JP4484685B2 - Spiral separation membrane element and manufacturing apparatus thereof - Google Patents

Spiral separation membrane element and manufacturing apparatus thereof Download PDF

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JP4484685B2
JP4484685B2 JP2004356435A JP2004356435A JP4484685B2 JP 4484685 B2 JP4484685 B2 JP 4484685B2 JP 2004356435 A JP2004356435 A JP 2004356435A JP 2004356435 A JP2004356435 A JP 2004356435A JP 4484685 B2 JP4484685 B2 JP 4484685B2
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central tube
separation membrane
membrane element
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JP2006159122A (en
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隆幸 増井
達也 小栗栖
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Nitto Denko Corp
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本発明は、分離膜を用いて逆浸透技術、櫨過技術等により流体の成分を分離するスパイラル型分離膜エレメント及びその製造装置に関する。   The present invention relates to a spiral separation membrane element that uses a separation membrane to separate components of a fluid by a reverse osmosis technique, a filtration technique, and the like, and an apparatus for manufacturing the same.

従来から、工場やビルなどにおける排水処理あるいは精製水供給には、多くの濾過装置が使用されている。特に、近年半導体製造工程における処理水などにおいては、高度な精密濾過装置が要求され、精密濾過膜(MF膜)や限外濾過膜(UF膜)あるいは逆浸透膜(RO膜)などを利用したスパイラル型分離膜エレメント(以下、膜エレメントと言う)が多用されている。   Conventionally, many filtration devices have been used for wastewater treatment or purified water supply in factories and buildings. In particular, advanced microfiltration devices are required for treated water in semiconductor manufacturing processes in recent years, and microfiltration membranes (MF membranes), ultrafiltration membranes (UF membranes), and reverse osmosis membranes (RO membranes) are used. Spiral type separation membrane elements (hereinafter referred to as membrane elements) are frequently used.

こうした膜エレメントの構造としては、図1に示す分離膜2、供給側流路材6および透過側流路材3の複数が、有孔の中空状中心管5の周りに渦巻き状に巻き付けられた膜エレメント1が知られている。この膜エレメント1において、原液7は一端面より供給され他端面より濃縮液9が取り出される。原液7は供給側流路材6に導かれる間に、分離膜2で濾過された透過液8は透過側流路材3を通り、中空状中心管5の孔を通って取り出される。また、透過液や洗浄液を用いた逆流洗浄の場合は、逆に中心管5に逆流洗浄液が供給され孔から分散供給され分離膜2の裏側から洗浄して洗浄排水として排出される(例えば、下記特許文献1参照)。   As a structure of such a membrane element, a plurality of separation membranes 2, a supply-side channel material 6 and a permeation-side channel material 3 shown in FIG. 1 are wound around a perforated hollow central tube 5 in a spiral shape. A membrane element 1 is known. In the membrane element 1, the stock solution 7 is supplied from one end surface, and the concentrated solution 9 is taken out from the other end surface. While the stock solution 7 is guided to the supply-side channel material 6, the permeate 8 filtered by the separation membrane 2 passes through the permeation-side channel material 3 and is taken out through the hole of the hollow central tube 5. In the case of back-flow cleaning using a permeate or cleaning liquid, the back-flow cleaning liquid is supplied to the central tube 5 in a dispersed manner, dispersedly supplied from the holes, cleaned from the back side of the separation membrane 2 and discharged as cleaning waste water (for example, Patent Document 1).

ここで、分離膜2等の中心管5への巻き付けは、例えば中心管5内部に駆動シャフトを挿入し、分離膜2等に張力を加えながら、この駆動シャフトを回転させることにより行っていた。   Here, the winding of the separation membrane 2 or the like around the central tube 5 is performed, for example, by inserting a drive shaft into the central tube 5 and rotating the drive shaft while applying tension to the separation membrane 2 or the like.

しかし、中心管5の内部形状が円形であると、張力が中心管5の内壁面と駆動シャフトとの間で生じる摩擦力よりも大きい場合には、両者の間で滑りが生じる。その結果、中心管5の内壁面に駆動シャフトがキズを付けるという問題があった。   However, if the inner shape of the center tube 5 is circular, if the tension is greater than the frictional force generated between the inner wall surface of the center tube 5 and the drive shaft, slip occurs between the two. As a result, there has been a problem that the drive shaft is scratched on the inner wall surface of the central tube 5.

