JPH0366929B2 - - Google Patents
Info
- Publication number
- JPH0366929B2 JPH0366929B2 JP59010778A JP1077884A JPH0366929B2 JP H0366929 B2 JPH0366929 B2 JP H0366929B2 JP 59010778 A JP59010778 A JP 59010778A JP 1077884 A JP1077884 A JP 1077884A JP H0366929 B2 JPH0366929 B2 JP H0366929B2
- Authority
- JP
- Japan
- Prior art keywords
- semipermeable membrane
- pressure
- cylindrical
- support tube
- resistant support
- 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 - Lifetime
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/10—Supported membranes; Membrane supports
- B01D69/107—Organic support material
- B01D69/1071—Woven, non-woven or net mesh
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は透過性能が改善された円筒状半透膜モ
ジユールに関するものである。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a cylindrical semipermeable membrane module with improved permeation performance.
さらに詳しくは液体の濃縮・分離・精製法とし
て食品業界、医薬品業界などで実用化が進められ
ている半透膜を利用した逆浸透法、限外過法な
どに用いる性能が改善された半透膜モジユールに
関する。 For more details, see semi-permeable membranes with improved performance used in reverse osmosis and ultrafiltration methods using semi-permeable membranes, which are being put into practical use in the food and pharmaceutical industries as liquid concentration, separation and purification methods. Regarding membrane modules.
半透膜を用いた逆浸透法や限外過法装置の性
能を左右するポイントは半透膜の性能ならびにそ
の半透膜を取扱い易いように加工・成形したモジ
ユールとしての性能であることは言うまでもな
い。 It goes without saying that the key factors that determine the performance of reverse osmosis and ultrafiltration devices that use semipermeable membranes are the performance of the semipermeable membrane and the performance of the module that is processed and molded to make it easy to handle. stomach.
この半透膜モジユールの形式には各種のものが
あるが、前記の円筒状半透膜モジユールは懸濁物
を含んだ液体や粘度の高い液体を処理するのに適
していることはよく知られているところである。 There are various types of semipermeable membrane modules, but it is well known that the cylindrical semipermeable membrane module described above is suitable for treating liquids containing suspended substances and liquids with high viscosity. This is where I am.
(従来技術)
ところでこの円筒状半透膜モジユールは他の形
式のモジユールと比較して単位体積あたりの膜の
充填密度が低いため、設備の処理能力を増大させ
るためにはモジユールあたりの性能、とくに透過
性能を改善させることが不可欠であるが、構造が
比較的簡単であるという特長を有しているため逆
に改善の余地が殆んどないのが実情である。(Prior art) By the way, this cylindrical semipermeable membrane module has a lower membrane packing density per unit volume than other types of modules, so in order to increase the processing capacity of equipment, the performance per module, especially Although it is essential to improve the transmission performance, the fact is that there is little room for improvement because the structure is relatively simple.
例えば耐圧支持管に穿つ小孔の数を増やした
り、孔径を大きくしたり、また耐圧支持管の内部
に複数本の小溝を筋状につけたりすることが提案
されている。 For example, it has been proposed to increase the number of small holes drilled in the pressure-resistant support tube, to increase the diameter of the holes, or to form a plurality of small grooves in a line inside the pressure-resistant support tube.
(従来技術の欠点)
即ち、前記のような透過液量を増大させるため
の方法は夫々以下のような欠点を有している。(Disadvantages of Prior Art) That is, the methods for increasing the amount of permeate as described above each have the following disadvantages.
先ず耐圧支持管に穿つ小孔の数を増やす方法は
加工費用が大巾に増大する割には透過液量の増加
はわづかであり、また限外過法の場合は一般的
にプラスチツクパイプを耐圧支持管として用いて
いる場合が多いので耐圧強度の点で問題がある。 First, the method of increasing the number of small holes drilled in the pressure-resistant support tube increases the processing cost considerably, but the amount of permeate increases only slightly, and in the case of the ultrafiltration method, plastic pipes are generally used. Since it is often used as a pressure-resistant support tube, there is a problem in terms of pressure-resistant strength.
小孔の孔径を大きくする方法も透過液量の増加
がわづかであり、この小孔の部分の支持体つき半
透膜の耐圧性の点で問題がある。 The method of increasing the diameter of the small pores also results in a small increase in the amount of permeated liquid, and there is a problem in terms of pressure resistance of the semipermeable membrane with a support in the small pore area.
またパイプ内面に複数本の筋状の小溝をつける
方法は透過液量の増大には非常に有効であるが、
小孔の数を増やす方法と同様に特にプラスチツク
パイプを耐圧管として用いる限外過法の場合耐
圧強度の点でで問題がある。 Additionally, creating multiple small grooves on the inner surface of the pipe is very effective in increasing the amount of permeate;
Similar to the method of increasing the number of small holes, there is a problem in terms of pressure resistance, particularly in the case of the ultra-pass method, which uses plastic pipes as pressure-resistant tubes.
(本発明の構成)
次に本発明の構成を図面を用いて詳しく説明す
る。(Configuration of the present invention) Next, the configuration of the present invention will be explained in detail using the drawings.
