WO2014141967A1 - Separating membrane element - Google Patents

Separating membrane element Download PDF

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Publication number
WO2014141967A1
WO2014141967A1 PCT/JP2014/055634 JP2014055634W WO2014141967A1 WO 2014141967 A1 WO2014141967 A1 WO 2014141967A1 JP 2014055634 W JP2014055634 W JP 2014055634W WO 2014141967 A1 WO2014141967 A1 WO 2014141967A1
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Prior art keywords
annular portion
separation membrane
membrane element
prevention plate
upstream
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PCT/JP2014/055634
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French (fr)
Japanese (ja)
Inventor
正彬 竹中
智正 片山
朗 片山
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東レ株式会社
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Priority to JP2014517319A priority Critical patent/JPWO2014141967A1/en
Publication of WO2014141967A1 publication Critical patent/WO2014141967A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/10Spiral-wound membrane modules
    • B01D63/12Spiral-wound membrane modules comprising multiple spiral-wound assemblies
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/10Spiral-wound membrane modules
    • B01D63/106Anti-Telescopic-Devices [ATD]

Definitions

  • the present invention relates to a separation membrane element using a reverse osmosis membrane.
  • Separation membranes as water treatment means in seawater desalination and ultrapure water production applications in the semiconductor field, and in various water treatment applications including general brine desalination, organic matter separation, wastewater reuse, etc.
  • the fluid separation process using the is used.
  • a typical separation membrane includes a reverse osmosis membrane. In this separation process using a membrane, a separation membrane element using a reverse osmosis membrane is used, and its use is rapidly increasing.
  • the separation membrane element has a structure in which a separation membrane is spirally wound around a collecting pipe together with a permeate channel material and a raw solution channel material.
  • the separation membrane element 1 includes a permeate passage material 5 sandwiched between envelope-like membranes formed by adhering three sides of the separation membrane 4, and this is connected to the stock solution passage material 6.
  • One or a plurality of membrane units 7 are prepared and wound around a liquid collecting tube 3 having a liquid collecting hole 2 in a spiral shape.
  • the envelope-like membrane is open on the liquid collection tube 3 side.
  • the stock solution 20 is supplied from one end face of the separation membrane element 1 and processed by the separation membrane 4.
  • the permeate 21 that has permeated through the separation membrane 4 is taken out from the collecting tube 3, and the stock solution 20 that has not permeated through the separation membrane 4 is discharged from the other end face of the separation membrane element 1 as a concentrate.
  • the separation membrane element 1 is provided with telescope prevention plates 10 provided with a stock solution flow path 11 for supplying the stock solution 20 to the end surface of the separation membrane element at both ends in the longitudinal direction. It takes the form covered by.
  • a plurality of separation membrane elements are arranged in series in the longitudinal direction in a pressure vessel and used as a separation membrane module. It is necessary to flow the required amount of liquid over the separation membrane surface in order to effectively exhibit the separation performance by the separation membrane and prevent the separation membrane surface from being contaminated. For this reason, 4 to 8 separations are required.
  • the membrane elements are housed in series in a pressure vessel. Separation membrane elements arranged in series are closely connected to the telescope prevention plate at the end of the separation membrane element and the telescope prevention plate of the adjacent separation membrane element, and the collecting pipe is connected by a connector. Connected by.
  • the telescope prevention plate is provided at each end of the separation membrane element in order to prevent the phenomenon that the membrane unit inside the separation membrane element is deformed by the stock solution flowing into the separation membrane element at a high pressure.
  • an inner peripheral annular portion that engages with a liquid collecting tube, an outer peripheral annular portion having a diameter substantially equal to the diameter of the separation membrane element, and these annular portions are arranged in a substantially radial direction, that is,
  • a spoke-type telescope prevention plate having a spoke portion connected in the same direction as the radius of the ring Patent Document 1
  • a plate punched with a round hole or a combination of a spoke and a round hole punching plate
  • a round hole punching type telescope prevention plate is used.
  • the telescope prevention plate generally has an extrapolated seal ring 12 made of rubber having a U-shaped or V-shaped cross section and locks both end faces thereof. It has a structure that can be done.
  • the seal ring 12 expands to the outside due to the pressure at the time of fluid separation, and seals the gap with the inner surface of the pressure vessel 13 so that the entire amount of the stock solution supplied at the time of fluid separation flows into the separation membrane element.
  • the telescope prevention plate is generally provided with the same shape at both the upstream and downstream ends of the separation membrane element, as shown in FIG. It is only necessary to provide the upstream side in view of the required function. Since the seal ring is not extrapolated to the downstream telescope prevention plate, this portion is an extra space.
  • the present invention provides a telescope prevention plate capable of increasing the film area while maintaining the function of the telescope prevention plate by reducing the excess space of the conventional telescope prevention plate, and separation using the same
  • An object is to provide a membrane element.
  • the separation membrane element of the present invention for achieving the above object has the following characteristics.
  • An exterior body is provided on the outer periphery of a spiral wound body in which a separation membrane, a raw liquid flow path material, and a permeate flow path material are wound in a spiral shape, and at both ends of the spiral wound body and the exterior body, respectively.
  • a separation membrane element having a structure in which an upstream telescope prevention plate and a downstream telescope prevention plate are arranged, and used by being loaded in series in a pressure vessel, wherein the upstream telescope prevention plate Are formed on the upstream side of the first annular portion and the first annular portion on which the exterior body is extrapolated, and on the downstream side and the upstream side of the upstream side of the exterior body and on the downstream side of the seal ring, respectively.
  • the seal The upstream end face of the groove includes a fourth annular portion that can be locked, and the downstream telescope prevention plate is provided on the downstream side of the fifth annular portion and the fifth annular portion on which the exterior body is extrapolated.
  • a separation membrane element comprising a sixth annular portion formed and capable of locking the downstream end portion of the outer package to the upstream end surface.
  • the width of the downstream telescope prevention plate in the separation membrane element axial direction is 15% to 60% of the width of the upstream telescope prevention plate in the separation membrane element axial direction, The separation membrane element according to (1).
  • FIG. 1 is a partially exploded perspective view according to an embodiment of the separation membrane element of the present invention.
  • FIG. 2 is a longitudinal sectional view of an embodiment in which the separation membrane element of the present invention is loaded in a pressure vessel.
  • 3A and 3B are examples of the telescope prevention plate constituting the separation membrane element of the present invention.
  • FIG. 3A is a longitudinal sectional view showing the upstream telescope prevention plate and
  • FIG. 3B is the downstream telescope prevention plate.
  • 4A and 4B are longitudinal sectional views corresponding to FIGS. 3A and 3B showing another example of the telescope prevention plate.
  • FIG. 5 is a longitudinal sectional view when a conventional separation membrane element is loaded in a pressure vessel.
  • FIG. 2 shows an embodiment according to the separation membrane element of the present invention.
  • this separation membrane element a spiral wound body in which a membrane unit 7 including a separation membrane, a permeate flow path material, and a raw liquid flow path material is spirally wound around a liquid collection tube 3 having a liquid collection hole.
