type separation membrane element that separates components present in a liquid, and more particularly, to reduce a pressure loss during permeate flow in a water collection pipe, a groove is formed on the inner peripheral surface of the water collection pipe. The present invention relates to a spiral separation membrane element.

従来のスパイラル型分離膜エレメントの構造としては、分離膜、供給側流路材及び透過水側流路材の積層体の単数または複数が、有孔の中空状集水管の周りに巻きつけられたものが知られている(例えば、特許文献1参照)。通常、複数本のエレメントが、圧力容器であるベッセル内に装填して使用される。   As a structure of a conventional spiral separation membrane element, one or a plurality of laminates of a separation membrane, a supply-side channel material, and a permeate-side channel material are wound around a perforated hollow water collecting pipe. Those are known (for example, see Patent Document 1). Usually, a plurality of elements are used by being loaded into a vessel which is a pressure vessel.

この膜エレメントでは、原液が一端面より供給され、供給側流路材に沿って流動しながら分離膜で濾過され、他端面より濃縮液が取り出される。分離膜で濾過された透過液は透過側流路材に沿って流動して、集水管の孔から流入し、集水管内を流動する。このように集水管中には透過水が流れるために、圧力損失(流動抵抗)が発生する。この圧力損失は運転中のエネルギーロスであるために少ないほうがよい。   In this membrane element, the stock solution is supplied from one end surface, filtered through the separation membrane while flowing along the supply-side channel material, and the concentrated solution is taken out from the other end surface. The permeate filtered through the separation membrane flows along the permeate-side channel material, flows in from the holes of the water collection pipe, and flows in the water collection pipe. Thus, since permeate flows through the water collection pipe, pressure loss (flow resistance) occurs. Since this pressure loss is an energy loss during operation, it is better to reduce the pressure loss.

集水管の圧力損失を少なくする方法として、集水管の内径を大きくする手段が考えられる。しかし、スパイラル型分離膜エレメントの外径は決まっているので、集水管内径を大きくするとエレメントに使用される分離膜の膜面積が小さくなり、エレメントの透過性能が低下するという問題がある。そのために、集水管径を大きくする対策には制限がある。   As a method for reducing the pressure loss of the water collecting pipe, a means for increasing the inner diameter of the water collecting pipe can be considered. However, since the outer diameter of the spiral separation membrane element is determined, there is a problem that when the inner diameter of the water collecting pipe is increased, the membrane area of the separation membrane used for the element is reduced and the permeation performance of the element is lowered. For this reason, there are limitations on measures to increase the diameter of the water collection pipe.

また、集水管の管の厚みを小さくして内径だけを大きくする方法も考えられるが、集水管の強度の低下や、集水管を連結するジョイント等の径を変える必要が生じるなどの問題があるため、好ましい方法とは言えない。   In addition, a method of reducing the thickness of the water collecting pipe and increasing only the inner diameter is conceivable, but there are problems such as a decrease in strength of the water collecting pipe and a need to change the diameter of a joint or the like connecting the water collecting pipe. Therefore, it is not a preferable method.

特開平10−137558号公報JP 10-137558 A

そこで、本発明の目的は、集水管の外径および内径を変えることなしに、集水管内の透過水流れによる圧力損失を低減できるスパイラル型分離膜エレメントを提供することにある。   Therefore, an object of the present invention is to provide a spiral separation membrane element that can reduce pressure loss due to the permeate flow in the water collection pipe without changing the outer diameter and inner diameter of the water collection pipe.

本発明者らは、上記目的を達成すべく、集水管の圧力損失について鋭意研究したところ、集水管の内周面に軸方向に沿って延びる複数の溝を設けることによって、透過水流れによる圧力損失を低減できることを見出し、本発明を完成するに至った。   In order to achieve the above-mentioned object, the present inventors diligently studied the pressure loss of the water collecting pipe, and by providing a plurality of grooves extending along the axial direction on the inner peripheral surface of the water collecting pipe, The present inventors have found that loss can be reduced and have completed the present invention.

即ち、本発明のスパイラル型分離膜エレメントは、分離膜、供給側流路材及び透過水側流路材が積層状態で有孔の集水管の周囲にスパイラル状に巻回されたスパイラル型分離膜エレメントにおいて、前記集水管の内周面には、集水管の軸方向に沿って延びる複数の溝を有することを特徴とする。   That is, the spiral separation membrane element of the present invention includes a spiral separation membrane in which a separation membrane, a supply-side flow path material, and a permeate-side flow path material are spirally wound around a perforated water collecting pipe. In the element, the inner peripheral surface of the water collecting pipe has a plurality of grooves extending along the axial direction of the water collecting pipe.

