JPS59162906A - Fluid separation apparatus and preparation thereof - Google Patents

Fluid separation apparatus and preparation thereof

Info

Publication number
JPS59162906A
JPS59162906A JP3786583A JP3786583A JPS59162906A JP S59162906 A JPS59162906 A JP S59162906A JP 3786583 A JP3786583 A JP 3786583A JP 3786583 A JP3786583 A JP 3786583A JP S59162906 A JPS59162906 A JP S59162906A
Authority
JP
Japan
Prior art keywords
outer cylinder
fluid separation
resin
membranes
separation device
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP3786583A
Other languages
Japanese (ja)
Other versions
JPH0317527B2 (en
Inventor
Norio Ikeyama
紀男 池山
Koichi Okuno
幸一 奥野
Shusaku Tamaru
田丸 秀作
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nitto Denko Corp
Original Assignee
Nitto Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nitto Electric Industrial Co Ltd filed Critical Nitto Electric Industrial Co Ltd
Priority to JP3786583A priority Critical patent/JPS59162906A/en
Publication of JPS59162906A publication Critical patent/JPS59162906A/en
Publication of JPH0317527B2 publication Critical patent/JPH0317527B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C41/00Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
    • B29C41/02Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of definite length, i.e. discrete articles
    • B29C41/04Rotational or centrifugal casting, i.e. coating the inside of a mould by rotating the mould
    • B29C41/042Rotational or centrifugal casting, i.e. coating the inside of a mould by rotating the mould by rotating a mould around its axis of symmetry
    • B29C41/045Rotational or centrifugal casting, i.e. coating the inside of a mould by rotating the mould by rotating a mould around its axis of symmetry the axis being placed vertically, e.g. spin casting
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C41/00Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
    • B29C41/02Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of definite length, i.e. discrete articles
    • B29C41/20Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of definite length, i.e. discrete articles incorporating preformed parts or layers, e.g. moulding inserts or for coating articles

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To prevent the generation of contamination in an internal pressure type fluid separation apparatus using a tubular or hollow fiber membrane caused by microorganisms propagated in the presence of the permeation liquid or air bubbles stayed in the apparatus, by imparting a specific configuration to each inner surface of the fixing parts due to a resin at both end parts of said apparatus. CONSTITUTION:A plurality of hollow fiber membranes 1 are received in an outer cylinder 3 having a permeation liquid outtake port 2 in a parallelly bundled state and the mutual spaces between the hollow fiber membranes and the outer cylinder 3 are secured at both end parts thereof by a casting resin 4. The inner surface 4' of this casting resin 4 is brought to the surface almost same to the opening surface 2' of the permeation liquid outtake port 2 in the vicinity thereof and formed into a slightly concaved surface shape from said opening surface 2' toward the outer cylinder 3. That is, the distance (l') between the inner surface 4' of the casting resin 4 in the inner wall of the outer cylinder 3 in the opposite side of the opening surface 2' becomes gradually large with respect to the distance (l) between the inner surface 4' and the end surface 4'' of said resin 4. The liquid permeated through the hollow fiber membranes 1 is smoothly flowed along the inner surface 4' in a staying-free state and easily withdrawn from the system through the permeation liquid outtake port 2.

Description

【発明の詳細な説明】 本発明は、管状膜又は中空繊維状膜を用いた内圧式の流
体分離装置及びその製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an internal pressure type fluid separation device using a tubular membrane or a hollow fibrous membrane, and a method for manufacturing the same.

逆浸透、限外沢過又は精密沢過により原液から溶媒又は
溶質を分離する際あるいはガス分離等の際に、管状膜又
は中空繊維状膜を有する内圧式の流体分離装置を使用す
ることがある。
When separating solvents or solutes from stock solutions by reverse osmosis, ultrafiltration, or precision filtration, or for gas separation, internal pressure fluid separation devices with tubular or hollow fibrous membranes may be used. .