  • An exterior body 8 is formed outside the membrane unit 7 to form the separation membrane element 1.
  • the end face of the separation membrane element 1 is exposed, and the upstream telescope prevention plate 10a and the downstream telescope prevention plate 10b are attached to both ends thereof.
  • the upstream telescope prevention plate 10a and the downstream telescope prevention plate 10b serve to prevent the separation membrane element 1 from being deformed into a telescope shape.
  • the stock solution 20 enters the membrane unit 7 through the stock solution flow path of the upstream telescope prevention plate 10 a, is subjected to membrane separation, and is collected in the liquid collection tube 3 as a permeate 21.
  • the stock solution 20 that has not passed through the separation membrane is discharged from the stock solution flow path of the downstream telescope prevention plate 10b.
  • a plurality of separation membrane elements 1 configured as described above are accommodated in series in the pressure vessel 13.
  • a seal ring 12 is extrapolated to the upstream telescope prevention plate 10 a so that the stock solution 20 enters the membrane unit 7, and seals between the inner wall surface of the pressure vessel 13.
  • the liquid collecting pipes 3 of the separation membrane elements 1 adjacent to each other are integrally connected via connecting pipes inserted into both the liquid collecting pipes 3.
  • the upstream telescope prevention plate 10 a includes a first annular portion 14, a second annular portion 15, a third annular portion 16, and a fourth annular portion 17.
  • the first annular portion 14 is connected to the upstream side of the spiral wound body of the membrane unit 7 with the exterior body 8 being extrapolated.
  • the second annular portion 15 is formed on the upstream side of the first annular portion 14, and enables the upstream end portion of the outer package 8 and the downstream end surface of the seal ring to be locked to the downstream and upstream end surfaces, respectively.
  • the third annular portion 16 is formed on the upstream side of the second annular portion 15, and the seal ring 12 is extrapolated.
  • the fourth annular portion 17 is formed on the upstream side of the third annular portion 16 and enables the upstream end surface of the seal ring 12 to be locked to the downstream end surface.
  • the downstream telescope prevention plate 10 b includes a fifth annular portion 18 and a sixth annular portion 19.
  • the fifth annular portion 18 is connected to the upstream side of the spiral wound body of the membrane unit 7 with the exterior body 8 being extrapolated.
  • the sixth annular portion 19 is formed on the downstream side of the fifth annular portion 18 and enables the downstream end portion of the exterior body 8 to be locked to the upstream end surface.
  • the width of the downstream telescope prevention plate 10b in the separation membrane element axial direction is 60% or less from the point of increase in the membrane area with respect to the width of the upstream telescope prevention plate 10a in the separation membrane element axial direction, and From the viewpoint of securing strength, it is preferably 15% or more. If the width of the downstream telescope prevention plate 10b in the axial direction of the separation membrane element is too small, the strength may be insufficient and the high pressure during operation may not be able to be endured.
  • the outer diameters of the fourth annular portion 17 and the sixth annular portion 19 are constant in the axial direction of the separation membrane element.
  • the fourth annular portion 17 and the sixth annular portion 19 have the same shape, that is, the same outer diameter and the same width in the axial direction of the separation membrane element. From the viewpoint of symmetry, it is more preferable.
  • grooves or protrusions on the outer peripheral surface are provided in a direction parallel to the element axial direction, or in the third annular portion 16, the outer peripheral surface and the inner peripheral surface are formed.
  • the fifth annular portion 18 has an upstream end having an outer diameter larger than that of the downstream end, or a groove or protrusion 23 on the outer periphery as shown in FIG. 4B. It is preferable from the viewpoint of firmly engaging the exterior body and preventing separation of the downstream telescope prevention plate 10b from the exterior body. Moreover, since it is the same also about the upstream telescope prevention plate 10a, it is more preferable that the 1st annular part 14 is the same shape as the 5th annular part 18 and plane symmetry. That is, the first annular portion 14 has the outer diameter of the downstream end portion larger than the outer diameter of the upstream end portion as shown in FIG. 3A, or has a groove or protrusion 23 on the outer periphery as shown in FIG. 4A. Is preferred.
  • the material for the upstream telescope prevention plate and the downstream telescope prevention plate is not particularly limited, but from the viewpoint of productivity, cost, and weight reduction, and also consider chemical resistance against various substances contained in the stock solution. And at least one selected from the group consisting of acrylonitrile butadiene styrene copolymer resin (ABS), vinyl chloride resin (PVC), modified polyphenylene oxide resin (PPO), modified polyphenylene ether resin (PPE), and polyoxymethylene resin (POM). It is preferable that Further, at least one selected from this group may be used as the glass fiber reinforced resin (GFRP).
  • ABS acrylonitrile butadiene styrene copolymer resin
  • PVC vinyl chloride resin
  • PPO modified polyphenylene oxide resin
  • PPE modified polyphenylene ether resin
  • POM polyoxymethylene resin
  • GFRP glass fiber reinforced resin
  • the high modulus fiber include, but are not limited to, glass fiber, carbon fiber, aramid fiber, and metal fiber.
  • the material of the resin is not particularly limited, and examples thereof include, but are not limited to, an epoxy resin, a polyester resin, a polyamide resin, a phenol resin, and a methyl methacrylate resin.
  • the high elastic modulus fiber and the resin forming the exterior body have a water absorption rate of 3% or less in terms of a weight change rate when immersed in 90 ° C. warm water for 24 hours.
  • the exterior body is preferably transparent so that a label attached to the outer peripheral surface of the membrane unit can be visually recognized in order to identify the product name, lot number, etc. of the separation membrane element.
  • the high modulus fiber impregnated in the resin is removed from one end (the first annular portion 14 of the upstream telescope prevention plate 10a) of one telescope prevention plate on the membrane unit surrounding side.
  • the outer periphery of the other telescope prevention plate is wound to one end (the fifth annular portion 18 of the downstream telescope prevention plate 10b) of the other telescope prevention plate on the side of the membrane unit surrounding body and thermally cured.
  • the fibers are arranged in the direction of the collecting tube axis between the end of the telescope prevention plate and the end of the membrane unit.
  • the thickness of the exterior body in the portion that engages with one end of the telescope prevention plate on the side of the membrane unit enclosure is made thicker than the thickness of the exterior body in the axial center portion of the membrane unit enclosure. Is preferred.
  • the thickness of the exterior body is reduced to prevent stress concentration in the exterior body. It is preferable that the thickness of the protective plate is gradually reduced from the portion engaging the one end of the membrane unit envelope on the side of the membrane unit envelope to the central portion in the axial direction of the membrane unit envelope.
  • the U-shaped or V-shaped cross section is preferable because it expands outward due to the pressure during fluid separation and seals the gap with the inner surface of the pressure vessel.
  • the material is not particularly limited, and for example, ethylene propylene rubber (EPM, EPDM), nitrile rubber (NBR), or silicon rubber is selected.
