JPH0646497Y2 - External heat exchange type liquid mixture separation module - Google Patents
External heat exchange type liquid mixture separation moduleInfo
- Publication number
- JPH0646497Y2 JPH0646497Y2 JP1988106327U JP10632788U JPH0646497Y2 JP H0646497 Y2 JPH0646497 Y2 JP H0646497Y2 JP 1988106327 U JP1988106327 U JP 1988106327U JP 10632788 U JP10632788 U JP 10632788U JP H0646497 Y2 JPH0646497 Y2 JP H0646497Y2
- Authority
- JP
- Japan
- Prior art keywords
- liquid mixture
- module
- heat exchange
- exchange type
- external heat
- 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
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Description
【考案の詳細な説明】 〔産業上の利用分野〕 本考案浸透気化法による液体混合物の分離に供するため
のは外部熱交換型液体混合物分離用モジユールに関す
る。さらに詳しくは、流体の出入口を有し、中空糸束が
内蔵された浸透気化法による液体混合物の分離に供する
ための液体混合物分離用モジユールにおいて、筐体の外
側に与熱用のジヤケツトを有する外部熱交換型の液体混
合物分離用モジユールに関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to an external heat exchange type liquid mixture separating module for separating a liquid mixture by a pervaporation method. More specifically, in a liquid mixture separating module having a fluid inlet / outlet and having a hollow fiber bundle incorporated therein for separating a liquid mixture by a pervaporation method, an outer casing having a heating jacket is provided on the outside. The present invention relates to a heat exchange type liquid mixture separating module.
分離膜を隔てて一次側(フイード側)に混合液体を供給
し、二次側(透過側)を減圧にするか、又はキヤリヤー
ガスを流して分離すべき物質を気体状で透過させるいわ
ゆる浸透気化分離法が1950年頃から研究されている。浸
透気化分離法は通常の蒸留では分離が不可能または困難
な共沸混合物や沸点差の小さい混合物の分離に適した方
法とされているが、未だ広く工業的に利用されるに至つ
ていない。これは主として膜の透過性、即ち分離係数及
び膜透過速度が大きくないことに原因があり、これら膜
の透過性をあげるべく種々検討がなされている。(例え
ば、特開昭62-186907号、62-210008号、62-250906号、6
3-7803号、63-12304号、63-28409号、63-44904号公報
等)。A so-called pervaporation separation in which a mixed liquid is supplied to the primary side (feed side) across a separation membrane and the secondary side (permeation side) is depressurized, or a carrier gas is flowed to permeate the substance to be separated in a gaseous state. The law has been studied since about 1950. Although the pervaporation separation method is considered to be suitable for separating azeotropic mixtures or mixtures with small boiling points that are difficult or difficult to separate by ordinary distillation, it has not yet been widely used industrially. . This is mainly due to the fact that the permeability of the membrane, that is, the separation coefficient and the membrane permeation rate are not large. (For example, JP-A-62-186907, 62-210008, 62-250906, 6
3-7803, 63-12304, 63-28409, 63-44904, etc.).
〔考案が解決しようとする課題〕 浸透気化分離法は、液体から気体への相変化を必ず伴う
分離法であり、この相変化に要する熱量は供給される混
合液体の顕熱によつてまかなわれている。従つて、混合
液体を通常の浸透気化分離方法によつて分離すると、分
離装置内の液温度は逐次低下し、膜を透過する量が多い
程、その温度低下は顕著になる。浸透気化分離法におい
て膜分離性能に与ぼす温度の効果は大きく、浸透気化分
離法を工業的に利用するためには膜自体の改良のみでは
不充分であり、モジユール自体の改良をも併せ検討する
ことが重要である。[Problems to be solved by the device] The pervaporative separation method is a separation method that necessarily involves a phase change from liquid to gas, and the amount of heat required for this phase change is covered by the sensible heat of the supplied mixed liquid. ing. Therefore, when the mixed liquid is separated by the usual pervaporation separation method, the temperature of the liquid in the separation device is gradually decreased, and the larger the amount of permeation through the membrane, the more remarkable the temperature decrease. The effect of temperature on the membrane separation performance in the pervaporation separation method is large, and improvement of the membrane itself is not sufficient for industrial application of the pervaporation separation method, and improvement of the module itself is also studied. It is important to.
しかしながら、前述のような重要性が指摘されているに
もかかわらず浸透気化分離法において、かかる寒天から
モジユール自体の検討がなされた例はほとんどない。従
つて、本考案の目的は、浸透気化法による液体混合物の
分離に供するための分離効率のよい液体混合物分離用モ
ジユールを提供することにある。However, in spite of the above-mentioned importance being pointed out, in the pervaporation separation method, there are few cases where the module itself has been examined from such agar. Therefore, an object of the present invention is to provide a module for separating a liquid mixture with high separation efficiency for use in separating a liquid mixture by pervaporation.
本考案者は、上記課題を解決すべく上記液体混合物分離
用モジユールについて検討し、本考案に至つた。すなわ
ち本考案は、流体の出入口を有し、中空糸束が内蔵され
た浸透気化法による液体混合物の分離に供するための液
体混合物分離用モジユールにおいて、筐体の外側に与熱
用のジヤケツトを有することを特徴とする外部熱交換型
液体混合物分離用モジユールである。The inventor of the present invention has studied the above-mentioned module for separating a liquid mixture to solve the above problems, and arrived at the present invention. That is, the present invention is a module for separating a liquid mixture, which has a fluid inlet / outlet and is provided with a hollow fiber bundle for separation of a liquid mixture by a pervaporation method, and has a heating jacket on the outside of the housing. An external heat exchange type liquid mixture separating module characterized by the above.