従来このような流体分離装置としては、管状膜又は中空
繊維状膜とそれを収納する外筒とが両端で注形樹脂によ
り固着されたものが知られている。
Conventionally, as such a fluid separation device, one in which a tubular membrane or a hollow fibrous membrane and an outer cylinder housing the membrane are fixed at both ends with casting resin is known.

第1図は従来の中空繊維状膜を用いた流体分離装置の一
例を示すものであり、複数本の中空繊維状膜11が平行
に集束されており、この両端は透過液収IJ3012を
有する外筒13に注形樹脂14により一体に固着されて
いる。
FIG. 1 shows an example of a fluid separation device using conventional hollow fibrous membranes, in which a plurality of hollow fibrous membranes 11 are bundled in parallel, and both ends of the hollow fibrous membranes 11 are connected to an outer wall having a permeate collecting IJ3012. It is integrally fixed to the cylinder 13 with molding resin 14.

上記装置1ffiを用いて液体を分離処理する場合、該
ら供給され、濃縮液は他方より流出され、得られた透過
液は、透過液取出口12より流出される。
When a liquid is separated using the apparatus 1ffi, the liquid is supplied, the concentrated liquid is discharged from the other side, and the obtained permeate is discharged from the permeate outlet 12.

このような流体分離装置の製造には、注形樹脂を外筒両
端に良好に充填させると共に注形樹脂の内面を均一にす
るために遠心注形法が用いられている。しかしながら従
来の遠心注形法で1ハ、第2図に示す如く遠心注形の回
転中心0を外筒13の中心軸P線上に設定し該中心軸P
と垂直な軸Qの周りに回転させているため、注形樹脂1
4は同転半径Rに沿って硬化し、注形樹脂14の内面1
4′は中心軸Pに対してわずかに凹面状に形成されてい
る。そのため運転開始時に生じる気泡や透過液が上記内
面14’付近に滞留し該滞留部に微生物が繁殖して、透
過液が汚染する等の問題が生じ、流体分離装置の性能の
低下を招くという欠点かぁ−。
In manufacturing such a fluid separation device, a centrifugal casting method is used in order to satisfactorily fill both ends of the outer cylinder with casting resin and to make the inner surface of the casting resin uniform. However, in the conventional centrifugal casting method, as shown in FIG.
Since it is rotated around the axis Q perpendicular to the casting resin 1
4 hardens along the rotational radius R, and the inner surface 1 of the casting resin 14
4' is formed in a slightly concave shape with respect to the central axis P. Therefore, bubbles and permeate generated at the start of operation accumulate near the inner surface 14', causing problems such as microorganisms propagating in the retention area and contaminating the permeate, resulting in a decrease in the performance of the fluid separation device. Huh.

たO 不発明はかかる従来波□術の欠点を解決するためになさ
れたものでろって、装置内に流体滞留部が存在せず、装
置μの性能低■を防ぎ安蚕件の極めて高い流体分離装置
及びその製造方法を提供するものである。
The invention was made in order to solve the drawbacks of the conventional wave technique.There is no fluid retention part in the device, which prevents the low performance of the device and makes it possible to create an extremely safe fluid. The present invention provides a separation device and a method for manufacturing the same.

即ち本発明は、管状膜又は中空繊維状膜が複数本平行に
集束されて透過液取出口を有する外筒内に収納され、そ
の両端部における上記膜相互間及び膜と外筒とが注形樹
脂で固着されてなる流体分離装置において、上記注形樹
脂の内面が、透過液取出口の開口面近傍において該開口
面と略同−面となると共に上記開口面から外筒内方向に
向って胡次湾曲していることを特徴とする流体分離装置
に関するものである。
That is, in the present invention, a plurality of tubular membranes or hollow fibrous membranes are bundled in parallel and housed in an outer cylinder having a permeate outlet, and the membranes at both ends thereof and between the membranes and the outer cylinder are formed by casting. In a fluid separation device fixed with resin, the inner surface of the molded resin is approximately flush with the opening surface of the permeated liquid outlet in the vicinity of the opening surface, and extends from the opening surface toward the inside of the outer cylinder. The present invention relates to a fluid separation device characterized by a curved shape.