  • the separation membrane element of the present invention it is possible to increase the membrane area while maintaining the function of the telescope prevention plate. That is, since the downstream telescope prevention plate is reduced by the axial width corresponding to the portion necessary for extrapolating the seal ring in the upstream telescope prevention plate, the membrane area can be increased.
  • each annular portion in the axial direction of the separation membrane element is defined as the first annular portion 7.2 mm, the second annular portion 4.0 mm, the third annular portion 8.8 mm, and the fourth annular portion 4. 5 mm, 24.5 mm in total, and the downstream telescope prevention plate is the same as the upstream telescope prevention plate, and the length in the element axial direction is 964 mm as shown in FIG.
  • the effective membrane area of the separation membrane elements was about 440 square feet.
  • each annular portion in the axial direction of the separation membrane element is defined as the first annular portion 7.2 mm, the second annular portion 4.0 mm, the third annular portion 8.8 mm, and the fourth annular portion 4. 0.5 mm and 24.5 mm overall.
  • the width of each annular portion in the separation membrane element axial direction was set to a fifth annular portion 7.2 mm, a sixth annular portion 4.0 mm, and a total of 11.2 mm. In this case, the width of the downstream telescope prevention plate in the element axial direction is 46% of that of the upstream telescope prevention plate.
  • the effective membrane of the separation membrane element was obtained.
  • the area was about 446 square feet. That is, compared to the 8-inch separation membrane element produced in Comparative Example 1, the effective membrane area increased by about 1.4%.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

Provided is a separating membrane element using anti-telescoping plates, which maintain the function of anti-telescoping plates while making it possible to increase the membrane area. The separation membrane element has an upstream anti-telescoping plate (10a) and a downstream anti-telescoping plate (10b). The upstream anti-telescoping plate (10a) is obtained from: a first ring-shaped section (14) on the outside of which a sheath (8) is fitted; a second ring-shaped section (15), the downstream and upstream endfaces of which can engage with the upstream end of the sheath (8) and the downstream end of a seal ring (12) respectively; a third ring-shaped section (16) on the outside of which the seal ring (12) is fitted; and a fourth ring-shaped section (17), the downstream endface of which can engage with the upstream endface of the seal ring (12). The downstream anti-telescoping plate (10b) is obtained from a fifth ring-shaped section (18) on the outside of which the sheath (8) is fitted, and a sixth ring-shaped section (19), the upstream endface of which can engage with the downstream end of the sheath (8).

Description

分離膜エレメントSeparation membrane element
 本発明は、逆浸透膜を用いた分離膜エレメントに関するものである。 The present invention relates to a separation membrane element using a reverse osmosis membrane.
 海水淡水化や、半導体分野における超純水製造の用途において、さらには、一般かん水淡水化用途や、有機物分離、廃水再利用などをはじめとする種々の水処理用途において、水処理手段として分離膜を用いた流体分離処理が利用されている。代表的な分離膜としては逆浸透膜が挙げられる。この膜による分離処理では、逆浸透膜を用いた分離膜エレメントが使用され、その使用が急速に増加してきている。 Separation membranes as water treatment means in seawater desalination and ultrapure water production applications in the semiconductor field, and in various water treatment applications including general brine desalination, organic matter separation, wastewater reuse, etc. The fluid separation process using the is used. A typical separation membrane includes a reverse osmosis membrane. In this separation process using a membrane, a separation membrane element using a reverse osmosis membrane is used, and its use is rapidly increasing.
 分離膜エレメントは、分離膜が透過液流路材と原液流路材と共に集液管の周りにスパイラル状に巻きつけられた構造をとる。図1に示すように、分離膜エレメント1は、分離膜4の3辺を接着して形成した封筒状膜の間に透過液流路材5を挟み込み、これと原液流路材6とを1つの膜ユニット7として、単数もしくは複数用意し、集液孔2を有する集液管3の周囲にスパイラル状に巻きつけてなる。封筒状膜は集液管3側で開口している。原液20は分離膜エレメント1の一方の端面から供給され、分離膜4で処理される。分離膜4を透過した透過液21は集液管3から取り出され、分離膜4を透過しなかった原液20は、分離膜エレメント1の他方の端面から濃縮液として排出される。 The separation membrane element has a structure in which a separation membrane is spirally wound around a collecting pipe together with a permeate channel material and a raw solution channel material. As shown in FIG. 1, the separation membrane element 1 includes a permeate passage material 5 sandwiched between envelope-like membranes formed by adhering three sides of the separation membrane 4, and this is connected to the stock solution passage material 6. One or a plurality of membrane units 7 are prepared and wound around a liquid collecting tube 3 having a liquid collecting hole 2 in a spiral shape. The envelope-like membrane is open on the liquid collection tube 3 side. The stock solution 20 is supplied from one end face of the separation membrane element 1 and processed by the separation membrane 4. The permeate 21 that has permeated through the separation membrane 4 is taken out from the collecting tube 3, and the stock solution 20 that has not permeated through the separation membrane 4 is discharged from the other end face of the separation membrane element 1 as a concentrate.
 通常、分離膜エレメント1は長手方向の両端部に、原液20を分離膜エレメントに端面に供給するための原液流路11を設けたテレスコープ防止板10が取り付けられ、さらに外周面を外装体8により覆われた形態をとる。 Usually, the separation membrane element 1 is provided with telescope prevention plates 10 provided with a stock solution flow path 11 for supplying the stock solution 20 to the end surface of the separation membrane element at both ends in the longitudinal direction. It takes the form covered by.
 分離膜エレメントを用いて実際に流体分離を行う際には、複数本の分離膜エレメントを、圧力容器内に長手方向に直列に配列して装填することにより分離膜モジュールとして使用される。分離膜による分離性能を効果的に発揮し、かつ分離膜面の汚れを防止するために必要な液量を分離膜面上に流すことが必要であり、このために、4~8本の分離膜エレメントを圧力容器内に直列に収容して使用されることが多い。直列に配列して装填された分離膜エレメントは、分離膜エレメントの端部のテレスコープ防止板と隣接する分離膜エレメントのテレスコープ防止板とを密接させ、かつ、集液管をコネクタによって繋ぐことによって接続されている。 When fluid separation is actually performed using a separation membrane element, a plurality of separation membrane elements are arranged in series in the longitudinal direction in a pressure vessel and used as a separation membrane module. It is necessary to flow the required amount of liquid over the separation membrane surface in order to effectively exhibit the separation performance by the separation membrane and prevent the separation membrane surface from being contaminated. For this reason, 4 to 8 separations are required. In many cases, the membrane elements are housed in series in a pressure vessel. Separation membrane elements arranged in series are closely connected to the telescope prevention plate at the end of the separation membrane element and the telescope prevention plate of the adjacent separation membrane element, and the collecting pipe is connected by a connector. Connected by.