また、十分な張力で分離膜2等を引っ張ることができないことから、特に中心管5の近傍で隙間が発生していた。膜エレメント1をハウジング等に収納する際には、ハウジング等のスペース上の制約が有ることから、膜エレメントの大きさを極力抑制する必要がある。しかし、前述のように隙間が生じるような巻き付けであると、ハウジング等に収納可能な範囲内で、より膜面積の大きい分離膜を巻き付けることができず、従って膜面積が大きく分離性能に優れた膜エレメントが得難いという問題もあった。
特開平10−137558号公報
Further, since the separation membrane 2 and the like cannot be pulled with sufficient tension, a gap is generated particularly near the central tube 5. When the membrane element 1 is housed in a housing or the like, the size of the membrane element needs to be suppressed as much as possible due to space limitations of the housing and the like. However, if the winding is such that a gap is generated as described above, it is not possible to wind a separation membrane having a larger membrane area within the range that can be accommodated in a housing or the like, and thus the membrane area is large and the separation performance is excellent. There was also a problem that it was difficult to obtain a membrane element.
JP 10-137558 A

本発明は前記問題点に鑑みなされたものであり、その目的は、有効な膜面積を拡大して分離性能を向上させることが可能なスパイラル型分離膜エレメント、及びその製造装置を提供することにある。   The present invention has been made in view of the above problems, and an object of the present invention is to provide a spiral separation membrane element capable of expanding an effective membrane area and improving separation performance, and a manufacturing apparatus thereof. is there.

本願発明者等は、前記従来の問題点を解決すべく、スパイラル型分離膜エレメント及びその製造装置について鋭意検討した。その結果、下記構成を採用することにより前記目的を達成できることを見出して、本発明を完成させるに至った。   In order to solve the above-described conventional problems, the inventors of the present application have made extensive studies on a spiral separation membrane element and a manufacturing apparatus therefor. As a result, the inventors have found that the object can be achieved by adopting the following configuration, and have completed the present invention.

すなわち、本発明に係るスパイラル型分離膜エレメントは、前記の課題を解決する為に、分離膜の間に供給側流路材を配置した分離膜ユニットと透過側流路材とを交互に重ねた積層体を、有孔の中空状中心管の周囲に巻回したスパイラル型分離膜エレメントに於いて、前記中心管の外形はその断面において円形であり、前記中心管の端部の内壁面はその断面において円形状を有し、それ以外の内壁面はその断面において楕円形状を有するものであり、相対回転を係止可能な楕円形状の外形を有する駆動シャフトの挿入を許容する形状であることを特徴とする。 That is, in order to solve the above-described problem, the spiral separation membrane element according to the present invention is formed by alternately stacking separation membrane units and permeation side flow passage materials in which supply side flow passage materials are arranged between separation membranes. In a spiral separation membrane element in which a laminate is wound around a perforated hollow central tube, the outer shape of the central tube is circular in cross section, and the inner wall surface at the end of the central tube is The cross section has a circular shape, and the other inner wall surface has an elliptical shape in its cross section, and has a shape that allows insertion of a drive shaft having an elliptical outer shape that can lock relative rotation. Features.

また、本発明に係るスパイラル型分離膜エレメントの製造装置は、前記の課題を解決する為に、分離膜の間に供給側流路材を配置した分離膜ユニットと透過側流路材とを交互に重ねた積層体を、有孔の中空状中心管の周囲に巻回する手段を備えたスパイラル型分離膜エレメントの製造装置に於いて、
前記中心管の内部に挿入して該中心管を回転させ、中心管の周囲に前記積層体を巻回させる為の駆動シャフトであって、
外形はその断面において円形であり、端部の内壁面はその断面において円形状を有し、それ以外の内壁面はその断面において楕円形状を有する前記中心管に対し、相対回転を係止可能な楕円形状の外形を有する駆動シャフトを有することを特徴とする。
In addition, in order to solve the above-described problems, the manufacturing apparatus for a spiral separation membrane element according to the present invention alternately includes a separation membrane unit in which a supply-side channel material is disposed between separation membranes and a permeation-side channel material. In the manufacturing apparatus of the spiral separation membrane element provided with means for winding the laminated body on the periphery of the perforated hollow central tube,
A drive shaft for inserting the inside of the central tube to rotate the central tube and winding the laminate around the central tube;
The outer shape is circular in the cross section, the inner wall surface of the end portion has a circular shape in the cross section, and the other inner wall surfaces can lock relative rotation with respect to the central tube having the elliptical shape in the cross section. A drive shaft having an elliptical outer shape is provided.

本発明は、前記に説明した手段により、以下に述べるような効果を奏する。   The present invention has the following effects by the means described above.