本発明によると、集水管の内周面に溝を設けるだけであるため、集水管の外径および内径が変わらないので、分離膜の膜面積が小さくならず、集水管の強度の低下などの問題も生じない。また、集水管の内周面にその軸方向に沿って延びる複数の溝を有するため、そのリブレット効果により乱流摩擦抵抗を減少させることによって、透過水流れによる圧力損失を低減できる。   According to the present invention, since only the grooves are provided on the inner peripheral surface of the water collecting pipe, the outer diameter and inner diameter of the water collecting pipe do not change, so the membrane area of the separation membrane is not reduced, and the strength of the water collecting pipe is reduced. There is no problem. Moreover, since it has several groove | channels extended along the axial direction in the internal peripheral surface of a water collection pipe | tube, the pressure loss by a permeate flow can be reduced by reducing turbulent frictional resistance by the riblet effect.

上記において、前記複数の溝が、集水管の軸方向に平行な溝であることが好ましい。このように、軸方向に平行な溝であると、圧力損失をより低減することができ、加工性も良好になる。   In the above, it is preferable that the plurality of grooves are grooves parallel to the axial direction of the water collecting pipe. Thus, when the groove is parallel to the axial direction, the pressure loss can be further reduced, and the workability is also improved.

以下、本発明の実施の形態について、図面を参照しながら説明する。図1は、本発明のスパイラル型分離膜エレメントの製造方法の一例を示す工程図である。図2は、本発明のスパイラル型分離膜エレメントの一例を示す部分破断した斜視図である。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a process diagram showing an example of a method for producing a spiral separation membrane element of the present invention. FIG. 2 is a partially broken perspective view showing an example of the spiral separation membrane element of the present invention.

本発明のスパイラル型分離膜エレメントは、集水管の内周面の形状のみが従来のものと異なっており、他の構造、材料などについては、従来のスパイラル型分離膜エレメントの構成をいずれも適用することができる。   The spiral type separation membrane element of the present invention is different from the conventional one only in the shape of the inner peripheral surface of the water collecting pipe, and the structure of the conventional spiral type separation membrane element is applied to other structures and materials. can do.

本発明のスパイラル型分離膜エレメントは、図1〜2に示すように、分離膜1、供給側流路材2、および透過側流路材3が積層状態で、有孔の集水管5の周囲にスパイラル状に巻回されている。この円筒状巻回体Rに対し、通常、供給側流体と透過側流体の混合を防ぐための封止部が設けられている。封止部には、両端封止部11と外周側封止部12が含まれる。   As shown in FIGS. 1 and 2, the spiral separation membrane element of the present invention includes a separation membrane 1, a supply-side flow channel material 2, and a permeation-side flow channel material 3 in a laminated state, and around a perforated water collecting pipe 5. It is wound in a spiral shape. The cylindrical wound body R is usually provided with a sealing portion for preventing mixing of the supply side fluid and the permeation side fluid. The sealing portion includes a both-end sealing portion 11 and an outer peripheral side sealing portion 12.

図2に示すように、透過側流路材3を介して対向する分離膜1の両端は、両端封止部11により封止され、スパイラル状に配置された複数の両端封止部11の間には、供給側流路材2が介在する。また、透過側流路材3を介して対向する分離膜1の外周側端部は、軸方向に沿った外周側封止部12により封止されている。   As shown in FIG. 2, both ends of the separation membrane 1 facing each other through the permeate-side flow path member 3 are sealed by a both-end sealing portion 11 and between a plurality of both-end sealing portions 11 arranged in a spiral shape. The supply-side flow path material 2 is interposed between them. Moreover, the outer peripheral side edge part of the separation membrane 1 which opposes via the permeation | transmission side channel material 3 is sealed by the outer peripheral side sealing part 12 along the axial direction.

円筒状巻回体Rは、分離膜1と供給側流路材2と透過側流路材3とを積層状態で有孔の集水管5の周囲にスパイラル状に巻回して円筒状巻回体Rを形成する工程と、供給側流体と透過側流体の混合を防ぐための封止部11,12を形成する工程とによって製造することができる。   The cylindrical wound body R is formed by spirally winding the separation membrane 1, the supply-side flow path member 2, and the permeate-side flow path member 3 around the perforated water collecting pipe 5. It can be manufactured by a process of forming R and a process of forming the sealing portions 11 and 12 for preventing mixing of the supply side fluid and the permeate side fluid.