第1図は従来型の何の工夫もなされていない通
常の円筒状半透膜モジユールの断面図を示したも
ので、1―1は長さ方向に一定間隔で小孔が穿孔
されたステンレス製またはプラスチツク製の耐圧
支持管で、通常は長さ1〜5m、内径10〜50mmの
ものである。2―2は耐圧支持管1―1の内面に
略ぴつたり密着する外径を有する支持体つき半透
膜の支持体であり、通常は織布または不織布が用
いられている。 Figure 1 shows a cross-sectional view of an ordinary cylindrical semipermeable membrane module with no conventional modifications, and 1-1 is made of stainless steel with small holes perforated at regular intervals in the length direction. Alternatively, it is a pressure-resistant support tube made of plastic, usually 1 to 5 m in length and 10 to 50 mm in inner diameter. Reference numeral 2-2 denotes a support for a semipermeable membrane with a support having an outer diameter that is in close contact with the inner surface of the pressure-resistant support tube 1-1, and is usually made of woven fabric or non-woven fabric.
3―3は支持体2―2上に流延されて通常は一
体化している円筒状半透膜で、4―4′は耐圧支
持管1―1の長さ方向に一定間隔で穿孔された透
過液の通路となる小孔で、通常は孔径0.5〜1mm
φで、穿孔ピツチは50〜100mm間隔である。 3-3 is a cylindrical semipermeable membrane that is cast onto the support 2-2 and is usually integrated therein, and 4-4' is perforated at regular intervals in the length direction of the pressure-resistant support tube 1-1. A small hole that serves as a passage for the permeate, usually with a pore diameter of 0.5 to 1 mm.
φ, and the perforation pitches are 50 to 100 mm apart.
これに対して第2図は本発明の円筒状半透膜モ
ジユールの断面で、5―5は耐圧支持管、6―6
は支持体つき半透膜の支持体、7―7は支持体6
―6上に流延された円筒状半透膜、8―8′は耐
圧支持管5―5に穿孔された小孔、9―9は円筒
状半透膜の支持体6―6と耐圧支持管5―5との
間にすべり込ませた耐圧支持管の長さ方向に概略
平行で、かつ、相互に連結されていない、それぞ
れが個別に連続した糸状物体で、通常は合成繊維
製のヤーンまたは紡績糸で太さは40μ〜200μ、デ
ニール表示で20〜400程度、番手表示で250〜15程
度が手項である。すべり込ませるヤーンまたは紡
績糸の本数は内径14mmφのチユーブ膜の場合で数
本〜十数本が適当である。 On the other hand, FIG. 2 is a cross section of the cylindrical semipermeable membrane module of the present invention, where 5-5 is a pressure-resistant support tube, 6-6
is a semipermeable membrane support with a support, 7-7 is a support 6
- 6 is a cylindrical semipermeable membrane cast, 8-8' is a small hole drilled in the pressure-resistant support tube 5-5, and 9-9 is a cylindrical semi-permeable membrane support 6-6 and pressure-resistant support. A filament-like object, each of which is individually continuous and is generally parallel to the length of the pressure-resistant support tube that is slid between the tube 5-5 and is not interconnected, and is usually a yarn made of synthetic fiber. Alternatively, the thickness of spun yarn is 40μ to 200μ, the denier is about 20 to 400, and the count is about 250 to 15. In the case of a tube membrane with an inner diameter of 14 mm, the appropriate number of yarns or spun threads to be slipped is from several to more than ten.
10―10は糸状物体9―9によつて円筒状半
透膜の支持体6―6と耐圧支持管5―5との間に
形成された透過液の通路となる空間である。第3
図は第2図の9―9の付近の拡大図である。 Reference numeral 10-10 is a space formed by the filamentous material 9-9 between the cylindrical semipermeable membrane support 6-6 and the pressure-resistant support tube 5-5 and serving as a passage for the permeate. Third
The figure is an enlarged view of the vicinity of 9-9 in FIG.
(本発明の効果)
第1図に示すような断面構造を有する円筒状半
透膜において半透膜3―3を透過した透過液は小
孔4―4′に集まつて外部に取り出される。この
時小孔4―4′の近くの透過液は殆んど流通抵抗
なしに流れるが、小孔4―4′から遠くの部分の
半透膜から透過した透過液は支持体の内部を浸透
していくため流通抵抗が大きくなり、充分な透過
性能が確保されない。(Effects of the Invention) In the cylindrical semipermeable membrane having a cross-sectional structure as shown in FIG. 1, the permeated liquid that has permeated the semipermeable membrane 3-3 is collected in the small holes 4-4' and taken out to the outside. At this time, the permeate near the small holes 4-4' flows with almost no flow resistance, but the permeate that permeates through the semipermeable membrane in the area far from the small holes 4-4' permeates inside the support. As a result, the flow resistance increases and sufficient permeation performance cannot be ensured.