すなわち、本発明に係るスパイラル型分離膜エレメントによれば、中心管の内壁面が、相対回転を係止可能な外形を有する駆動シャフトの挿入を許容する形状であるので、該駆動シャフトを用いて中心管を軸回転させ積層体を巻回させた場合、その中心管の内壁面が傷付くのを防止することができる。さらに、積層体に大きな張力を加えて巻回させることも可能になり、また集水管長手方向に対し均一に駆動力をかけることができ、これにより積層体にシワが発生したり、或いは中心管の巻き始め部分に隙間が生じるのを無くすこともできる。その結果、サイズが大きくなるのを抑制しつつできるだけ面積の大きい分離膜を中心管に巻き付けることができ、分離性能に優れたスパイラル型分離膜エレメントを提供することができる。   That is, according to the spiral-type separation membrane element of the present invention, the inner wall surface of the center tube has a shape that allows insertion of a drive shaft having an outer shape that can lock relative rotation. When the central tube is rotated and the laminate is wound, the inner wall surface of the central tube can be prevented from being damaged. Furthermore, it is possible to wind the laminated body with a large tension, and it is possible to apply a driving force uniformly in the longitudinal direction of the water collecting pipe, which causes wrinkles in the laminated body or the central pipe. It is also possible to eliminate the occurrence of a gap at the winding start portion. As a result, a separation membrane having as large an area as possible can be wound around the central tube while suppressing an increase in size, and a spiral separation membrane element having excellent separation performance can be provided.

また、本発明に係るスパイラル型分離膜エレメントの製造装置によれば、スパイラル型分離膜エレメントに於ける中心管の内部で、相対回転を係止可能な外形を有する駆動シャフトを備えているので、中心管に積層体を巻き付ける際には、中心管の内壁面を傷付けることなく回転させることができる。また、積層体に大きな張力を加えつつ巻回させることも可能になる。これにより、積層体に隙間やシワが発生するのを防止し、サイズが大きくなるのを抑制しつつできるだけ面積の大きい分離膜を中心管に巻き付けて製造することができる。従って、本発明によれば、分離性能に優れたスパイラル型分離膜エレメントの製造が可能な製造装置を提供することができる。   Further, according to the spiral separation membrane element manufacturing apparatus according to the present invention, since the drive shaft having an outer shape capable of locking relative rotation is provided inside the central tube in the spiral separation membrane element, When the laminate is wound around the central tube, it can be rotated without damaging the inner wall surface of the central tube. In addition, the laminate can be wound while applying a large tension. As a result, it is possible to manufacture a separation membrane having as large an area as possible around the central tube while preventing gaps and wrinkles from occurring in the laminate and suppressing an increase in size. Therefore, according to this invention, the manufacturing apparatus which can manufacture the spiral-type separation membrane element excellent in the separation performance can be provided.

本発明の実施の形態について、図を参照しながら以下に説明する。尚、本発明に係るスパイラル型分離膜エレメント(以下、膜エレメントという)は、中心管内面の形状のみが従来のものと異なっており、他の構造は上述の従来の膜エレメントの構成を適用することができる。したがって、ここでは、再度図1を参照して本実施の形態に係る膜エレメントの構成の一例について説明する。   Embodiments of the present invention will be described below with reference to the drawings. The spiral type separation membrane element (hereinafter referred to as membrane element) according to the present invention is different from the conventional one only in the shape of the inner surface of the central tube, and the other structure applies the configuration of the conventional membrane element described above. be able to. Therefore, here, an example of the configuration of the membrane element according to the present embodiment will be described with reference to FIG. 1 again.

図1に示すように、本実施の形態に係る膜エレメント1は、合成樹脂のネットからなる透過側流路材3の両面に分離膜2を重ね合わせて3辺を接着することにより封筒状膜(袋状膜)4を形成し、その封筒状膜4の開口部を中心管5に取付け、合成樹脂のネットからなる供給側流路材6とともに中心管5の外周面にスパイラル状に巻回することにより構成される。   As shown in FIG. 1, the membrane element 1 according to the present embodiment has an envelope-like membrane by superposing separation membranes 2 on both surfaces of a permeation-side flow path material 3 made of a synthetic resin net and adhering three sides. (Bag-like membrane) 4 is formed, and the opening of the envelope-like membrane 4 is attached to the central tube 5 and spirally wound around the outer peripheral surface of the central tube 5 together with the supply-side flow path member 6 made of a synthetic resin net. It is constituted by doing.

前記分離膜2は、例えば不織布層上に多孔性支持体及びスキン層(緻密層)が順次積層された構造を有する。不織布層の構成材料としては特に限定されるものではなく、従来公知のものを採用することができる。   The separation membrane 2 has a structure in which, for example, a porous support and a skin layer (dense layer) are sequentially laminated on a nonwoven fabric layer. It does not specifically limit as a constituent material of a nonwoven fabric layer, A conventionally well-known thing is employable.