具体的には、例えば、図1に示す実施形態により製造することができる。図1の(a)は、分離膜ユニットの組立斜視図であり、(b)は、分離膜ユニットを積層して巻回する前の状態を示す正面図である。   Specifically, for example, it can be manufactured by the embodiment shown in FIG. FIG. 1A is an assembled perspective view of a separation membrane unit, and FIG. 1B is a front view showing a state before the separation membrane units are stacked and wound.

まず、図1(a)に示すように、分離膜1を二つ折りにした間に供給側流路材2を配置したものと透過側流路材3とを積み重ね、供給側流体と透過側流体の混合を防ぐ封止部を形成するための接着剤4,6を、透過側流路材3の軸方向両端部および巻回終端部に塗布したユニットを準備する。このとき、分離膜1の折目部分に保護テープを貼り付けても良い。   First, as shown in FIG. 1 (a), the supply-side fluid 3 and the permeation-side fluid 3 are stacked while the separation membrane 1 is folded in half. A unit is prepared in which adhesives 4 and 6 for forming a sealing portion that prevents the mixing of these are applied to both end portions in the axial direction and winding end portions of the permeate-side flow path member 3. At this time, a protective tape may be attached to the fold portion of the separation membrane 1.

分離膜1には、逆浸透膜、限外ろ過膜、精密ろ過膜、ガス分離膜、脱ガス膜などが使用できる。供給側流路材2には、ネット状材料、メッシュ状材料、溝付シート、波形シート等が使用できる。透過側流路材3には、ネット状材料、メッシュ状材料、溝付シート、波形シート等が使用できる。   As the separation membrane 1, a reverse osmosis membrane, an ultrafiltration membrane, a microfiltration membrane, a gas separation membrane, a degassing membrane, or the like can be used. For the supply-side channel material 2, a net-like material, a mesh-like material, a grooved sheet, a corrugated sheet, or the like can be used. For the permeate-side channel material 3, a net-like material, a mesh-like material, a grooved sheet, a corrugated sheet or the like can be used.

接着剤4,6としては、ウレタン系接着剤、エポキシ系接着剤、ホットメルト接着剤等、従来公知の何れの接着剤も使用することができる。   As the adhesives 4 and 6, any conventionally known adhesives such as urethane adhesives, epoxy adhesives, hot melt adhesives and the like can be used.

次に、図1(b)に示すように、この分離膜ユニットUの複数を積層し、有孔の集水管5の周囲にスパイラル状に巻回した後、接着剤などを熱により硬化等させることで、円筒状巻回体Rを得る。その際、集水管5の周囲の封止を同時に行っても良い。円筒状巻回体Rは、軸方向の長さを調整するために、必要に応じて両端部がトリミング等される。   Next, as shown in FIG. 1B, a plurality of the separation membrane units U are stacked, wound around the perforated water collecting pipe 5 in a spiral shape, and then the adhesive is cured by heat or the like. Thus, the cylindrical wound body R is obtained. At that time, sealing around the water collecting pipe 5 may be performed simultaneously. The cylindrical wound body R is trimmed at both ends as necessary in order to adjust the length in the axial direction.

分離膜ユニットUを積層する際の数量は、必要とされる透過流量に応じて決まるものであり、1層以上であれば良いが、操作性を考慮すると100層程度が上限である。なお、分離膜ユニットUの積層数量が大きいほど、各分離膜ユニットUの巻回回数が少なくなる。   The number when the separation membrane unit U is stacked is determined according to the required permeation flow rate and may be one or more layers, but about 100 layers is the upper limit in consideration of operability. In addition, the winding number of each separation membrane unit U decreases as the number of stacked separation membrane units U increases.

本発明は、上記のようなスパイラル型分離膜エレメントにおいて、集水管5の内周面には、集水管5の軸方向に沿って延びる複数の溝5aを有することを特徴とする。有孔の集水管5は、管の周囲に開孔を有するものであり、集水管5の材質は、樹脂、金属など何れでもよいが、ノリル樹脂、ABS樹脂等のプラスチックが通常使用される。   In the spiral separation membrane element as described above, the present invention is characterized in that the inner peripheral surface of the water collecting pipe 5 has a plurality of grooves 5 a extending along the axial direction of the water collecting pipe 5. The perforated water collecting pipe 5 has an opening around the pipe, and the material of the water collecting pipe 5 may be any of resin, metal, etc., but plastics such as noryl resin and ABS resin are usually used.