これに対して第2図に示すような本発明に係る
円筒状膜の場合は糸状物体9―9によつて形成さ
れたわづかな空間10―10および糸状物体9―
9が半透膜を透過した液の通路となるため、透過
液が流れ易くなり、透過性能が著しく向上する。 On the other hand, in the case of the cylindrical membrane according to the present invention as shown in FIG.
Since 9 serves as a passage for the liquid that has permeated through the semi-permeable membrane, the permeated liquid can flow easily and the permeation performance is significantly improved.
次に本発明の効果を実施例と比較例に基いて説
明する。 Next, the effects of the present invention will be explained based on Examples and Comparative Examples.
実施例
耐圧支持管:日本棒管(株)製17.5φ/14.5φ、2250
硬質PVC
半透膜 :ダイセル化学(株)製ポリサルホン限
外過膜(特開昭57−94309参照)
小孔 :50mm間隔でパイプの相対する両側
に夫々45個ずつ計90個穿孔
孔径 :1mmφ
半透膜支持体と耐圧支持管との間にすべり込ま
せるヤーン:ポリエステル製、110デニール
ヤーン本数 :円周方向に等間隔に8本
性能測定条件:送水量 1m3/時間
水温 25℃
操作圧力 3Kg/cm2・G
透過性能水量 22m3/m2・日
比較例
110デニールのポリエステル製ヤーンを使用し
ないこと以外は全て実施例と同様に行ない、透過
水量12m3/m2・日という結果を得た。Example Pressure-resistant support pipe: Nippon Bokan Co., Ltd. 17.5φ/14.5φ, 2250
Hard PVC semi-permeable membrane: Polysulfone ultra-permeable membrane manufactured by Daicel Chemical Co., Ltd. (see JP-A-57-94309) Small holes: 90 holes in total, 45 perforated on opposite sides of the pipe at 50 mm intervals Hole diameter: 1 mmφ and a half Yarn to be slipped between the membrane support and the pressure-resistant support tube: Made of polyester, 110 denier Number of yarns: 8 equally spaced in the circumferential direction Performance measurement conditions: Water flow rate: 1 m 3 /hour Water temperature: 25°C Operating pressure: 3 kg /cm 2・G Permeation performance water amount 22m 3 /m 2・day Comparative example Except for not using 110 denier polyester yarn, everything was carried out in the same manner as in the example, and a permeation water amount of 12m 3 /m 2・day was obtained. Ta.
この実施例で得られた結果と比較例で得られた
結果を比較すると約8割の透過性能の増大が得ら
れ、本発明が有効であることがわかる。 Comparing the results obtained in this example with the results obtained in the comparative example, it can be seen that the transmission performance is increased by about 80%, indicating that the present invention is effective.
第1図は従来型の何の工夫も施されていない円
筒状半透膜の断面図、第2図は本発明の円筒状半
透膜の断面図、第3図は第2図の糸状物体付近の
拡大図である。
Fig. 1 is a cross-sectional view of a conventional cylindrical semipermeable membrane without any modifications, Fig. 2 is a cross-sectional view of a cylindrical semipermeable membrane of the present invention, and Fig. 3 is a filamentous object shown in Fig. 2. It is an enlarged view of the vicinity.
Claims (1)
入され、両端がシール加工された円筒状半透膜モ
ジユールにおいて、支持体つき円筒状半透膜の外
周と耐圧支持管との間の長さ方向に概略平行に、
かつ、相互に連結されていない複数本のそれぞれ
が個別に連続した糸状物体が挿入された構造を有
することを特徴とする円筒状半透膜モジユール。1 In a cylindrical semipermeable membrane module in which a cylindrical semipermeable membrane with a support is inserted into a pressure-resistant support tube and both ends are sealed, the longitudinal direction between the outer periphery of the cylindrical semipermeable membrane with a support and the pressure-resistant support tube roughly parallel to
A cylindrical semipermeable membrane module characterized in that it has a structure in which each of a plurality of unconnected threads is individually inserted with a continuous thread-like object.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59010778A JPS60153904A (en) | 1984-01-24 | 1984-01-24 | Cylindrical semipermeable membrane module improved in permeablity |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59010778A JPS60153904A (en) | 1984-01-24 | 1984-01-24 | Cylindrical semipermeable membrane module improved in permeablity |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60153904A JPS60153904A (en) | 1985-08-13 |
| JPH0366929B2 true JPH0366929B2 (en) | 1991-10-21 |
Family
ID=11759787
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59010778A Granted JPS60153904A (en) | 1984-01-24 | 1984-01-24 | Cylindrical semipermeable membrane module improved in permeablity |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60153904A (en) |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5610909U (en) * | 1979-07-06 | 1981-01-30 | ||
| AU528590B2 (en) * | 1979-09-07 | 1983-05-05 | Union Carbide Corporation | Ultrafiltration and reverse osmosis device |
| US4309287A (en) * | 1980-05-01 | 1982-01-05 | Abcor, Inc. | Reverse-osmosis tubular membrane |
| JPS58146504U (en) * | 1982-03-23 | 1983-10-01 | 日東電工株式会社 | liquid separator |
-
1984
- 1984-01-24 JP JP59010778A patent/JPS60153904A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60153904A (en) | 1985-08-13 |
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