前記多孔性支持体の構成材料としては、従来公知のものを採用することができる。具体的には、例えば、ポリスルホン、ポリエーテルスルホン等のポリアリールエーテルスルホン、ポリイミド、ポリフッ化ビニリデン等が例示できる。   As the constituent material of the porous support, conventionally known materials can be employed. Specifically, for example, polyarylethersulfone such as polysulfone and polyethersulfone, polyimide, polyvinylidene fluoride and the like can be exemplified.

前記スキン層は、流体に含まれる分離対象物質に対し透過性を示さない分離機能を有する。スキン層を構成する材料としては、特に限定されるものではなく、従来公知のものを採用することができる。具体的には、例えば、PE、PP、PET、ナイロン、ポリアミド、ポリアクリロニトリル(PAN)、ポリビニルアルコール(PVA)、PMMA、ポリサルホン、ポリエーテルサルホン、ポリイミド、エチレン−ビニルアルコール共重合体等が例示できる。   The skin layer has a separation function that does not exhibit permeability to the separation target substance contained in the fluid. The material constituting the skin layer is not particularly limited, and conventionally known materials can be adopted. Specific examples include PE, PP, PET, nylon, polyamide, polyacrylonitrile (PAN), polyvinyl alcohol (PVA), PMMA, polysulfone, polyethersulfone, polyimide, and ethylene-vinyl alcohol copolymer. it can.

前記供給側流路材6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。また、透過側流路材3には、ネット状材料、編み物状材料、メッシュ状材料、溝付シート、波形シート等が使用できる。   For the supply-side channel material 6, 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 knitted material, a mesh-like material, a grooved sheet, a corrugated sheet, or the like can be used.

前記中心管5は、図2に示すように、管の周囲に複数の開孔を有する構造である。中心管5の内壁面10は、その断面に於いて正六角形状となっており、後述の駆動シャフトの挿入を許容する形状を有している。この様な内壁面10であると、駆動シャフトが回転することにより中心管5に伝達される力は、中心管5の内壁面10を、回転させようとする方向(巻回方向)側に押す力となる。この力が中心管5を回転させる駆動力となる。一方、従来の円形状であると、中心管5を回転させる駆動力は、中心管5の内壁と駆動シャフトとの接触面に生じる摩擦力だけである。この場合、巻き付ける分離膜2等に張力を加えたりすると、中心管5の内壁面10と駆動シャフトとの間で滑りを生じる場合が多く、その結果内壁面10を傷付けたり、中心管5の近傍等で積層体間に隙間が生じたりする。尚、中心管5の内壁面10の断面に於ける形状は、軸方向に於いて同一であることが好ましい。   As shown in FIG. 2, the central tube 5 has a structure having a plurality of openings around the tube. The inner wall surface 10 of the central tube 5 has a regular hexagonal shape in its cross section, and has a shape that allows insertion of a drive shaft, which will be described later. With such an inner wall surface 10, the force transmitted to the central tube 5 by the rotation of the drive shaft pushes the inner wall surface 10 of the central tube 5 toward the direction (winding direction) in which it is intended to rotate. It becomes power. This force becomes a driving force for rotating the central tube 5. On the other hand, in the conventional circular shape, the driving force for rotating the center tube 5 is only the friction force generated on the contact surface between the inner wall of the center tube 5 and the drive shaft. In this case, if tension is applied to the separation membrane 2 or the like to be wound, slippage often occurs between the inner wall surface 10 of the central tube 5 and the drive shaft. As a result, the inner wall surface 10 is damaged or the vicinity of the central tube 5 For example, a gap may be generated between the stacked bodies. In addition, it is preferable that the shape in the cross section of the inner wall surface 10 of the center tube 5 is the same in the axial direction.

