JPH0611075Y2 - Pervaporation membrane module - Google Patents
Pervaporation membrane moduleInfo
- Publication number
- JPH0611075Y2 JPH0611075Y2 JP11984488U JP11984488U JPH0611075Y2 JP H0611075 Y2 JPH0611075 Y2 JP H0611075Y2 JP 11984488 U JP11984488 U JP 11984488U JP 11984488 U JP11984488 U JP 11984488U JP H0611075 Y2 JPH0611075 Y2 JP H0611075Y2
- Authority
- JP
- Japan
- Prior art keywords
- membrane module
- plate
- membrane
- pervaporation
- module
- 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
- 239000012528 membrane Substances 0.000 title claims description 33
- 238000005373 pervaporation Methods 0.000 title claims description 17
- 239000007788 liquid Substances 0.000 claims description 20
- 239000006185 dispersion Substances 0.000 description 4
- 238000000926 separation method Methods 0.000 description 3
- 239000004372 Polyvinyl alcohol Substances 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 229920002451 polyvinyl alcohol Polymers 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 125000006850 spacer group Chemical group 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Description
【考案の詳細な説明】 〔産業上の利用分野〕 本考案は浸透気化膜モジュールに係わり、更に詳しくは
有機液体のモジュールプレート上での良好な流動状況が
得られる浸透気化膜モジールに関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to a pervaporative membrane module, and more particularly to a pervaporative membrane module capable of obtaining a good flow state of an organic liquid on a module plate.
近年、浸透気化膜は膜の一次側に供給した液体混合物中
の特定成分を膜の二次側に浸透、気化させて蒸気状で取
り出す分離方法として注目をあびつつある。In recent years, pervaporation membranes have been attracting attention as a separation method in which a specific component in a liquid mixture supplied to the primary side of a membrane permeates to the secondary side of the membrane, is vaporized, and is taken out in a vapor state.
そして、浸透気化膜の実際上の使用に際しては、膜を支
持すると共に膜に強度を与えるために、例えば第3図に
示すような浸透気化膜モジュールが製造されている。When the pervaporation membrane is actually used, for example, a pervaporation membrane module as shown in FIG. 3 is manufactured in order to support the membrane and give strength to the membrane.
即ち、第3図には薄層平板型膜モジュールが示されてお
り、図中1,1がセルプレートでこれ等セルプレート
1,1上にはセルガスケット2,2を介して活性層がポ
リビニルアルコール等からなる浸透気化膜3,3が配置
されている。これ等浸透気化膜3,3の外側に多孔板
4,4がそれぞれ積層され、更に最外側には金網5,5
が積層されている。なお、図中6,6は分散板、7,7
は分散バッフル、8,8はゴムリングで、9はエンドプ
レートである。That is, FIG. 3 shows a thin flat plate type membrane module, in which 1,1 is a cell plate, and the active layer is polyvinyl alcohol on these cell plates 1,1 via cell gaskets 2,2. Pervaporation membranes 3 made of alcohol or the like are arranged. Perforated plates 4 and 4 are laminated on the outer sides of these pervaporation membranes 3 and 3, and wire meshes 5 and 5 are further arranged on the outermost sides.
Are stacked. In the figure, 6 and 6 are dispersion plates and 7, 7
Is a dispersion baffle, 8 and 8 are rubber rings, and 9 is an end plate.
従って、図中に矢印で示したように、浸透気化膜3,3
の一次側に供給された有機液体は、その特定成分が浸透
気化膜3,3を経て減圧に保持されている浸透気化膜
3,3の二次側に浸透、気化して適宜の手段により外部
に取り出される。一方、特定成分が除去された残余の有
機液体は矢印方向に沿ってエンドプレート9の出口9a
より排出される。Therefore, as shown by the arrows in the figure, the pervaporation membranes 3, 3
The specific component of the organic liquid supplied to the primary side of the permeation vaporizes into the secondary side of the pervaporation membranes 3 and 3 where the specific components pass through the pervaporation membranes 3 and 3 and is kept at a reduced pressure, and is externalized by an appropriate means. Taken out. On the other hand, the remaining organic liquid from which the specific component has been removed is discharged from the outlet 9a of the end plate 9 along the arrow direction.