さらに本発明は上記流体分離装置の製造方法を提供する
ものであり、管状膜又は中空繊維状膜を複数本平行に集
束して透過液取出口を有する外面内に収納し、その両端
部における十記膜相〃間及び膜と外筒とを注形樹脂で遠
心注形により固着する流体分離装置の製造方法において
、−上記遠心注形の回転中心を、外筒の中心軸に対して
垂直な軸に沿って透過液取出口側へ偏心させた状態で遠
心注形することを特徴とする流体分離装置の製造方法に
関するものである。
Furthermore, the present invention provides a method for manufacturing the above-mentioned fluid separation device, in which a plurality of tubular membranes or hollow fibrous membranes are bundled in parallel and housed in an outer surface having a permeate outlet. In the manufacturing method of a fluid separation device in which the membrane phase and the membrane and the outer cylinder are fixed with casting resin by centrifugal casting, the center of rotation of the centrifugal casting is set perpendicular to the central axis of the outer cylinder. The present invention relates to a method for manufacturing a fluid separation device characterized by performing centrifugal casting in a state eccentric to the permeate outlet side along the axis.

以下、本発明の実例として中空繊維状膜を用いた流体分
離装置について図面に基づいて説明するが、本発明は透
水性不織布管の内面に透過膜を設けてなる管状膜を用い
た流体分離装置にも適用できるものである。
Hereinafter, a fluid separation device using a hollow fibrous membrane will be described as an example of the present invention based on the drawings. It can also be applied to

第3図において、複数本の中空#[状膜1が平行に集束
されて透過液取出口2を有する外筒3内に収納され、そ
の両端部の中空繊維状膜1相互間及び中空繊維状膜1と
外筒3とが注形樹脂4で固着されている。該注形樹脂4
の内面4′は、透過液取出口2の開口面グの近傍におい
て該開口面2′と略同−面とされており、かつ上記開口
面2′から外筒3内方向に向ってわずかに凹面状に漸次
湾曲している。すなわち注形樹脂4の内面4′は、開口
面2′における注形樹脂4の内面4′と端面4“との距
離lに対して上記開口面2′と反対側の外筒3内壁にお
ける内面4′と端面4“との距離4′が漸次大きくなる
ように形成されている。
In FIG. 3, a plurality of hollow membranes 1 are bundled in parallel and housed in an outer cylinder 3 having a permeate outlet 2, and the hollow fibrous membranes 1 at both ends are The membrane 1 and the outer cylinder 3 are fixed with a casting resin 4. The casting resin 4
The inner surface 4' is approximately flush with the opening surface 2' of the permeated liquid outlet 2 in the vicinity of the opening surface 2', and slightly extends from the opening surface 2' toward the inside of the outer cylinder 3. It is gradually curved in a concave shape. That is, the inner surface 4' of the casting resin 4 is the inner surface of the inner wall of the outer cylinder 3 on the opposite side to the opening surface 2' with respect to the distance l between the inner surface 4' of the casting resin 4 at the opening surface 2' and the end surface 4''. The distance 4' between the end face 4'' and the end face 4'' gradually increases.

このように構成してなる流体分離装置を用いて液体を分
離処理すると、気泡や透過液は装置内に滞留することな
く注形樹脂4の内面4′に沿うてスムーズに流れ、透過
液取出口2から系外へ良好に抜くことができる。
When a liquid is separated using the fluid separation device configured in this manner, bubbles and permeate flow smoothly along the inner surface 4' of the molded resin 4 without remaining in the device, and the permeate exit port 2 can be successfully extracted from the system.