 テレスコープ防止板は、分離膜エレメントに高圧で流入する原液によって分離膜エレメント内部の膜ユニットが型崩れする現象を防止するために分離膜エレメントの両端部にそれぞれ設けるものである。一般的に、図1に示すように、集液管と係合する内周環状部と、分離膜エレメントの直径とほぼ同等の直径を有する外周環状部と、これら環状部同士を略放射状方向すなわち環の半径と概ね同じ方向に連結するスポーク部を有するスポーク型のテレスコープ防止板や(特許文献1)、または、丸孔をパンチングした板、あるいはスポークと丸孔パンチング板とを組み合わせて構成される丸孔パンチング型のテレスコープ防止板(特許文献2)が用いられている。 The telescope prevention plate is provided at each end of the separation membrane element in order to prevent the phenomenon that the membrane unit inside the separation membrane element is deformed by the stock solution flowing into the separation membrane element at a high pressure. In general, as shown in FIG. 1, an inner peripheral annular portion that engages with a liquid collecting tube, an outer peripheral annular portion having a diameter substantially equal to the diameter of the separation membrane element, and these annular portions are arranged in a substantially radial direction, that is, A spoke-type telescope prevention plate having a spoke portion connected in the same direction as the radius of the ring (Patent Document 1), a plate punched with a round hole, or a combination of a spoke and a round hole punching plate A round hole punching type telescope prevention plate (Patent Document 2) is used.
 また、テレスコープ防止板は、一般的に、図5に示すように、断面がU字型やV字型の形状のゴム等で作製されたシールリング12を外挿し、その両端面を係止できる構造となっている。シールリング12は流体分離時の圧力によって外側に拡がり、圧力容器13の内面との隙間を封止することで、流体分離時に供給する原液の全量を分離膜エレメントに流入させる。 In addition, as shown in FIG. 5, the telescope prevention plate generally has an extrapolated seal ring 12 made of rubber having a U-shaped or V-shaped cross section and locks both end faces thereof. It has a structure that can be done. The seal ring 12 expands to the outside due to the pressure at the time of fluid separation, and seals the gap with the inner surface of the pressure vessel 13 so that the entire amount of the stock solution supplied at the time of fluid separation flows into the separation membrane element.
日本国特開平11-267470号公報Japanese Patent Laid-Open No. 11-267470 日本国特開2005-111473号報Japanese Laid-Open Patent Publication No. 2005-111473
 ところで、分離膜エレメントに求められている課題の一つに膜面積の増加が挙げられる。しかし、圧力容器の内径や長さの寸法は規格化されているため、分離膜エレメントの外径や長さの寸法にも制限がある。 Incidentally, an increase in membrane area is one of the issues required for the separation membrane element. However, since the inner diameter and length of the pressure vessel are standardized, the outer diameter and length of the separation membrane element are also limited.
 一方、テレスコープ防止板は、一般的に、図5に示すように、分離膜エレメントの上流側と下流側の両端で同一形状のものを設けているが、これに外挿するシールリングは、その要求機能から上流側のみに設ければよく、下流側のテレスコープ防止板にはシールリングを外挿しないため、この部分が余剰スペースになっている。 On the other hand, the telescope prevention plate is generally provided with the same shape at both the upstream and downstream ends of the separation membrane element, as shown in FIG. It is only necessary to provide the upstream side in view of the required function. Since the seal ring is not extrapolated to the downstream telescope prevention plate, this portion is an extra space.
 そこで、本発明は、従来のテレスコープ防止板の余剰スペースを削減することにより、テレスコープ防止板の機能を維持しつつ膜面積の増加を可能とするテレスコープ防止板、およびこれを用いた分離膜エレメントを提供することを目的とする。 Accordingly, the present invention provides a telescope prevention plate capable of increasing the film area while maintaining the function of the telescope prevention plate by reducing the excess space of the conventional telescope prevention plate, and separation using the same An object is to provide a membrane element.
 前記目的を達成するための本発明の分離膜エレメントは、次の特徴を備えるものである。 The separation membrane element of the present invention for achieving the above object has the following characteristics.
 (1)分離膜、原液流路材および透過液流路材がスパイラル状に巻回されてなるスパイラル巻体の外周に外装体が設けられるとともに前記スパイラル巻体および前記外装体の両端部にそれぞれ上流側テレスコープ防止板および下流側テレスコープ防止板が配設された構造を有し、圧力容器内に直列に複数装填して使用される分離膜エレメントであって、前記上流側テレスコープ防止板は、前記外装体が外挿される第1環状部と、前記第1環状部の上流側に形成され、下流側および上流側の端面にそれぞれ前記外装体の上流側端部およびシールリングの下流側端面を係止可能な第2環状部と、前記第2環状部の上流側に形成され、前記シールリングが外挿される第3環状部と、前記第3環状部の上流側に形成され、下流側端面に前記シールリングの上流側端面が係止可能な第4環状部からなり、さらに、前記下流側テレスコープ防止板は、前記外装体が外挿される第5環状部と、前記第5環状部の下流側に形成され、上流側端面に前記外装体の下流側端部を係止可能な第6環状部からなることを特徴とする分離膜エレメント。 (1) An exterior body is provided on the outer periphery of a spiral wound body in which a separation membrane, a raw liquid flow path material, and a permeate flow path material are wound in a spiral shape, and at both ends of the spiral wound body and the exterior body, respectively. A separation membrane element having a structure in which an upstream telescope prevention plate and a downstream telescope prevention plate are arranged, and used by being loaded in series in a pressure vessel, wherein the upstream telescope prevention plate Are formed on the upstream side of the first annular portion and the first annular portion on which the exterior body is extrapolated, and on the downstream side and the upstream side of the upstream side of the exterior body and on the downstream side of the seal ring, respectively. A second annular portion that can lock the end surface; a third annular portion that is formed on the upstream side of the second annular portion; the seal ring is extrapolated; and an upstream side of the third annular portion; The seal The upstream end face of the groove includes a fourth annular portion that can be locked, and the downstream telescope prevention plate is provided on the downstream side of the fifth annular portion and the fifth annular portion on which the exterior body is extrapolated. A separation membrane element comprising a sixth annular portion formed and capable of locking the downstream end portion of the outer package to the upstream end surface.
 (2)前記下流側テレスコープ防止板の分離膜エレメント軸方向の幅が、前記上流側テレスコープ防止板の分離膜エレメント軸方向の幅の15%以上60%以下であることを特徴とする、前記(1)に記載の分離膜エレメント。 (2) The width of the downstream telescope prevention plate in the separation membrane element axial direction is 15% to 60% of the width of the upstream telescope prevention plate in the separation membrane element axial direction, The separation membrane element according to (1).
 (3)前記第4環状部および前記第6環状部の外径が、分離膜エレメント軸方向について一定であることを特徴とする、前記(1)または前記(2)に記載の分離膜エレメント。 (3) The separation membrane element according to (1) or (2) above, wherein outer diameters of the fourth annular portion and the sixth annular portion are constant in the axial direction of the separation membrane element.
 (4)前記第5環状部において、上流側端部の外径が下流側端部の外径より大きいことを特徴とする、前記(1)~(3)のいずれかに記載の分離膜エレメント。 (4) The separation membrane element according to any one of (1) to (3), wherein the outer diameter of the upstream end is larger than the outer diameter of the downstream end in the fifth annular portion. .