ここで、中心管5の断面形状は、図2に示す形状のものに限定されず、例えば図3に示す楕円形状の内壁面11や、図4に示す矩形状の内壁面12とすることもできる。また図5(a)に示す様に、中心管5の端部が円形状の内壁面13を有し、それ以外の部分は正六角形状の内壁面14を有する構造としてもよい。更に、図5(b)に示す正六角形状の内壁面15としてもよい。また中心管5は、円形状の内壁面の一部に溝を設けたものや、軸方向に平行に延在した突条部を設けたものも採用することができる。さらに中心管5は、駆動シャフトがスプライン軸の場合には、少なくとも4条以上のキー溝が軸方向に形成された内壁面を備えたものとすることもできる。この様な形状であると、中心管5に一層大きな回転力を伝達することができる。すなわち、本発明に於いて、中心管5の内壁面は、これを回転させる駆動力が該中心管5と駆動シャフトとの間に生じる摩擦力だけでなく、巻回方向側に押す力が内壁面の少なくとも一部に加わる様なものであれば、特に限定されるものではない。   Here, the cross-sectional shape of the central tube 5 is not limited to the shape shown in FIG. 2, but may be, for example, an elliptical inner wall surface 11 shown in FIG. 3 or a rectangular inner wall surface 12 shown in FIG. it can. Moreover, as shown to Fig.5 (a), the edge part of the center pipe | tube 5 is good also as a structure which has the circular inner wall surface 13, and the other part has the inner wall surface 14 of a regular hexagon. Furthermore, it may be a regular hexagonal inner wall surface 15 shown in FIG. Further, the center tube 5 may be one in which a groove is provided in a part of a circular inner wall surface or one in which a ridge portion extending in parallel with the axial direction is provided. Further, when the drive shaft is a spline shaft, the center tube 5 may be provided with an inner wall surface in which at least four or more key grooves are formed in the axial direction. With such a shape, a larger rotational force can be transmitted to the central tube 5. That is, in the present invention, the inner wall surface of the center tube 5 is not only subjected to a driving force for rotating the inner tube 5 but also a friction force generated between the center tube 5 and the drive shaft, and a force pushing toward the winding direction side. There is no particular limitation as long as it is added to at least a part of the wall surface.

尚、中心管5の回転を防止する点からは、例えば、単にその外形を矩形状にしたり、或いは突起部を設けたりする態様も考えられる。しかしながら、これらの形状であると、円形状に積層体を巻き付けることができず、歪な形状の膜エレメントになるという不都合がある。   From the viewpoint of preventing the rotation of the central tube 5, for example, an aspect in which the outer shape is simply made into a rectangular shape or a protrusion is provided is also conceivable. However, these shapes have the disadvantage that the laminate cannot be wound in a circular shape, resulting in a distorted membrane element.

前記中心管5の構成材料としては特に限定されず、従来公知の樹脂等を採用することができる。また、中心管5の長さ、外径及び内径等も用途等に応じて適宜変更可能である。さらに、中心管5の製造方法についても、従来公知の方法を採用することができる。   The constituent material of the central tube 5 is not particularly limited, and a conventionally known resin or the like can be employed. In addition, the length, outer diameter, inner diameter, and the like of the center tube 5 can be changed as appropriate according to the application. Furthermore, a conventionally well-known method can be adopted as a method for manufacturing the center tube 5.

本実施の形態に係る膜エレメントの製造装置に於いては、中心管5の内部に挿入してこれを回転させ、中心管5の周囲に前記積層体を巻回させる為の駆動シャフトを備える。該駆動シャフトの外形は、中心管5の内壁面の形状及び大きさと合致していることが好ましい。駆動シャフトの回転力を中心管5に有効に伝達させる為である。従って、中心管5の内壁面が、その断面に於いて図2及び3に示すような楕円形状または正四角形状である場合には、駆動シャフトの外形も楕円形状または矩形状とするのが好ましい。また駆動シャフトとしては、円形状の外形の一部に軸方向に平行に延在した突条部を設けたものや、その一部に溝を設けたもの、スプライン軸等を採用することもできる。但し、本発明に於いて、駆動シャフトの外形は前記の場合に限定されず、例えば略円形状を除く形状にする等して中心管5の内壁面との間に相対回転を係止できる構造であれば、その内壁面の形状と必ずしも一致させる必要はない。   The membrane element manufacturing apparatus according to the present embodiment includes a drive shaft that is inserted into the center tube 5 and rotated, and the laminate is wound around the center tube 5. The outer shape of the drive shaft preferably matches the shape and size of the inner wall surface of the central tube 5. This is because the rotational force of the drive shaft is effectively transmitted to the central tube 5. Therefore, when the inner wall surface of the center tube 5 has an elliptical shape or a regular square shape as shown in FIGS. 2 and 3 in its cross section, the outer shape of the drive shaft is also preferably an elliptical shape or a rectangular shape. . Moreover, as a drive shaft, a part provided with a ridge extending in parallel to the axial direction in a part of a circular outer shape, a part provided with a groove, a spline shaft, or the like can be adopted. . However, in the present invention, the outer shape of the drive shaft is not limited to the above case, and a structure that can lock relative rotation with the inner wall surface of the central tube 5 by, for example, a shape other than a substantially circular shape. Then, it is not always necessary to match the shape of the inner wall surface.