上記流体分離装置は、中空繊維状膜1を複数本平行に集
束して外筒3内に収納し、その両端部の中空#l!維状
膜1相互間及び中空fJ!!維状膜1と外筒3とを注形
樹脂4で遠心注形により固着する際に、遠心注形の回転
中心Oを外筒3の中心軸Pに対して垂直な軸Qに沿−2
で透過液取出口2側へ偏心させて遠心注形を行なうこと
により得られる。ここで偏心量θは外筒3の長さ及び内
径により異なるが少なくとも外筒3の内径の1/2倍以
上であればよく、通常1/2〜2倍とする。また偏心t
eを大きくすれば注形樹脂4の内面4′と端面4“との
距離の差(#’−l )を大きくすることができるが、
本   ゛好マシくは10+u〜20酊程度となるよう
に偏心量eを設定するのがよい。
The above-mentioned fluid separation device has a plurality of hollow fibrous membranes 1 bundled in parallel and housed in an outer cylinder 3, with hollow #l! Between fibrous membranes 1 and hollow fJ! ! When fixing the fibrous membrane 1 and the outer cylinder 3 with the casting resin 4 by centrifugal casting, the rotation center O of the centrifugal casting is aligned along the axis Q perpendicular to the central axis P of the outer cylinder 3.
This can be obtained by performing centrifugal injection while eccentrically moving toward the permeate outlet 2 side. Here, the eccentricity θ varies depending on the length and inner diameter of the outer cylinder 3, but may be at least 1/2 times the inner diameter of the outer cylinder 3, and is usually set to 1/2 to 2 times. Also, eccentricity t
If e is increased, the difference in distance (#'-l) between the inner surface 4' and end surface 4'' of the casting resin 4 can be increased;
It is preferable to set the eccentricity e to be about 10+u to 20+u.

以上に述べた如く本発明によれば、装置内に流体滞留部
が存在しないため気泡や透過液が滞留せず、装置の性能
低下を防ぎ安全性の極めて高い流体分離装置が得られる
という10点を有する。
As described above, according to the present invention, since there is no fluid retention part in the device, air bubbles and permeate do not accumulate, preventing deterioration of device performance and providing a fluid separation device with extremely high safety. has.

なお以上の説明では液体を膜分離処理する場合を示した
が、本発明の流体分離装置は、カス分離処理にも適用す
ることができるものである。
Note that although the above explanation has been given for the case where liquid is subjected to membrane separation treatment, the fluid separation device of the present invention can also be applied to waste separation treatment.

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

第1図は従来の流体分離装置を示す縦断面図、第2図は
第1図の端部の拡大縦断面図、第3図は本発明の実例を
示す流体分離装置の端部の拡大縦断面図である。 l・・・・・・中空繊維状膜、2・・・・・・透過液取
出口、3・・・・・外筒、4・・・・・・注形樹脂特許
出願人 日東電気工業株式会社 代表者土方三部
FIG. 1 is a longitudinal sectional view showing a conventional fluid separation device, FIG. 2 is an enlarged longitudinal sectional view of the end of FIG. 1, and FIG. 3 is an enlarged longitudinal sectional view of the end of the fluid separation device showing an example of the present invention. It is a front view. l...Hollow fibrous membrane, 2...Permeated liquid outlet, 3...Outer cylinder, 4...Casting resin patent applicant Nitto Electric Industry Co., Ltd. Company representative Sanbe Hijikata

Claims (2)