 (5)前記第5環状部が、外周に溝または突起を有することを特徴とする、前記(1)~(4)のいずれかに記載の分離膜エレメント。 (5) The separation membrane element according to any one of (1) to (4), wherein the fifth annular portion has a groove or a protrusion on an outer periphery.
 (6)前記第1環状部が、前記第5環状部と同一形状であることを特徴とする、前記(1)~(5)のいずれかに記載の分離膜エレメント。 (6) The separation membrane element according to any one of (1) to (5), wherein the first annular portion has the same shape as the fifth annular portion.
 本発明によれば、テレスコープ防止板の機能を維持しつつ膜面積の増加を可能とする分離膜エレメントを提供することができる。 According to the present invention, it is possible to provide a separation membrane element that can increase the membrane area while maintaining the function of the telescope prevention plate.
図1は、本発明の分離膜エレメントの一実施態様に係る部分分解斜視図である。FIG. 1 is a partially exploded perspective view according to an embodiment of the separation membrane element of the present invention. 図2は、本発明の分離膜エレメントを圧力容器に装填した一実施態様の縦断面図である。FIG. 2 is a longitudinal sectional view of an embodiment in which the separation membrane element of the present invention is loaded in a pressure vessel. 図3A,3Bは、本発明の分離膜エレメントを構成するテレスコープ防止板の一例であり、図3Aは上流側テレスコープ防止板、図3Bは下流側テレスコープ防止板を示す縦断面図である。3A and 3B are examples of the telescope prevention plate constituting the separation membrane element of the present invention. FIG. 3A is a longitudinal sectional view showing the upstream telescope prevention plate and FIG. 3B is the downstream telescope prevention plate. . 図4A,4Bは、テレスコープ防止板の別の例を示す図3A,3Bに相当する縦断面図である。4A and 4B are longitudinal sectional views corresponding to FIGS. 3A and 3B showing another example of the telescope prevention plate. 図5は、従来の分離膜エレメントを圧力容器に装填した場合の縦断面図である。FIG. 5 is a longitudinal sectional view when a conventional separation membrane element is loaded in a pressure vessel.
 以下、本発明について、最良の実施形態を模式的に示す図面を参照しながら説明する。ただし、本発明の範囲がこれらに限られるものではない。 Hereinafter, the present invention will be described with reference to the drawings schematically showing the best embodiment. However, the scope of the present invention is not limited to these.
 図2に本発明の分離膜エレメントに係る一実施態様を示す。この分離膜エレメント1において、集液孔を有する集液管3の周りに、分離膜と透過液流路材と原液流路材とを含む膜ユニット7がスパイラル状に巻囲されたスパイラル巻体を形成する。その膜ユニット7の外側に外装体8が形成されて分離膜エレメント1が構成されている。この分離膜エレメント1の端面が露出され、その両端部に、上流側テレスコープ防止板10aおよび下流側テレスコープ防止板10bが装着される。上流側テレスコープ防止板10aおよび下流側テレスコープ防止板10bは、分離膜エレメント1がテレスコープ状に変形することを防止する役割を果たす。原液20は上流側テレスコープ防止板10aの原液流路を通って膜ユニット7に進入し、膜分離され、透過液21として集液管3に集められる。分離膜を透過しなかった原液20は、下流側テレスコープ防止板10bの原液流路から排出される。 FIG. 2 shows an embodiment according to the separation membrane element of the present invention. In this separation membrane element 1, a spiral wound body in which a membrane unit 7 including a separation membrane, a permeate flow path material, and a raw liquid flow path material is spirally wound around a liquid collection tube 3 having a liquid collection hole. Form. An exterior body 8 is formed outside the membrane unit 7 to form the separation membrane element 1. The end face of the separation membrane element 1 is exposed, and the upstream telescope prevention plate 10a and the downstream telescope prevention plate 10b are attached to both ends thereof. The upstream telescope prevention plate 10a and the downstream telescope prevention plate 10b serve to prevent the separation membrane element 1 from being deformed into a telescope shape. The stock solution 20 enters the membrane unit 7 through the stock solution flow path of the upstream telescope prevention plate 10 a, is subjected to membrane separation, and is collected in the liquid collection tube 3 as a permeate 21. The stock solution 20 that has not passed through the separation membrane is discharged from the stock solution flow path of the downstream telescope prevention plate 10b.
 上記のように構成された分離膜エレメント1が、圧力容器13内に複数個直列に収容される。各々の分離膜エレメント1では、原液20が膜ユニット7に進入するように、上流側テレスコープ防止板10aにシールリング12が外挿され、圧力容器13の内壁面との間をシールしている。また、互いに隣接する分離膜エレメント1の集液管3は、両方の集液管3に内挿される接続管を介して一体的に接続される。 A plurality of separation membrane elements 1 configured as described above are accommodated in series in the pressure vessel 13. In each separation membrane element 1, a seal ring 12 is extrapolated to the upstream telescope prevention plate 10 a so that the stock solution 20 enters the membrane unit 7, and seals between the inner wall surface of the pressure vessel 13. . Further, the liquid collecting pipes 3 of the separation membrane elements 1 adjacent to each other are integrally connected via connecting pipes inserted into both the liquid collecting pipes 3.
 図3Aおよび図3Bに、本発明の上流側テレスコープ防止板および下流側テレスコープ防止板の一例をそれぞれ示す。上流側テレスコープ防止板10aは、第1環状部14、第2環状部15、第3環状部16および第4環状部17からなる。第1環状部14は、外装体8が外挿され膜ユニット7のスパイラル巻体の上流側と接続する。第2環状部15は、第1環状部14の上流側に形成され、下流側および上流側の端面にそれぞれ外装体8の上流側端部およびシールリングの下流側端面を係止可能にする。第3環状部16は、第2環状部15の上流側に形成され、シールリング12が外挿される。第4環状部17は、第3環状部16の上流側に形成され、下流側端面にシールリング12の上流側端面を係止可能にする。さらに、下流側テレスコープ防止板10bは、第5環状部18と第6環状部19からなる。第5環状部18は、外装体8が外挿され膜ユニット7のスパイラル巻体の上流側と接続する。第6環状部19は、第5環状部18の下流側に形成され、上流側端面に外装体8の下流側端部を係止可能にする。 3A and 3B show examples of the upstream telescope prevention plate and the downstream telescope prevention plate of the present invention, respectively. The upstream telescope prevention plate 10 a includes a first annular portion 14, a second annular portion 15, a third annular portion 16, and a fourth annular portion 17. The first annular portion 14 is connected to the upstream side of the spiral wound body of the membrane unit 7 with the exterior body 8 being extrapolated. The second annular portion 15 is formed on the upstream side of the first annular portion 14, and enables the upstream end portion of the outer package 8 and the downstream end surface of the seal ring to be locked to the downstream and upstream end surfaces, respectively. The third annular portion 16 is formed on the upstream side of the second annular portion 15, and the seal ring 12 is extrapolated. The fourth annular portion 17 is formed on the upstream side of the third annular portion 16 and enables the upstream end surface of the seal ring 12 to be locked to the downstream end surface. Further, the downstream telescope prevention plate 10 b includes a fifth annular portion 18 and a sixth annular portion 19. The fifth annular portion 18 is connected to the upstream side of the spiral wound body of the membrane unit 7 with the exterior body 8 being extrapolated. The sixth annular portion 19 is formed on the downstream side of the fifth annular portion 18 and enables the downstream end portion of the exterior body 8 to be locked to the upstream end surface.