More discharged.
ところが、上記したような従来の膜モジールは、薄層流
路構造で流路構造が単純なため、第4図に矢印で示した
ように、セルプレート1,1上での液流れは、液入口1
a,1aから液流出口1b,1bへとショートパスし、そのま
わりに大きな死水域が生じると共に浸透気化膜3,3膜
面と液バルク7との間の温度差が大きくなって、分離性
能の低下をきたすという問題点があった。また、薄層の
ため、プラント停止時或いは膜モジュールの運搬・取付
け時等において、浸透気化膜3,3の活性層がセルプレ
ート1,1と付着し、膜破損が生じるという虞れもあっ
た。However, since the conventional membrane module as described above has a thin layer channel structure and a simple channel structure, the liquid flow on the cell plates 1 and 1 is as shown by the arrow in FIG. Entrance 1
Short pass from a, 1a to the liquid outlets 1b, 1b, a large dead water area is generated around them, and the temperature difference between the pervaporation membranes 3, 3 membrane and the liquid bulk 7 becomes large, and the separation performance is increased. However, there was a problem in that Further, because of the thin layer, there is a possibility that the active layer of the pervaporation membranes 3, 3 may adhere to the cell plates 1, 1 when the plant is stopped or the membrane module is transported or attached, resulting in membrane damage. .
本考案は上記従来の問題点を解消するためになされたも
のであり、有機液体のモジュールプレート上での良好な
流動状況が得られる浸透気化膜モジュールを提供するこ
とを目的とする。The present invention has been made in order to solve the above-mentioned conventional problems, and an object thereof is to provide a pervaporation membrane module that can obtain a good flow state of an organic liquid on a module plate.
上記目的を達成するために、本考案に係る浸透気化膜モ
ジュールは、モジュールプレートの上面に液流分散用の
複数のせき板を液流れ方向に多段的に配設したことを特
徴とする。In order to achieve the above object, the pervaporation membrane module according to the present invention is characterized in that a plurality of weir plates for liquid flow dispersion are arranged in multiple stages in the liquid flow direction on the upper surface of the module plate.
上記構成によれば、液入口からの有機液体は、せき板に
よりモジュールプレート上面の略全域に亘って均一に分
散して流動した後液体出口へと至る。According to the above configuration, the organic liquid from the liquid inlet reaches the liquid outlet after being evenly dispersed and flowed over substantially the entire area of the upper surface of the module plate by the weir plate.
以下添付図面に基づいて、本考案膜モジールの一実施例
を説明する。An embodiment of the membrane module of the present invention will be described below with reference to the accompanying drawings.
第1図において、1は略正方形のセルプレート、2はセ
ルガスケットで、第3図及び第4図と同様である。In FIG. 1, 1 is a substantially square cell plate and 2 is a cell gasket, which is the same as in FIGS. 3 and 4.
上記セルプレート1の上面には液流分散用の複数のせき
板10…が、液入口1aから液流出口1bへ向けて多段的
に配設されている。On the upper surface of the cell plate 1, a plurality of dam plates 10 for liquid flow dispersion are arranged in multiple stages from the liquid inlet 1a to the liquid outlet 1b.