【特許請求の範囲】[Claims] (1)管状膜又は中空繊維状膜が複数本平行に集束され
て透過液取出口を有する外筒内に収納され、その両端部
における上記膜相互間及び膜と外筒とが注形樹脂で固着
されてなる流体分離装置において、上記注形樹脂の内面
が、透過液取出口の開口面近傍において該開口面と略同
−面となると共に上記開口面から外筒内方向に向って漸
次湾曲していることを特徴とする流体分離装置。
(1) A plurality of tubular membranes or hollow fibrous membranes are bundled in parallel and housed in an outer cylinder having a permeate outlet, and the spaces between the membranes at both ends and the membrane and the outer cylinder are made of casting resin. In the fluid separation device, the inner surface of the molded resin is approximately flush with the opening surface of the permeate outlet near the opening surface of the permeate outlet, and is gradually curved from the opening surface toward the inside of the outer cylinder. A fluid separation device characterized by:
(2)管状膜V、は中空繊維状膜を複数本平行に集束し
て透過液取出口を有する外筒内に収納し、その両端部に
おける上記膜相互間及び膜と外筒とを注形1酎脂で遠心
注形により固有する流体分離装置の製造方法に分いて、
上記遠心注形の回転中心を、外筒の中心軸に対して垂直
な軸に沿って透過液取出口側へ偏心さすた状態で遠心注
形することを特徴とする流体分離装置の製造方法C
(2) The tubular membrane V is a plurality of hollow fibrous membranes bundled in parallel and housed in an outer cylinder having a permeate outlet, and molded between the membranes at both ends and between the membrane and the outer cylinder. 1. A unique method for manufacturing a fluid separation device using centrifugal casting using lard,
A method for manufacturing a fluid separation device C, characterized in that centrifugal casting is performed with the center of rotation of the centrifugal casting eccentrically pointing toward the permeate outlet side along an axis perpendicular to the central axis of the outer cylinder.
JP3786583A 1983-03-07 1983-03-07 Fluid separation apparatus and preparation thereof Granted JPS59162906A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3786583A JPS59162906A (en) 1983-03-07 1983-03-07 Fluid separation apparatus and preparation thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3786583A JPS59162906A (en) 1983-03-07 1983-03-07 Fluid separation apparatus and preparation thereof

Publications (2)

Publication Number Publication Date
JPS59162906A true JPS59162906A (en) 1984-09-13
JPH0317527B2 JPH0317527B2 (en) 1991-03-08

Family

ID=12509431

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3786583A Granted JPS59162906A (en) 1983-03-07 1983-03-07 Fluid separation apparatus and preparation thereof

Country Status (1)

Country Link
JP (1) JPS59162906A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0229388A2 (en) * 1986-01-10 1987-07-22 Fresenius AG Hollow fibre filter for the production of plasma or plasma water and process for the manufacture thereof
JPH02237622A (en) * 1989-01-27 1990-09-20 Ceramiques Techniques Soc Assembling method of rigid element having membrance for separation, filtration or catalytic reforming in module
FR2865415A1 (en) * 2004-01-22 2005-07-29 Tech Avancees & Membranes Ind Filter module with an external envelope attached at each end to a support plate for one or more filter elements where the support plates have a fixing skirt to assemble them to the envelope
JP2007144349A (en) * 2005-11-29 2007-06-14 Ebara Corp Hollow fiber membrane module

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56100605A (en) * 1980-01-16 1981-08-12 Kuraray Co Ltd Hollow yarn element
JPS5939603U (en) * 1982-09-08 1984-03-13 日東電工株式会社 liquid separator

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56100605A (en) * 1980-01-16 1981-08-12 Kuraray Co Ltd Hollow yarn element
JPS5939603U (en) * 1982-09-08 1984-03-13 日東電工株式会社 liquid separator

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0229388A2 (en) * 1986-01-10 1987-07-22 Fresenius AG Hollow fibre filter for the production of plasma or plasma water and process for the manufacture thereof
US4789473A (en) * 1986-01-10 1988-12-06 Fresenius Ag Filter for obtaining plasma or plasma water
JPH02237622A (en) * 1989-01-27 1990-09-20 Ceramiques Techniques Soc Assembling method of rigid element having membrance for separation, filtration or catalytic reforming in module
FR2865415A1 (en) * 2004-01-22 2005-07-29 Tech Avancees & Membranes Ind Filter module with an external envelope attached at each end to a support plate for one or more filter elements where the support plates have a fixing skirt to assemble them to the envelope
JP2007144349A (en) * 2005-11-29 2007-06-14 Ebara Corp Hollow fiber membrane module

Also Published As

Publication number Publication date
JPH0317527B2 (en) 1991-03-08

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