 ここで、下流側テレスコープ防止板10bの分離膜エレメント軸方向の幅が、上流側テレスコープ防止板10aの分離膜エレメント軸方向の幅に対し、膜面積の増加の点から60%以下、かつ、強度の確保の点から15%以上であることが好ましい。下流側テレスコープ防止板10bの分離膜エレメント軸方向の幅が小さ過ぎると、強度が不足し、運転時の高圧に耐えられないおそれがある。 Here, the width of the downstream telescope prevention plate 10b in the separation membrane element axial direction is 60% or less from the point of increase in the membrane area with respect to the width of the upstream telescope prevention plate 10a in the separation membrane element axial direction, and From the viewpoint of securing strength, it is preferably 15% or more. If the width of the downstream telescope prevention plate 10b in the axial direction of the separation membrane element is too small, the strength may be insufficient and the high pressure during operation may not be able to be endured.
 また、第4環状部17および第6環状部19の外径が、分離膜エレメント軸方向で一定であることが好ましい。特に、第4環状部17と第6環状部19で同一形状、すなわち同一の外径および同一の分離膜エレメント軸方向の幅であることが、外装体8との保持に関する上流側と下流側の対称性の観点から、より好ましい。 Further, it is preferable that the outer diameters of the fourth annular portion 17 and the sixth annular portion 19 are constant in the axial direction of the separation membrane element. In particular, the fourth annular portion 17 and the sixth annular portion 19 have the same shape, that is, the same outer diameter and the same width in the axial direction of the separation membrane element. From the viewpoint of symmetry, it is more preferable.
 また、第4環状部17および第6環状部19において、エレメント軸方向に平行な方向に外周面上の溝もしくは突起を設けるか、もしくは第3環状部16において、外周面と内周面とを貫通する孔を設けることで、テレスコープ防止板の各環状部の外周面と内周面に生じる圧力差による破損を防止することができる。 Further, in the fourth annular portion 17 and the sixth annular portion 19, grooves or protrusions on the outer peripheral surface are provided in a direction parallel to the element axial direction, or in the third annular portion 16, the outer peripheral surface and the inner peripheral surface are formed. By providing the through-hole, it is possible to prevent damage due to a pressure difference generated between the outer peripheral surface and the inner peripheral surface of each annular portion of the telescope prevention plate.
 また、図3Bに示すように、第5環状部18が、上流側端部の外径が下流側端部の外径より大きいこと、もしくは図4Bに示すように、外周に溝または突起23を有することが、外装体を強固に係合し、外装体からの下流側テレスコープ防止板10bの離脱を防ぐ観点から好ましい。また、上流側テレスコープ防止板10aについても同様であることから、第1環状部14が第5環状部18と面対称の同一形状であることがより好ましい。すなわち、第1環状部14は、図3Aに示すように下流側端部の外径が上流側端部の外径より大きいこと、もしくは図4Aに示すように外周に溝または突起23を有することが好ましい。 Further, as shown in FIG. 3B, the fifth annular portion 18 has an upstream end having an outer diameter larger than that of the downstream end, or a groove or protrusion 23 on the outer periphery as shown in FIG. 4B. It is preferable from the viewpoint of firmly engaging the exterior body and preventing separation of the downstream telescope prevention plate 10b from the exterior body. Moreover, since it is the same also about the upstream telescope prevention plate 10a, it is more preferable that the 1st annular part 14 is the same shape as the 5th annular part 18 and plane symmetry. That is, the first annular portion 14 has the outer diameter of the downstream end portion larger than the outer diameter of the upstream end portion as shown in FIG. 3A, or has a groove or protrusion 23 on the outer periphery as shown in FIG. 4A. Is preferred.
 上流側テレスコープ防止板および下流側テレスコープ防止板については、素材は特に限定しないが、生産性、コスト、軽量化の観点から、また、原液に含まれる様々な物質に対する耐薬品性も考慮し、アクリロニトリルブタジエンスチレン共重合樹脂(ABS)、塩化ビニル樹脂(PVC)、変性ポリフェニレンオキシド樹脂(PPO)、変性ポリフェニレンエーテル樹脂(PPE)、ポリオキシメチレン樹脂(POM)からなる群から選ばれる少なくとも1つであることが好ましい。また、この群から選ばれる少なくとも1つをガラス繊維強化樹脂(GFRP)として用いても良い。 The material for the upstream telescope prevention plate and the downstream telescope prevention plate is not particularly limited, but from the viewpoint of productivity, cost, and weight reduction, and also consider chemical resistance against various substances contained in the stock solution. And at least one selected from the group consisting of acrylonitrile butadiene styrene copolymer resin (ABS), vinyl chloride resin (PVC), modified polyphenylene oxide resin (PPO), modified polyphenylene ether resin (PPE), and polyoxymethylene resin (POM). It is preferable that Further, at least one selected from this group may be used as the glass fiber reinforced resin (GFRP).
 外装体については、高弾性率繊維を樹脂に含浸し熱硬化させて形成した繊維強化プラスチック(FRP)のシェルが好ましい。高弾性率繊維は、ガラス繊維、炭素繊維、アラミド繊維、金属繊維などが挙げられるが、これらに限定されるものではない。また、樹脂の素材も特に限定しないが、エポキシ樹脂、ポリエステル樹脂、ポリアミド樹脂、フェノール樹脂、メチルメタアクリレート樹脂などが挙げられるが、これらに限定されるものではない。高弾性率繊維および樹脂が膨潤すると、集液管軸方向に伸長し圧力容器へ分離膜エレメントを収納するのが困難となる。これを抑えるため、外装体を形成する高弾性率繊維および樹脂は、吸水率が90℃温水24時間浸漬における重量変化率で3%以下であることが好ましい。さらに、外装体は、分離膜エレメントの品名やロット番号等を識別するために膜ユニットの外周面上に貼り付けるラベルが視認可能な、透明性のあるものが好ましい。 For the exterior body, a fiber reinforced plastic (FRP) shell formed by impregnating a resin with a high modulus fiber and thermosetting it is preferable. Examples of the high modulus fiber include, but are not limited to, glass fiber, carbon fiber, aramid fiber, and metal fiber. The material of the resin is not particularly limited, and examples thereof include, but are not limited to, an epoxy resin, a polyester resin, a polyamide resin, a phenol resin, and a methyl methacrylate resin. When the high elastic modulus fiber and the resin swell, it becomes difficult to accommodate the separation membrane element in the pressure vessel by extending in the direction of the collecting tube axis. In order to suppress this, it is preferable that the high elastic modulus fiber and the resin forming the exterior body have a water absorption rate of 3% or less in terms of a weight change rate when immersed in 90 ° C. warm water for 24 hours. Further, the exterior body is preferably transparent so that a label attached to the outer peripheral surface of the membrane unit can be visually recognized in order to identify the product name, lot number, etc. of the separation membrane element.