前記駆動シャフトの構成材料としては特に限定されず、例えば鋼材など従来公知のものを採用することができる。また、駆動シャフトは、図示しない駆動モーター等の従来公知の駆動装置により駆動される。   The constituent material of the drive shaft is not particularly limited, and a conventionally known material such as a steel material can be employed. The drive shaft is driven by a conventionally known drive device such as a drive motor (not shown).

また、本実施の形態に係る膜エレメントの製造装置は、中心管5に巻き付けられつつある積層体のうち、最外層の積層体の端部に張力を加える手段を備えることが好ましい。これにより、積層体を中心管5の近傍に於いても隙間無く巻き付けることができ、その結果、従来の膜エレメントと比較して面積の一層大きい分離膜2を、従来の膜エレメントと同じサイズ内で巻き付けることが可能になる。その結果、膜有効面積を大きくすることができ、分離性能に優れた膜エレメントを製造することができる。   In addition, the membrane element manufacturing apparatus according to the present embodiment preferably includes means for applying tension to the end of the outermost layered laminate among the laminates being wound around the central tube 5. As a result, the laminate can be wound without any gap even in the vicinity of the central tube 5. As a result, the separation membrane 2 having a larger area compared to the conventional membrane element is within the same size as the conventional membrane element. It becomes possible to wind with. As a result, the membrane effective area can be increased, and a membrane element having excellent separation performance can be produced.

ここで、前記手段としては特に限定されず、例えば積層体の端部を把持して張力を加えることが可能なニップロール等が挙げられる。また、積層体に加える張力は、前記駆動モーターの駆動力等に応じて適宜設定されるのが好ましい。具体的には、例えば2〜5N/エレメント幅の範囲内であることが好ましい。   Here, the means is not particularly limited, and examples thereof include a nip roll capable of gripping the end of the laminated body and applying a tension. Moreover, it is preferable that the tension applied to the laminate is appropriately set according to the driving force of the driving motor. Specifically, for example, it is preferably within a range of 2 to 5 N / element width.

尚、本発明に係る膜エレメントの製造装置に於いて、その他の構成については、従来公知のものを採用し得る。   Incidentally, in the membrane element manufacturing apparatus according to the present invention, conventionally known ones can be adopted for the other configurations.

また、膜エレメント1の表面には、図6(a)〜(d)に示すように、駆動シャフトを用いて中心管5を軸回転させ、膜エレメント1の表面にシート状の外周テープ20を巻回してもよい。この様な場合にも中心管5の内壁面が、相対回転を係止可能な外形を有する駆動シャフトの挿入を許容する形状であるので、その中心管5の内壁面が傷付くのを防止することができる。この外周テープ20に加えるテープテンションは10〜20kgf/75mm(0.13〜0.27kgf/mm、1.31〜2.65N/mm)の範囲内であることが好ましい。同図(a)〜(d)は、所定幅の外周テープ20を軸方向端部に向けてらせん状に巻回した後、他方の軸方向端部に向けてらせん状に巻回し、更に軸方向中央付近に向けてらせん状に巻回する例を示す。即ち、外周テープ20は膜エレメント1の各部において、らせん状に2層分巻回されている。なお、外周テープ20の巻回方向は、膜エレメント1における積層体の巻回方向と同じである。   Further, as shown in FIGS. 6A to 6D, the central tube 5 is axially rotated on the surface of the membrane element 1 using a drive shaft, and a sheet-like outer peripheral tape 20 is placed on the surface of the membrane element 1. It may be wound. Even in such a case, since the inner wall surface of the center tube 5 has a shape that allows insertion of a drive shaft having an outer shape capable of locking relative rotation, the inner wall surface of the center tube 5 is prevented from being damaged. be able to. The tape tension applied to the outer peripheral tape 20 is preferably in the range of 10 to 20 kgf / 75 mm (0.13 to 0.27 kgf / mm, 1.31 to 2.65 N / mm). FIGS. 4A to 4D show a case in which the outer peripheral tape 20 having a predetermined width is spirally wound toward the end in the axial direction, and then spirally wound toward the other end in the axial direction. An example of spiral winding toward the center of the direction is shown. That is, the outer peripheral tape 20 is spirally wound around each part of the membrane element 1 for two layers. The winding direction of the outer peripheral tape 20 is the same as the winding direction of the laminate in the membrane element 1.

図6(a)に示すように、外周テープ20の先端を膜エレメント1の巻回の開始位置に固定する。固定の方法は貼付、融着、接着などの方法で行うことができる。巻回の際には、外周テープ20の供給ロールをトラバースさせたり、膜エレメント1を軸方向又は供給ロール側に移動させたりすることで、外周テープ20をらせん状に巻回することができる。   As shown in FIG. 6A, the tip of the outer peripheral tape 20 is fixed at the winding start position of the membrane element 1. The fixing method can be performed by a method such as sticking, fusing, and adhesion. At the time of winding, the outer peripheral tape 20 can be wound spirally by traversing the supply roll of the outer peripheral tape 20 or moving the membrane element 1 in the axial direction or the supply roll side.

