JPS6010764B2 - fluid separation device - Google Patents

fluid separation device

Info

Publication number
JPS6010764B2
JPS6010764B2 JP8268677A JP8268677A JPS6010764B2 JP S6010764 B2 JPS6010764 B2 JP S6010764B2 JP 8268677 A JP8268677 A JP 8268677A JP 8268677 A JP8268677 A JP 8268677A JP S6010764 B2 JPS6010764 B2 JP S6010764B2
Authority
JP
Japan
Prior art keywords
membrane
separation device
folded
fluid separation
water collection
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.)
Expired
Application number
JP8268677A
Other languages
Japanese (ja)
Other versions
JPS5417378A (en
Inventor
安弘 坂口
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.)
Daicel Corp
Original Assignee
Daicel Chemical Industries 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 Daicel Chemical Industries Ltd filed Critical Daicel Chemical Industries Ltd
Priority to JP8268677A priority Critical patent/JPS6010764B2/en
Priority to IL7854676A priority patent/IL54676A0/en
Priority to US05/906,076 priority patent/US4235722A/en
Priority to GB23000/78A priority patent/GB1581122A/en
Priority to DE19782825698 priority patent/DE2825698A1/en
Priority to FR7817538A priority patent/FR2394318A1/en
Publication of JPS5417378A publication Critical patent/JPS5417378A/en
Publication of JPS6010764B2 publication Critical patent/JPS6010764B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 精密炉過、限外炉週、逆浸透法などの液体分離技術は、
分離・精製・濃縮の単位操作や、造水・産業排水処理の
前処理やメインプロセスとして実用化され始めてきた。
[Detailed Description of the Invention] Liquid separation technologies such as precision furnace filtration, ultrafurnace filtration, and reverse osmosis are
It has begun to be put into practical use as unit operations for separation, purification, and concentration, as well as pretreatment and main processes for water production and industrial wastewater treatment.

膜分離装置の形式には管状型、渦巻型、中空繊維型、プ
レート型の4種があり、単位シェル容積当りの有効膜表
面積の大小、装置形式と膜の汚染度の大小、運転管理の
難易などの面でそれぞれ長所短所があることは文献など
により公知の通りである。特に現在、用途適性や装置価
格の面から実用上最も多用されているものは、渦巻型で
あり、その単位シェル容積当りの有効膜表面積は650
〜700め/れ程度である。
There are four types of membrane separation equipment: tubular type, spiral type, hollow fiber type, and plate type.The size of the effective membrane surface area per unit shell volume, the size of the device type, the degree of contamination of the membrane, and the difficulty of operational management. It is well known from literature that each type has its own advantages and disadvantages. In particular, currently, the most commonly used type in practice from the viewpoint of suitability and equipment cost is the spiral type, which has an effective membrane surface area of 650 per unit shell volume.
It is about 700 to 700.

しかもこの渦巻型はその流体分離機能部(以下これを「
ヱレメント」と称する)の製造に当り1.5のから2.
0仇の二枚の平膜を封筒状に三方をシールしたいわゆる
「リーフ」を渦巻型に捲き上げる必要があり、捲き上げ
管理が複雑である。特に直径15仇舷〜30仇舷のェレ
メントを製造する場合は4リーフ、6リーフなどマルチ
リーフを用い、リーフ内の集水チャンネルの流通抵抗を
軽減化する方式を探用せざるを得ないのが実状である。
Moreover, this spiral type has a fluid separation function (hereinafter referred to as "
1.5 to 2.
It is necessary to roll up the so-called "leaf", which is made by sealing two flat membranes on three sides like an envelope, into a spiral shape, and the management of rolling it up is complicated. In particular, when manufacturing elements with a diameter of 15 to 30 m, it is necessary to use multi-leaf, such as 4-leaf or 6-leaf, to find a method to reduce the flow resistance of the water collection channel within the leaf. is the actual situation.

そのため、これらェレメントの大型化に伴い捲き上げ管
理は更に複雑になり、コストも割高になる欠点がある。
本発明者はこれらの欠点を改善すべ〈各種のェレメント
につき検討を加えた結果、製造管理が容易で信頼性が大
きく且つコスト面からも最も経済的なェレメントを発明
した。
Therefore, as these elements become larger, the winding management becomes more complicated and the cost becomes relatively high.
The inventor of the present invention sought to improve these shortcomings and, after studying various elements, invented an element that is easy to manufacture, highly reliable, and most economical in terms of cost.