溝5aは透過水流れ方向(図3の矢印の方向)と沿うように、集水管5の軸方向に沿って延びるものであり、集水管の軸方向に平行な溝が好ましいが、軸方向から若干傾斜した溝(らせん状溝など)などでもよい。また、溝5aは、集水管5の全長に設けてもよいが、流速が大きくなる下流側だけに設けたり、装着に関与する集水管5の端部を除く、中間部だけに溝5aを設けてもよい。中間部だけに溝5aを設けてることによって、従来の端部のシール構造をそのまま使用できるという効果が生じる。   The groove 5a extends along the axial direction of the water collecting pipe 5 so as to be along the permeate flow direction (the direction of the arrow in FIG. 3), and is preferably a groove parallel to the axial direction of the water collecting pipe. A slightly inclined groove (such as a spiral groove) may be used. Moreover, although the groove 5a may be provided in the full length of the water collection pipe 5, it is provided only in the downstream side where the flow velocity increases, or the groove 5a is provided only in the middle part excluding the end of the water collection pipe 5 involved in the mounting. May be. By providing the groove 5a only at the intermediate portion, an effect that the conventional end seal structure can be used as it is is produced.

溝5aの形状としては、何れの断面形状を有するものでもよく、例えば図3〜図6に示すような、V溝、U溝、角溝、半円溝等が挙げられる。このような溝5aの形状は、集水管5を押出成形する際に形成したり、成型後に溝加工することによって形成することができる。なお、溝5aの本数は、集水管5の内径にもよるが、10〜2000本が好ましい。
溝5aの各部の寸法は、圧力損失の低減効果と壁面近傍の流れ変化を考慮すると、次の寸法が好ましい。即ち、溝5aの高さhは、0.05〜3mmが好ましく、0.1〜1.5mmがより好ましい。幅Wは0.05〜6mmが好ましく、0.1〜3mmがより好ましい。間隔iは、0〜5mmが好ましい。
The shape of the groove 5a may have any cross-sectional shape, and examples thereof include a V groove, a U groove, a square groove, and a semicircular groove as shown in FIGS. Such a shape of the groove 5a can be formed when the water collecting pipe 5 is formed by extrusion, or by forming a groove after forming. In addition, although the number of the groove | channel 5a is based also on the internal diameter of the water collecting pipe 5, 10-2000 are preferable.
The dimensions of each part of the groove 5a are preferably the following dimensions in consideration of the effect of reducing the pressure loss and the flow change in the vicinity of the wall surface. That is, the height h of the groove 5a is preferably 0.05 to 3 mm, and more preferably 0.1 to 1.5 mm. The width W is preferably 0.05 to 6 mm, and more preferably 0.1 to 3 mm. The interval i is preferably 0 to 5 mm.

本発明のスパイラル型分離膜エレメントは、通常、外装材により拘束されて拡径しない構造になっているが、外装材は、円筒状巻回体の表面に単数又は複数のシートを巻回することができる。外装材としては、ポリエステル、ポリプロピレン、ポリエチレン、ポリ塩化ビニル、ガラス繊維布等が使用できる。   The spiral separation membrane element of the present invention is usually constrained by an exterior material and does not expand in diameter, but the exterior material is formed by winding one or more sheets on the surface of a cylindrical wound body. Can do. As the exterior material, polyester, polypropylene, polyethylene, polyvinyl chloride, glass fiber cloth, or the like can be used.

本発明のスパイラル型分離膜エレメントには、更に変形(テレスコープ等)を防止するための有孔の端部材や、シール材、補強材などを必要に応じて設けることができる。   The spiral separation membrane element of the present invention can be further provided with a perforated end member for preventing deformation (telescope or the like), a sealing material, a reinforcing material, and the like as necessary.

[他の実施形態]
(1)前述の実施形態では、分離膜ユニットを作製する際、分離膜を2つ折りにして供給側流路材を挟み込む例を示したが、連続する分離膜を用いて、これを交互に折り返して、供給側流路材および透過側流路材を挟み込むことも可能である。その場合、両端封止部に対してのみ、透過側流路材の切除部を設ければよい。
[Other Embodiments]
(1) In the above-described embodiment, when the separation membrane unit is manufactured, the separation membrane is folded in half and the supply-side channel material is sandwiched. However, the separation membrane unit is folded back alternately using a continuous separation membrane. It is also possible to sandwich the supply-side channel material and the permeation-side channel material. In that case, it suffices to provide a cut-out portion of the permeate-side channel material only for the both-end sealed portions.