 外装体の成形については、樹脂に含浸した高弾性率繊維を、一方のテレスコープ防止板の膜ユニット巻囲体側の一端(上流側テレスコープ防止板10aの第1環状部14)から、膜ユニットの外周を覆い、もう一方のテレスコープ防止板の膜ユニット巻囲体側の一端(下流側テレスコープ防止板10bの第5環状部18)まで巻きつけて熱硬化する方法が挙げられる。この場合、分離膜エレメント使用時にテレスコープ防止板が外装体から離脱もしくは破損するのを防ぐため、テレスコープ防止板の端部と膜ユニットの端部との間で繊維を集液管軸方向に往復させて固定させ、テレスコープ防止板の膜ユニット巻囲体側の一端に係合する部分における外装体の厚みを、膜ユニット巻囲体の軸方向中央部分における外装体の厚みよりも厚くすることが好ましい。また、膜ユニット巻囲体の外径が、テレスコープ防止板の膜ユニット巻囲体側の一端の外径よりも小さくなる場合、外装体における応力集中を防ぐため、外装体の厚みを、テレスコープ防止板の膜ユニット巻囲体側の一端に係合する部分から膜ユニット巻囲体の軸方向中央部分にかけてなだらかに減少させることが好ましい。 For the molding of the exterior body, the high modulus fiber impregnated in the resin is removed from one end (the first annular portion 14 of the upstream telescope prevention plate 10a) of one telescope prevention plate on the membrane unit surrounding side. The outer periphery of the other telescope prevention plate is wound to one end (the fifth annular portion 18 of the downstream telescope prevention plate 10b) of the other telescope prevention plate on the side of the membrane unit surrounding body and thermally cured. In this case, in order to prevent the telescope prevention plate from being detached or damaged from the exterior body when using the separation membrane element, the fibers are arranged in the direction of the collecting tube axis between the end of the telescope prevention plate and the end of the membrane unit. The thickness of the exterior body in the portion that engages with one end of the telescope prevention plate on the side of the membrane unit enclosure is made thicker than the thickness of the exterior body in the axial center portion of the membrane unit enclosure. Is preferred. In addition, when the outer diameter of the membrane unit enclosure is smaller than the outer diameter of one end of the telescope prevention plate on the membrane unit enclosure side, the thickness of the exterior body is reduced to prevent stress concentration in the exterior body. It is preferable that the thickness of the protective plate is gradually reduced from the portion engaging the one end of the membrane unit envelope on the side of the membrane unit envelope to the central portion in the axial direction of the membrane unit envelope.
 シールリングについては、流体分離時の圧力によって外側に拡がり、圧力容器の内面との隙間を封止するため、断面はU字型やV字型の形状が好ましい。また、素材は特に限定しないが、例えばエチレンプロピレンゴム(EPM,EPDM)、ニトリルゴム(NBR)またはシリコンゴムが選択される。 As for the seal ring, the U-shaped or V-shaped cross section is preferable because it expands outward due to the pressure during fluid separation and seals the gap with the inner surface of the pressure vessel. The material is not particularly limited, and for example, ethylene propylene rubber (EPM, EPDM), nitrile rubber (NBR), or silicon rubber is selected.
 本発明の分離膜エレメントによれば、テレスコープ防止板の機能を維持しつつ膜面積の増加を可能とする。すなわち、下流側テレスコープ防止板を、上流側テレスコープ防止板におけるシールリングを外挿するのに必要な部分に相当する軸方向の幅だけ小さくしたため、膜面積の増加が可能となる。 According to the separation membrane element of the present invention, it is possible to increase the membrane area while maintaining the function of the telescope prevention plate. That is, since the downstream telescope prevention plate is reduced by the axial width corresponding to the portion necessary for extrapolating the seal ring in the upstream telescope prevention plate, the membrane area can be increased.
 <比較例1>
 上流側テレスコープ防止板において、各環状部の分離膜エレメント軸方向の幅を、第1環状部7.2mm、第2環状部4.0mm、第3環状部8.8mm、第4環状部4.5mm、全体24.5mmとし、下流側テレスコープ防止板は上流側テレスコープ防止板と同一のものを使用して、図5に示すような、エレメント軸方向の長さが964mmである膜ユニット29枚からなる8インチ分離膜エレメントの作製を行った結果、分離膜エレメントの有効膜面積は約440平方フィートとなった。
<Comparative Example 1>
In the upstream telescope prevention plate, the width of each annular portion in the axial direction of the separation membrane element is defined as the first annular portion 7.2 mm, the second annular portion 4.0 mm, the third annular portion 8.8 mm, and the fourth annular portion 4. 5 mm, 24.5 mm in total, and the downstream telescope prevention plate is the same as the upstream telescope prevention plate, and the length in the element axial direction is 964 mm as shown in FIG. As a result of producing 29-inch 8-inch separation membrane elements, the effective membrane area of the separation membrane elements was about 440 square feet.
 <実施例1>
 上流側テレスコープ防止板において、各環状部の分離膜エレメント軸方向の幅を、第1環状部7.2mm、第2環状部4.0mm、第3環状部8.8mm、第4環状部4.5mm、全体24.5mmとした。また、下流側テレスコープ防止板において、各環状部の分離膜エレメント軸方向の幅を、第5環状部7.2mm、第6環状部4.0mm、全体11.2mmとした。この場合、下流側テレスコープ防止板のエレメント軸方向の幅は、上流側テレスコープ防止板の46%となる。これらのテレスコープ防止板を使用して、図2に示すような、エレメント軸方向の長さが964mmである膜ユニット29枚からなる分離膜エレメントの作製を行った結果、分離膜エレメントの有効膜面積は約446平方フィートとなった。すなわち、比較例1で作製した8インチ分離膜エレメントと比較して、有効膜面積が約1.4%増加した。
<Example 1>
In the upstream telescope prevention plate, the width of each annular portion in the axial direction of the separation membrane element is defined as the first annular portion 7.2 mm, the second annular portion 4.0 mm, the third annular portion 8.8 mm, and the fourth annular portion 4. 0.5 mm and 24.5 mm overall. In the downstream telescope prevention plate, the width of each annular portion in the separation membrane element axial direction was set to a fifth annular portion 7.2 mm, a sixth annular portion 4.0 mm, and a total of 11.2 mm. In this case, the width of the downstream telescope prevention plate in the element axial direction is 46% of that of the upstream telescope prevention plate. As a result of producing separation membrane elements composed of 29 membrane units each having a length of 964 mm in the element axial direction using these telescope prevention plates, the effective membrane of the separation membrane element was obtained. The area was about 446 square feet. That is, compared to the 8-inch separation membrane element produced in Comparative Example 1, the effective membrane area increased by about 1.4%.