以下本発明の装置を図示の実施態様に基き説明する。The apparatus of the present invention will be explained below based on the illustrated embodiments.

本発明の装置はいわゆるプリーツ型流体分離装置の一種
で第1図に示すように連続した一枚の分離膜又は髪打布
付膜をアコーデオン状に上下二段に折りたたみ、かく折
りたたまれた分離膜1の眉間に濃度分極現像を軽減させ
る為の網状スベーサ‐2を有し、上下二段間に膿透過水
の築水用として多数の孔を有する扇平状の集水管を有し
、分離膜1はその端部を3の個所で接着剤で重着され、
折りたたんだ端部は第5図の末端シール部6又は第7図
の末端シール部6に示すようにェポキシ樹脂、ウレタン
樹脂、シリコン樹脂などの合成樹脂系接着剤で全面又は
必要面を密封され、折たたみ部の外周は分離膜の保護と
同時に供孫舎液線速度を高める為にプラスチックフィル
ム5で捲き上げられることによりェレメントが構成され
る。
The device of the present invention is a type of so-called pleated fluid separation device, and as shown in FIG. It has a net-like smoother 2 between the eyebrows of 1 to reduce concentration polarization development, and has a fan-shaped water collection pipe with many holes between the upper and lower two stages for building up water permeated with pus, and a separation membrane. 1 has its end overlapped with adhesive at point 3,
The folded end is sealed on its entire surface or on necessary surfaces with a synthetic resin adhesive such as epoxy resin, urethane resin, or silicone resin, as shown in the end seal part 6 in FIG. 5 or the end seal part 6 in FIG. The outer periphery of the folded part is rolled up with a plastic film 5 to protect the separation membrane and increase the linear velocity of the liquid, thereby forming an element.

このェレメントを第5図又は第6図に示す如く耐圧円筒
管8内に内接させて挿入し、該円筒管8とェレメントで
形成される空間をプラスチックスフィルム5上の任意の
場所で例えば7の如く閉塞し、ェレメント内供〉給液線
速を高めるよう流路規制を行う。
This element is inserted into a pressure-resistant cylindrical tube 8 as shown in FIG. 5 or FIG. The flow path is restricted to increase the linear velocity of liquid supply within the element.

この結果ェレメントは円筒管8内で第5図と第7図に示
す給液流路10の例が生じるが、ェレメント性能として
は特に差はない。
As a result, an example of the liquid supply channel 10 shown in FIGS. 5 and 7 is generated in the element within the cylindrical pipe 8, but there is no particular difference in element performance.

又、一枚の分離膜から構成されるェレメントの変法とし
て二枚の分離膜を別々に折りたたみ、かく折りたたまれ
た二つの膜体を繋水管14を中心として、第9図に示す
様に枠12で一体的に組立てられたェレメントも考えら
れる。
In addition, as a modification of the element composed of one separation membrane, two separation membranes are folded separately, and the two membrane bodies thus folded are placed in a frame as shown in FIG. Elements assembled integrally with 12 are also conceivable.

なお、本願で述べる枠というのは2枚の割り型になって
おり、これを対向させてボルトナットにより結合させて
第1図における扇平状集水管4の扇平部に相当する役割
りをもたせたものである。この場合、折りたたまれた分
離膜1は網状スベーサー2を間挿した状態で膿透過水を
通過させるための多孔板13と集水管14と‘0’リン
グ溝とを具備した枠12に組込み、枠12内辺と膜体と
の間を接着剤でシールし、供給液部と膜透過部とを完全
に分離できる。かく構成された枠付膜体を上下に組合せ
枠内に‘0’リングを入れボルトナットにより枠を結合
し、以下一枚の分離膜から構成されたェレメント同様に
して、組立て方式によるェレメントが形成される。同様
にして膿体の数を増やして大きなェレメントを形成でき
るが、製造管理が複雑化し、コストアップする欠点があ
る。
In addition, the frame described in this application is made of two split molds, which are placed facing each other and connected with bolts and nuts to play a role corresponding to the fan flat part of the fan flat water collection pipe 4 in Fig. 1. It is something that has been maintained. In this case, the folded separation membrane 1 is assembled into a frame 12 equipped with a perforated plate 13 for passing pus permeated water, a water collection pipe 14, and a '0' ring groove with a reticulated spacer 2 interposed therein. By sealing between the inner side of No. 12 and the membrane body with an adhesive, the supply liquid section and the membrane permeation section can be completely separated. The frame-equipped membrane body constructed in this manner is assembled vertically, a '0' ring is inserted into the frame, and the frames are connected with bolts and nuts, and an element is formed by the assembly method in the same manner as an element composed of a single separation membrane. be done. In the same way, it is possible to increase the number of purulent bodies to form large elements, but this method has the disadvantage of complicating manufacturing management and increasing costs.