(2)前述の実施形態では、図1に示すように、供給側流路材2を挟みこむように二つ折りにした分離膜1の上に、透過側流路材3を重ねて、接着剤4,6を塗布する例で説明したが、本発明では、透過側流路材3の上に二つ折りにした分離膜1を重ねその上に接着剤4,6を塗布することも可能である。   (2) In the above-mentioned embodiment, as shown in FIG. In the present invention, it is also possible to apply the adhesives 4 and 6 on the separation membrane 1 that is folded in two on the permeate-side channel material 3.

(3)前述の実施形態では、図1に示すように、複数の分離膜ユニットUを使用して、複数の膜リーフを備えるスパイラル膜エレメントを製造する例を示したが、本発明では、 1組の分離膜ユニットUを使用して、1枚の膜リーフを備えるスパイラル膜エレメントを製造してもよい。   (3) In the above-described embodiment, as shown in FIG. 1, an example in which a spiral membrane element including a plurality of membrane leaves is manufactured using a plurality of separation membrane units U has been described. A spiral membrane element having one membrane leaf may be manufactured using a set of separation membrane units U.

以下、本発明の構成と効果を具体的に示す実施例等について説明する。なお、実施例等における評価項目は下記のようにして測定を行った。   Examples and the like specifically showing the configuration and effects of the present invention will be described below. In addition, the evaluation item in an Example etc. measured as follows.

(1)圧力損失
圧力損失は、集水管の入口と出口に圧力計を設置し、その差圧を圧力損失として求めた。
(1) Pressure loss Pressure loss was obtained by installing pressure gauges at the inlet and outlet of the water collection pipe and calculating the differential pressure as pressure loss.

(2)透過性能
運転開始から10分後、透過水配管中の流量計の値を1日当たりの流量(m/d)に換算した。
(2) Permeation performance 10 minutes after the start of operation, the value of the flow meter in the permeate pipe was converted to the flow rate per day (m 3 / d).

(3)阻止率
透過液を通水してから10分後にサンプリングし、そのNaCl濃度から原液濃度を基準にして、阻止率(%)を求めた。
(3) Blocking rate The sample was taken 10 minutes after passing the permeate, and the blocking rate (%) was determined from the NaCl concentration based on the stock solution concentration.

比較例1
内径26.7mm、外径38mmのノリル樹脂製の集水管を使用し、膜面積37mのスパイラル型逆浸透膜エレメント(内径28.65mm)を作った。このエレメントの性能を1500ppmNaCl水溶液で、圧力1.55MPaの条件下で評価したところ、透過性能41m/d、阻止率は99.77%であった。この時、集水管中の圧力損失は242Paであった。
Comparative Example 1
A spiral type reverse osmosis membrane element (inner diameter 28.65 mm) having a membrane area of 37 m 2 was made using a water collecting tube made of Noryl resin having an inner diameter of 26.7 mm and an outer diameter of 38 mm. The performance of this element was evaluated with a 1500 ppm NaCl aqueous solution under a pressure of 1.55 MPa. As a result, the permeation performance was 41 m 3 / d, and the rejection was 99.77%. At this time, the pressure loss in the water collecting pipe was 242 Pa.

実施例1
高さ(h)1mm、幅(w)1.3mm、間隔(i)0mmの軸方向に平行なV溝を内周面に69本有するノリル樹脂製集水管を使用した以外は、比較例と同じエレメントを作った。このエレメントの性能を1500ppmNaClで、1.55MPaの条件下で評価したところ、透過性能42m/d、阻止率は99.70%であった。この時、集水管中の圧力損失は223Paであった。このように、集水管内部にV溝を設置することで、圧力損失が7.8%低減できた。
Example 1
Except for using a water collecting pipe made of Noryl resin having 69 V-grooves on the inner peripheral surface parallel to the axial direction of height (h) 1 mm, width (w) 1.3 mm, and interval (i) 0 mm, Made the same element. When the performance of this element was evaluated at 1500 ppm NaCl under the condition of 1.55 MPa, the permeation performance was 42 m 3 / d and the rejection rate was 99.70%. At this time, the pressure loss in the water collecting pipe was 223 Pa. Thus, the pressure loss could be reduced by 7.8% by installing the V groove inside the water collecting pipe.