また、外周テープ20を巻回する際、らせん状のシート同士が重なって隙間が無い状態とするのが好ましい。具体的には外周テープ20の重なりをシート幅の5〜50%とするのが好ましい。この範囲を下回ると隙間が出来やすく、隙間が出来るとその部分は分離膜と供給側流路材と透過側流路材の密着性が低下し易い。また、この範囲を超えると外周テープ20の巻き付け時間と外周テープ20の使用量が増加し安価なスパイラル膜エレメントを供給しにくくなる。   Further, when the outer peripheral tape 20 is wound, it is preferable that the spiral sheets overlap with each other so that there is no gap. Specifically, the overlap of the outer peripheral tape 20 is preferably 5 to 50% of the sheet width. Below this range, a gap is likely to be formed, and when a gap is formed, the adhesion between the separation membrane, the supply-side channel material, and the permeate-side channel material tends to be reduced. If this range is exceeded, the winding time of the outer peripheral tape 20 and the amount of use of the outer peripheral tape 20 will increase, making it difficult to supply inexpensive spiral membrane elements.

本実施形態では、図6(b)に示すように、外周テープ20を一方の軸方向端部まで巻回すると、続いて他方の軸方向端部に向けてらせん状に外周テープ20を巻回する。その際、外周テープ20を一旦切断した後に、再度、一方の軸方向端部から巻回を開始してもよいが、外周テープ20を切断せずに連続して巻回を行うのが好ましい。巻回を連続して行う場合、徐々に巻回の角度(シート長手方向と軸方向のなす角度)を変えてもよく、一時に変えてもよい。また、このようなターン部分を、外周テープ20の巻回後にトリミングして除去することも可能である。   In the present embodiment, as shown in FIG. 6B, when the outer peripheral tape 20 is wound to one axial end, the outer peripheral tape 20 is then wound spirally toward the other axial end. To do. At that time, after the outer peripheral tape 20 is once cut, the winding may be started again from one end portion in the axial direction, but it is preferable that the outer peripheral tape 20 is continuously wound without being cut. When the winding is continuously performed, the winding angle (angle formed between the sheet longitudinal direction and the axial direction) may be gradually changed or may be changed at a time. Further, such a turn portion can be trimmed and removed after the outer peripheral tape 20 is wound.

本実施形態では、図6(c)〜(d)に示すように、外周テープ20を他方の軸方向端部まで巻回すると、続いて軸方向中央付近に向けてらせん状に外周テープ20を巻回する。この場合も上記と同様にしてターンを行うのが好ましい。本実施形態において、更に巻回の層数を増加させてもよい。   In this embodiment, as shown in FIGS. 6C to 6D, when the outer peripheral tape 20 is wound up to the other axial end, the outer peripheral tape 20 is then spiraled toward the vicinity of the axial center. Wind. Also in this case, it is preferable to perform the turn in the same manner as described above. In the present embodiment, the number of winding layers may be further increased.

本発明の実施の一形態に係るスパイラル型分離膜エレメントの構成例を示す説明図である。It is explanatory drawing which shows the structural example of the spiral-type separation membrane element which concerns on one Embodiment of this invention. 前記スパイラル型分離膜エレメントに於ける中心管の断面形状を示す模式図である。It is a schematic diagram which shows the cross-sectional shape of the center pipe | tube in the said spiral type separation membrane element. 前記スパイラル型分離膜エレメントに於ける他の中心管の断面形状を示す模式図である。It is a schematic diagram which shows the cross-sectional shape of the other center pipe | tube in the said spiral type separation membrane element. 前記スパイラル型分離膜エレメントに於ける他の中心管の断面形状を示す模式図である。It is a schematic diagram which shows the cross-sectional shape of the other center pipe | tube in the said spiral type separation membrane element. 前記スパイラル型分離膜エレメントに於ける他の中心管の断面形状を示す模式図である。It is a schematic diagram which shows the cross-sectional shape of the other center pipe | tube in the said spiral type separation membrane element. 前記スパイラル型分離膜エレメントに外周テープを巻き付ける工程を説明する為の模式図である。It is a schematic diagram for demonstrating the process of winding an outer periphery tape around the said spiral type separation membrane element.