上記せき板10…はセルプレート1上面の外周部を除く内
側寄りに設けられているとともに、第2図に示すよう
に、浸透気化膜3の膜面との間に所定の間隙が形成され
るようその高さが設定される。また、せき板10…は、平
板なセルプレート1とは別体に形成されて適宜の手段に
よりセルプレート1上面に固設されるとともに、その材
料としては、浸透気化膜3と付着し難いもの例えば活性
層がポリビニルアルコールであれば表面がテフロン加工
されたものが選択される。The barrier plates 10 are provided on the inner side of the upper surface of the cell plate 1 excluding the outer peripheral portion thereof, and as shown in FIG. 2, a predetermined gap is formed between the barrier plate 10 and the membrane surface of the pervaporation membrane 3. The height is set so that Further, the weirs 10 ... Are formed separately from the flat cell plate 1 and fixed to the upper surface of the cell plate 1 by an appropriate means, and the material thereof is one that is difficult to adhere to the pervaporation film 3. For example, if the active layer is polyvinyl alcohol, the surface of which is treated with Teflon is selected.
その他の構成は第3図及び第4図と同様なので、第3図
及び第4図を参照してここでは詳しい説明は省略する。Other configurations are the same as those in FIGS. 3 and 4, so detailed description will be omitted here with reference to FIGS. 3 and 4.
このように本実施例では、せき板10…とセルプレート1
とを別体に形成するようにしたので、特にセルプレート
1の平滑度を出し易く、強いては多層型の膜モジュール
を精度良く簡単に製作できるという利点がある。As described above, in this embodiment, the weirs 10 ...
Since they are formed separately, there is an advantage that the smoothness of the cell plate 1 can be easily obtained, and in particular, a multi-layer type membrane module can be manufactured accurately and easily.
以上説明したように本考案によれば、モジュールプレー
トの上面に液流分散用の複数のせき板を液流れ方向に多
段的に配設するようにしたので、液流をプレート上面の
略全域へ均一に分散でき、よって膜垂直方向の大きな温
度歪も回避して分離性能の向上が図れる。また、上記き
せ板はプレート上面と膜面とのスペーサの役割も奏する
ので、プラント停止時等において膜の活性層がプレート
上面に付着して膜破損が生じるということもない。As described above, according to the present invention, the plurality of dam plates for distributing the liquid flow are arranged on the upper surface of the module plate in multiple stages in the liquid flow direction. It is possible to disperse evenly, and thus a large temperature strain in the vertical direction of the membrane can be avoided to improve the separation performance. Further, since the above-mentioned baffle plate also serves as a spacer between the plate upper surface and the film surface, the active layer of the film does not adhere to the plate upper surface and the film is not damaged when the plant is stopped.
第1図は本考案膜モジュール一実施例を示す要部平面
図、第2図はその要部側断面図である。第3図は従来の
膜モジュールの側断面図、第4図はその要部平面図であ
る。 1…セルプレート、2…セルガスケット、3…浸透気化
膜、10…せき板。FIG. 1 is a plan view of an essential part showing an embodiment of the membrane module of the present invention, and FIG. 2 is a sectional side view of the essential part. FIG. 3 is a side sectional view of a conventional membrane module, and FIG. 4 is a plan view of a main part thereof. 1 ... cell plate, 2 ... cell gasket, 3 ... pervaporation membrane, 10 ... weir.
Claims (1)
の複数のせき板を液流れ方向に多段的に配設したことを
特徴とする浸透気化膜モジュール。1. A pervaporation membrane module, wherein a plurality of weir plates for dispersing a liquid flow are arranged on the upper surface of a module plate in multiple stages in the liquid flow direction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11984488U JPH0611075Y2 (en) | 1988-09-14 | 1988-09-14 | Pervaporation membrane module |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11984488U JPH0611075Y2 (en) | 1988-09-14 | 1988-09-14 | Pervaporation membrane module |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0240427U JPH0240427U (en) | 1990-03-19 |
| JPH0611075Y2 true JPH0611075Y2 (en) | 1994-03-23 |
Family
ID=31365430
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11984488U Expired - Lifetime JPH0611075Y2 (en) | 1988-09-14 | 1988-09-14 | Pervaporation membrane module |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0611075Y2 (en) |
-
1988
- 1988-09-14 JP JP11984488U patent/JPH0611075Y2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0240427U (en) | 1990-03-19 |
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