本発明のスパイラル型分離膜エレメントの製造方法の一例を示す工程図Process drawing which shows an example of the manufacturing method of the spiral type separation membrane element of this invention 本発明のスパイラル型分離膜エレメントの一例を示す部分破断した斜視図The partially broken perspective view which shows an example of the spiral type separation membrane element of this invention 本発明のスパイラル型分離膜エレメントの要部の一例を示す斜視図The perspective view which shows an example of the principal part of the spiral-type separation membrane element of this invention 本発明のスパイラル型分離膜エレメントの要部の他の例を示す断面図Sectional drawing which shows the other example of the principal part of the spiral type separation membrane element of this invention 本発明のスパイラル型分離膜エレメントの要部の他の例を示す断面図Sectional drawing which shows the other example of the principal part of the spiral type separation membrane element of this invention 本発明のスパイラル型分離膜エレメントの要部の他の例を示す断面図Sectional drawing which shows the other example of the principal part of the spiral type separation membrane element of this invention

符号の説明Explanation of symbols

1 分離膜
2 供給側流路材
3 透過側流路材
4 接着剤
5 集水管
5a 溝
6 接着剤
DESCRIPTION OF SYMBOLS 1 Separation membrane 2 Supply side flow path material 3 Permeation side flow path material 4 Adhesive 5 Water collecting pipe 5a Groove 6 Adhesive

Claims (2)

分離膜、供給側流路材及び透過水側流路材が積層状態で有孔の集水管の周囲にスパイラル状に巻回されたスパイラル型分離膜エレメントにおいて、
前記集水管の内周面には、集水管の軸方向に沿って延びる複数の溝を有することを特徴とするスパイラル型分離膜エレメント。
In the spiral-type separation membrane element in which the separation membrane, the supply-side channel material and the permeate-side channel material are spirally wound around the perforated water collecting pipe in a laminated state,
A spiral separation membrane element having a plurality of grooves extending along an axial direction of the water collecting pipe on an inner peripheral surface of the water collecting pipe.
前記複数の溝が、集水管の軸方向に平行な溝である請求項1記載のスパイラル型分離膜エレメント。   The spiral separation membrane element according to claim 1, wherein the plurality of grooves are grooves parallel to the axial direction of the water collecting pipe.
JP2005308347A 2005-10-24 2005-10-24 Spiral separation membrane element Pending JP2007111674A (en)

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Cited By (5)

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WO2012057938A1 (en) * 2010-10-29 2012-05-03 General Electric Company Spiral wound membrane element product water tube with external flow grooves
CN102946978A (en) * 2010-06-18 2013-02-27 日东电工株式会社 Spiral separation membrane element, porous hollow tube and production method for same
WO2012158896A3 (en) * 2011-05-17 2013-04-18 Natrix Separations Inc. Layered tubular membranes for chromatography, and methods of use thereof
CN104474901A (en) * 2014-11-25 2015-04-01 武汉纺织大学 Water filer roll type membrane component with double-channel central tube structure
US10800808B2 (en) 2008-09-02 2020-10-13 Merck Millipore Ltd. Chromatography membranes, devices containing them, and methods of use thereof

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10800808B2 (en) 2008-09-02 2020-10-13 Merck Millipore Ltd. Chromatography membranes, devices containing them, and methods of use thereof
US10981949B2 (en) 2008-09-02 2021-04-20 Merck Millipore Ltd. Chromatography membranes, devices containing them, and methods of use thereof
US11884701B2 (en) 2008-09-02 2024-01-30 Merck Millipore Ltd. Chromatography membranes, devices containing them, and methods of use thereof
CN102946978A (en) * 2010-06-18 2013-02-27 日东电工株式会社 Spiral separation membrane element, porous hollow tube and production method for same
WO2012057938A1 (en) * 2010-10-29 2012-05-03 General Electric Company Spiral wound membrane element product water tube with external flow grooves
CN103201021A (en) * 2010-10-29 2013-07-10 通用电气公司 Spiral wound membrane element product water tube with external flow grooves
WO2012158896A3 (en) * 2011-05-17 2013-04-18 Natrix Separations Inc. Layered tubular membranes for chromatography, and methods of use thereof
US9873088B2 (en) 2011-05-17 2018-01-23 Natrix Separations Inc. Layered tubular membranes for chromatography, and methods of use thereof
US10195567B2 (en) 2011-05-17 2019-02-05 Natrix Separations Inc. Layered tubular membranes for chromatography, and methods of use thereof
US10874990B2 (en) 2011-05-17 2020-12-29 Merck Millipore Ltd. Layered tubular membranes for chromatography, and methods of use thereof
CN104474901A (en) * 2014-11-25 2015-04-01 武汉纺织大学 Water filer roll type membrane component with double-channel central tube structure

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