本発明に係る装置の最大の特徴は次の4点に要約される
。即ち第一に、折りたたみ長さが20〜10仇帆といっ
た比較的短いため膜透過水の集水時における通路抵抗が
渦巻型と比べ極めて少く効率的流体分離機能を有するこ
と。特に渦巻型の場合に使用する樹脂加工トリコット布
などを不要とし、材料節約及び組立の簡易化によるコス
ト減効果が大きい。第二に、分離膜の折りたたみ、絹状
スベーサ−の挿入、集水管の取付、接着剤塗布等は比較
的単純且つ簡単な作業であるので、流れ作業が可能とな
り、生産性が高い。
The most important features of the device according to the present invention can be summarized in the following four points. That is, firstly, since the folded length is relatively short, such as 20 to 10 lengths, the passage resistance during collection of membrane permeated water is much lower than that of the spiral type, and it has an efficient fluid separation function. In particular, it eliminates the need for resin-treated tricot cloth, which is used in the case of a spiral type, and has a significant cost reduction effect by saving materials and simplifying assembly. Secondly, folding the separation membrane, inserting the silk-like substrate, attaching the water collecting pipe, applying adhesive, etc. are relatively simple and easy operations, so assembly line operations are possible and productivity is high.

第三に「単位シェル容積当りの有効膜面積(膜充填密度
)は、渦巻型に比して30%程度向上する。この頃向は
ェレメントが大型になる程顕著になる。第四に、炉過膜
面をウオータージェット等により洗浄可能である。
Third, the effective membrane area per unit shell volume (membrane packing density) is improved by about 30% compared to the spiral type.This improvement becomes more noticeable as the element becomes larger.Fourth, the furnace The membrane surface can be cleaned using a water jet or the like.

以下実施例により説明する。This will be explained below using examples.

二酢酸セルロースを公知の製膜法でSamngClot
hNo.601(MillsTravis社商品名)に
流延し、Nac職E除率95.2%、透水速度1.4の
′枕日(Nacl150瓜血、圧力40k9/仇、温度
25o0流速1の/secの条件下)の性能を有する髪
打布付膜を得た。
SamngClot cellulose diacetate using a known film forming method.
hNo. 601 (trade name of Mills Travis Co.), NaCl 150%, pressure 40k9/sec, temperature 25o0, flow rate 1/sec. A membrane with a hair dressing having the performance shown in (lower) was obtained.

この分離膜を用いて、下記仕様の本発明品並びに対照品
として渦巻型ェレメントを作成し、その性能を測定した
結果を表1に示す。
Using this separation membrane, spiral-shaped elements were prepared as products of the present invention and control products having the following specifications, and their performances were measured. Table 1 shows the results.

表 1 ※ NacZ1500p「pm、圧力40Kムイでh温
度25℃、給液量20之イmin.回収率10〜15舞
この結果から本発明品は膜充填密度が大きく、膜透過水
の流路抵抗の少し、、膜性能の良好なェレメントであり
流体分離装置であることが認められる。
Table 1 * NacZ1500p pm, pressure 40K mui, h temperature 25℃, liquid supply amount 20 min. recovery rate 10-15 min. From these results, the product of the present invention has a high membrane packing density and a low flow path resistance for membrane permeated water. It is recognized that it is an element with good membrane performance and a fluid separation device.