符号の説明Explanation of symbols

1 スパイラル型分離膜エレメント
2 分離膜
3 透過側流路材
4 封筒状膜
5 中空状中心管
6 供給側流路材
7 原液
8 透過液
9 濃縮液
10〜15 内壁面
20 外周テープ
DESCRIPTION OF SYMBOLS 1 Spiral type separation membrane element 2 Separation membrane 3 Permeation side flow path material 4 Envelope-shaped membrane 5 Hollow center tube 6 Supply side flow path material 7 Stock solution 8 Permeate 9 Concentrate 10-15 Inner wall surface 20 Outer tape

Claims (3)

分離膜の間に供給側流路材を配置した分離膜ユニットと透過側流路材とを交互に重ねた積層体を、有孔の中空状中心管の周囲に巻回したスパイラル型分離膜エレメントに於いて、
前記中心管の外形はその断面において円形であり、
前記中心管の端部の内壁面はその断面において円形状を有し、それ以外の内壁面はその断面において楕円形状を有するものであり、相対回転を係止可能な楕円形状の外形を有する駆動シャフトの挿入を許容する形状であることを特徴とするスパイラル型分離膜エレメント。
Spiral type separation membrane element in which a laminated body in which a separation membrane unit and a permeation channel material are alternately stacked between the separation membranes is wound around a perforated hollow central tube In
The outer shape of the central tube is circular in cross section,
The inner wall surface at the end of the central tube has a circular shape in its cross section, and the other inner wall surface has an elliptical shape in its cross section, and has an elliptical outer shape capable of locking relative rotation. A spiral separation membrane element characterized by having a shape allowing insertion of a shaft.
分離膜の間に供給側流路材を配置した分離膜ユニットと透過側流路材とを交互に重ねた積層体を、有孔の中空状中心管の周囲に巻回する手段を備えたスパイラル型分離膜エレメントの製造装置に於いて、
前記中心管の内部に挿入して該中心管を回転させ、中心管の周囲に前記積層体を巻回させる為の駆動シャフトであって、
外形はその断面において円形であり、端部の内壁面はその断面において円形状を有し、それ以外の内壁面はその断面において楕円形状を有する前記中心管に対し、相対回転を係止可能な楕円形状の外形を有する駆動シャフト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の製造装置。
Spiral provided with means for winding a laminated body in which a separation membrane unit and a permeation channel material alternately arranged between separation membranes around a perforated hollow central tube In the manufacturing apparatus of the mold separation membrane element,
A drive shaft for inserting the inside of the central tube to rotate the central tube and winding the laminate around the central tube;
The outer shape is circular in the cross section, the inner wall surface of the end portion has a circular shape in the cross section, and the other inner wall surfaces can lock relative rotation with respect to the central tube having the elliptical shape in the cross section. An apparatus for manufacturing a spiral separation membrane element, comprising a drive shaft having an elliptical outer shape .
前記中心管に前記積層体を巻き付ける際に、該積層体の端部に張力を加える手段を備えることを特徴とする請求項に記載のスパイラル型分離膜エレメントの製造装置。 The apparatus for manufacturing a spiral separation membrane element according to claim 2 , further comprising means for applying tension to an end of the laminated body when the laminated body is wound around the central tube.
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JPH0618787Y2 (en) * 1989-11-29 1994-05-18 前田金属工業株式会社 Torque transmission member for screw tightening
JPH0742470A (en) * 1993-07-29 1995-02-10 Hitachi Constr Mach Co Ltd Adapter for mounting bucket
JPH081319Y2 (en) * 1991-06-05 1996-01-17 忠義 藤原 Electric cylinder
JPH10137558A (en) * 1996-11-11 1998-05-26 Nitto Denko Corp Spiral separation membrane element and its production
JP2002143653A (en) * 2000-11-14 2002-05-21 Toray Ind Inc Manufacturing device of separation membrane element
JP2003010650A (en) * 2001-06-29 2003-01-14 Toray Ind Inc Method and apparatus for producing fluid separation membrane element

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0618787Y2 (en) * 1989-11-29 1994-05-18 前田金属工業株式会社 Torque transmission member for screw tightening
JPH081319Y2 (en) * 1991-06-05 1996-01-17 忠義 藤原 Electric cylinder
JPH0742470A (en) * 1993-07-29 1995-02-10 Hitachi Constr Mach Co Ltd Adapter for mounting bucket
JPH10137558A (en) * 1996-11-11 1998-05-26 Nitto Denko Corp Spiral separation membrane element and its production
JP2002143653A (en) * 2000-11-14 2002-05-21 Toray Ind Inc Manufacturing device of separation membrane element
JP2003010650A (en) * 2001-06-29 2003-01-14 Toray Ind Inc Method and apparatus for producing fluid separation membrane element

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