 続いて、上記分離膜エレメントの上流側テレスコープ防止板の第3環状部にシールリングを外挿し、圧力容器に装填して、海水の膜分離を運転圧力5.5MPaにて1ヶ月間実施した結果、テレスコープ防止板の外装体からの離脱や膜ユニットの型崩れはなく、テレスコープ防止板の機能を維持していることが確認できた。 Subsequently, a seal ring was extrapolated to the third annular portion of the upstream telescope prevention plate of the separation membrane element and loaded into a pressure vessel, and membrane separation of seawater was performed at an operating pressure of 5.5 MPa for one month. As a result, it was confirmed that the telescope prevention plate was not detached from the outer casing and the membrane unit was not deformed, and the function of the telescope prevention plate was maintained.
 1  分離膜エレメント
 2  集液孔
 3  集液管
 4  分離膜
 5  透過液流路材
 6  原液流路材
 7  膜ユニット
 8  外装体
10  テレスコープ防止板
10a 上流側テレスコープ防止板
10b 下流側テレスコープ防止板
11  原液流路
12  シールリング
13  圧力容器
14  第1環状部
15  第2環状部
16  第3環状部
17  第4環状部
18  第5環状部
19  第6環状部
20  原液
21  透過液
DESCRIPTION OF SYMBOLS 1 Separation membrane element 2 Liquid collection hole 3 Liquid collection pipe 4 Separation membrane 5 Permeate flow path material 6 Stock solution flow path material 7 Membrane unit 8 Exterior body 10 Telescope prevention plate 10a Upstream telescope prevention plate 10b Downstream telescope prevention Plate 11 Stock solution flow path 12 Seal ring 13 Pressure vessel 14 First annular portion 15 Second annular portion 16 Third annular portion 17 Fourth annular portion 18 Fifth annular portion 19 Sixth annular portion 20 Stock solution 21 Permeate

Claims (6)

  1.  分離膜、原液流路材および透過液流路材がスパイラル状に巻回されてなるスパイラル巻体の外周に外装体が設けられるとともに前記スパイラル巻体および前記外装体の両端部にそれぞれ上流側テレスコープ防止板および下流側テレスコープ防止板が配設された構造を有し、圧力容器内に直列に複数装填して使用される分離膜エレメントであって、前記上流側テレスコープ防止板は、前記外装体が外挿される第1環状部と、前記第1環状部の上流側に形成され、下流側および上流側の端面にそれぞれ前記外装体の上流側端部およびシールリングの下流側端面を係止可能な第2環状部と、前記第2環状部の上流側に形成され、前記シールリングが外挿される第3環状部と、前記第3環状部の上流側に形成され、下流側端面に前記シールリングの上流側端面が係止可能な第4環状部からなり、さらに、前記下流側テレスコープ防止板は、前記外装体が外挿される第5環状部と、前記第5環状部の下流側に形成され、上流側端面に前記外装体の下流側端部を係止可能な第6環状部からなることを特徴とする分離膜エレメント。 An exterior body is provided on the outer periphery of a spiral wound body in which a separation membrane, a raw liquid flow path material, and a permeate flow path material are wound in a spiral shape, and an upstream telescope is provided at each end of the spiral wound body and the exterior body. A separation membrane element that has a structure in which a scope prevention plate and a downstream telescope prevention plate are disposed, and is used by being loaded in series in a pressure vessel, wherein the upstream telescope prevention plate is A first annular portion on which the exterior body is extrapolated and an upstream end surface of the exterior body and a downstream end surface of the seal ring are respectively formed on the upstream side and the downstream end surface of the first annular portion. A second annular portion that can be stopped, a third annular portion that is formed on the upstream side of the second annular portion, and on which the seal ring is extrapolated; an upstream side of the third annular portion; Of the seal ring The downstream end surface of the downstream telescope prevention plate is formed on the downstream side of the fifth annular portion and the fifth annular portion on which the exterior body is extrapolated. A separation membrane element comprising a sixth annular portion capable of locking the downstream end portion of the outer package to the upstream end surface.
  2.  前記下流側テレスコープ防止板の分離膜エレメント軸方向の幅が、前記上流側テレスコープ防止板の分離膜エレメント軸方向の幅の15%以上60%以下であることを特徴とする、請求項1に記載の分離膜エレメント。 The width in the separation membrane element axial direction of the downstream telescope prevention plate is 15% or more and 60% or less of the width in the separation membrane element axial direction of the upstream telescope prevention plate. The separation membrane element described in 1.
  3.  前記第4環状部および前記第6環状部の外径が、分離膜エレメント軸方向について一定であることを特徴とする、請求項1または2に記載の分離膜エレメント。 The separation membrane element according to claim 1 or 2, wherein the outer diameters of the fourth annular portion and the sixth annular portion are constant in the axial direction of the separation membrane element.
  4.  前記第5環状部において、上流側端部の外径が下流側端部の外径より大きいことを特徴とする、請求項1~3のいずれかに記載の分離膜エレメント。 4. The separation membrane element according to claim 1, wherein, in the fifth annular portion, the outer diameter of the upstream end is larger than the outer diameter of the downstream end.
  5.  前記第5環状部が、外周に溝または突起を有することを特徴とする、請求項1~4のいずれかに記載の分離膜エレメント。 The separation membrane element according to any one of claims 1 to 4, wherein the fifth annular portion has a groove or a protrusion on an outer periphery.
  6.  前記第1環状部が、前記第5環状部と同一形状であることを特徴とする、請求項1~5のいずれかに記載の分離膜エレメント。 6. The separation membrane element according to claim 1, wherein the first annular portion has the same shape as the fifth annular portion.
PCT/JP2014/055634 2013-03-11 2014-03-05 Separating membrane element WO2014141967A1 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023156509A1 (en) * 2022-02-21 2023-08-24 Evonik Operations Gmbh High-temperature spiral-wound module made of metal components

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000093761A (en) * 1998-09-24 2000-04-04 Toray Ind Inc Fluid separation element
JP2005111473A (en) * 2003-09-17 2005-04-28 Nitto Denko Corp Membrane element and sealing material holding member therefor
WO2010095739A1 (en) * 2009-02-23 2010-08-26 日東電工株式会社 Edge member for film element and film element equipped with same

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000093761A (en) * 1998-09-24 2000-04-04 Toray Ind Inc Fluid separation element
JP2005111473A (en) * 2003-09-17 2005-04-28 Nitto Denko Corp Membrane element and sealing material holding member therefor
WO2010095739A1 (en) * 2009-02-23 2010-08-26 日東電工株式会社 Edge member for film element and film element equipped with same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023156509A1 (en) * 2022-02-21 2023-08-24 Evonik Operations Gmbh High-temperature spiral-wound module made of metal components

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