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

第1図は本発明の実施例を示す横断面図、第2,3,4
図はェレメントを構成する分離膜と絹状スベーサーの配
列の態様を示す横断面拡大図、第5図はェレメントの耐
圧シェル内での使用態様を示す縦断面図、第6図は第5
図での横断面図、第7,8図はェレメントの変形態様の
一例を示す縦断面及び横断面図、第9図は本発明の変形
ェレメントの態様を示す横断面図、第10図は第9図の
斜視図であり、図中1は分離膜(la:膜、lb:髪打
布、lc:補強布)、2は網状スベーサー、3は膜シー
ル部、4は扇平状集水管、5はプラスチックスフイルム
、6は端末シール部、8は耐圧円筒管、10は供給液流
路、11は膜透過水、12は枠、13多孔板を示す。 婆’図 孝之図 姿3■ 群ム図 菱5函 穿る函 多7図 菱a図 姿?図 ¥′o図
Figure 1 is a cross-sectional view showing an embodiment of the present invention, Figures 2, 3, and 4
The figure is an enlarged cross-sectional view showing the arrangement of the separation membrane and silk substrate that make up the element, Figure 5 is a longitudinal cross-sectional view showing how the element is used within a pressure-resistant shell, and Figure 6 is the
7 and 8 are longitudinal and cross-sectional views showing an example of a modified element, FIG. 9 is a cross-sectional view showing an example of a modified element of the present invention, and FIG. 9 is a perspective view of FIG. 9, in which 1 is a separation membrane (LA: membrane, LB: hair cloth, LC: reinforcing cloth), 2 is a mesh baser, 3 is a membrane seal part, 4 is a fan-shaped water collection pipe, 5 is a plastic film, 6 is an end seal, 8 is a pressure-resistant cylindrical tube, 10 is a feed liquid channel, 11 is membrane permeation water, 12 is a frame, and 13 is a porous plate. Ba'zu Takayuki figure 3 ■ Gunmu figure 5 box pierced box 7 figure figure A figure? Figure¥′oFigure

Claims (1)

【特許請求の範囲】 1 精密濾過、限外濾過、逆浸透法などの流体分離装置
に於て扁平状集水管と、該扁平状集水管を中心として上
下二段に規則正しく折りたたまれ且つ端部を接着剤で重
着した一枚の分離膜又は裏打布付分離膜と、該折りたた
まれた膜の給液側に挿入された網状スペーサーと、外周
を包むプラスチツクスシート又はフイルムとから構成さ
れるエレメントと該エレメントが内接して挿入される耐
圧円筒管と、該耐圧円筒管と上記エレメントとで形成さ
れる空間を閉塞するシール材とを具備してなる液体分離
装置。 2 上記第1項記載の流体分離装置に於て、上下別々に
折りたたまれた二つの膜体と、該二つの膜体を一体的に
組立てる枠とを具備してなる流体分離装置。
[Scope of Claims] 1. In a fluid separation device such as precision filtration, ultrafiltration, or reverse osmosis, a flat water collection pipe is regularly folded into two upper and lower stages around the flat water collection pipe, and the ends thereof are An element consisting of a single separation membrane adhered with an adhesive or a separation membrane with a cloth lining, a mesh spacer inserted into the liquid supply side of the folded membrane, and a plastic sheet or film surrounding the outer periphery. A liquid separation device comprising: a pressure-resistant cylindrical tube into which the element is inserted and inscribed; and a sealing material that closes a space formed by the pressure-resistant cylindrical tube and the element. 2. The fluid separation device according to item 1 above, which comprises two membrane bodies folded up and down separately, and a frame for assembling the two membrane bodies integrally.
JP8268677A 1977-06-13 1977-07-11 fluid separation device Expired JPS6010764B2 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP8268677A JPS6010764B2 (en) 1977-07-11 1977-07-11 fluid separation device
IL7854676A IL54676A0 (en) 1977-06-13 1978-05-09 A liquid trating unit
US05/906,076 US4235722A (en) 1977-06-13 1978-05-15 Liquid treating unit
GB23000/78A GB1581122A (en) 1977-06-13 1978-05-26 Liquid treating units
DE19782825698 DE2825698A1 (en) 1977-06-13 1978-06-12 UNIT FOR THE TREATMENT OF LIQUIDS
FR7817538A FR2394318A1 (en) 1977-06-13 1978-06-12 LIQUID TREATMENT APPARATUS, OF THE PLISSED SEMI-PERMEABLE MEMBRANE TYPE

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8268677A JPS6010764B2 (en) 1977-07-11 1977-07-11 fluid separation device

Publications (2)

Publication Number Publication Date
JPS5417378A JPS5417378A (en) 1979-02-08
JPS6010764B2 true JPS6010764B2 (en) 1985-03-20

Family

ID=13781294

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8268677A Expired JPS6010764B2 (en) 1977-06-13 1977-07-11 fluid separation device

Country Status (1)

Country Link
JP (1) JPS6010764B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6248981U (en) * 1985-09-10 1987-03-26

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5652901B2 (en) * 2008-03-07 2015-01-14 住友電気工業株式会社 Separation membrane module for filtration and filtration apparatus using the separation membrane module
JP2011101864A (en) 2009-11-11 2011-05-26 Nitto Denko Corp Separation membrane unit, and separation membrane element equipped therewith

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6248981U (en) * 1985-09-10 1987-03-26

Also Published As

Publication number Publication date
JPS5417378A (en) 1979-02-08

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