以下、図面に従つて本考案を説明する。第1図は本考案
の液体混合分離用モジユールの概略図であり、第2図は
本考案の別の態様を示す概略図である。1は被処理流体
入口、2又は11は膜透過流体出口、3は膜非透過流体出
口、4は与熱用流体入口又は出口、5は与熱用流体出口
又は入口、6はジヤケツト、7は中空糸束、8は固定用
フランジ、9はバンドルシート、10は中空糸束端部の支
持部材である。2又は11は通常、冷却器を通して真空ラ
インに連結される。The present invention will be described below with reference to the drawings. FIG. 1 is a schematic view of a liquid mixing and separating module of the present invention, and FIG. 2 is a schematic view showing another embodiment of the present invention. 1 is a fluid inlet to be treated, 2 or 11 is a membrane permeating fluid outlet, 3 is a membrane non-permeating fluid outlet, 4 is a heating fluid inlet or outlet, 5 is a heating fluid outlet or inlet, 6 is a jacket, and 7 is A hollow fiber bundle, 8 is a fixing flange, 9 is a bundle sheet, and 10 is a supporting member at the end of the hollow fiber bundle. 2 or 11 is usually connected to a vacuum line through a cooler.
本考案の液体混合物分離用モジユールに内蔵される中空
糸束を構成する中空糸としては通常用いられる例えばセ
ルロース系、セルロースアセテート系、ポリビニルアル
コール系、ポリアクリロニトリル系、ポリスルホン系、
ポリプロピレン系等の素材からなる中空糸が使用され
る。中空糸束の開口端部はエポキシ樹脂、不飽和エポキ
シ樹脂、ウレタン樹脂、シリコーン樹脂等のポツテンイ
グ材からなる支持部材により支持され、モジユール内に
収容される。The hollow fibers that constitute the hollow fiber bundle contained in the liquid mixture separating module of the present invention are commonly used, for example, cellulose-based, cellulose acetate-based, polyvinyl alcohol-based, polyacrylonitrile-based, polysulfone-based,
A hollow fiber made of a material such as polypropylene is used. The open end of the hollow fiber bundle is supported by a support member made of a potting material such as epoxy resin, unsaturated epoxy resin, urethane resin, or silicone resin, and is housed in the module.
中空糸束をモジユール内に固定するには、このようなポ
ツテイング材で中空糸束を形成し、例えば、図面に示す
ように、フランジを用いてバンドルシートにボルト、ナ
ツト等の固定具により固定すればよい。中空糸束の開口
端部は一端開口端でもよいし、両端開口端でもよい。In order to fix the hollow fiber bundle in the module, the hollow fiber bundle is formed with such a potting material and, for example, as shown in the drawing, it is fixed to the bundle sheet with a fixture such as a bolt or nut as shown in the drawing. Good. The open end of the hollow fiber bundle may be open at one end or open at both ends.
本考案においては筐体の外側にジヤケツトを有すること
が重要である。ジヤケツトには通常、スチーム、熱水、
オイル等の熱媒を流し、被処理流体に与熱することによ
りモジユール内の温度低下を防ぎ、効率よく液体混合物
の分離を行うが、ジヤケツトに温水や冷水等を流して分
離を調節することは自由である。ジヤケツトはモジユー
ル筐体の外側に設けられたものであれば形式にはとくに
制限はない。一例としては第1図に示すように単純なジ
ヤケツトを筐体の外側に設けたものや、第2図に示すよ
うに蛇管型のジヤケツトを設けたもの等があげられる。In the present invention, it is important to have a jacket on the outside of the housing. Normally, steam, hot water,
By flowing a heat medium such as oil and applying heat to the fluid to be treated, the temperature inside the module is prevented from decreasing and the liquid mixture is separated efficiently. Be free. The type of the jacket is not particularly limited as long as it is provided on the outside of the module housing. As an example, as shown in FIG. 1, a simple jacket is provided on the outside of the housing, and as shown in FIG. 2, a flexible jacket is provided.
モジユールやジヤケツトの材質はとくに限定なく、接触
する流体に浸されない材質を適宜選択して使用すればよ
い。The material of the module or the jacket is not particularly limited, and a material that is not soaked in the fluid in contact may be appropriately selected and used.
被処理流体は有機液体水溶液が多いが、有機液体混合物
やこれらが複数混合された液体混合物の場合も処理され
る。The fluid to be processed is often an organic liquid aqueous solution, but an organic liquid mixture or a liquid mixture in which a plurality of these are mixed is also processed.
本考案の液体混合物分離用モジユールにおいて、内部に
邪魔板を入れたり、種々の工夫によつて流体の流動をよ
くするのが好ましい。In the liquid mixture separating module of the present invention, it is preferable to put a baffle inside and to improve the fluid flow by various means.
本考案のモジユールを用いて液体混合物の分離を行うに
は、ジヤケツトに予め与熱用流体を流して所望の温度に
セツトしておき、被処理流体を通じ、透過側を真空ポン
プ等で規定の圧力に制御して実施すればよい。本考案の
ジヤケツト式モジユールは熱効率の点からとくに膜面積
が5m2以下の場合に好ましく使用される。In order to separate a liquid mixture using the module of the present invention, a heating fluid is made to flow in a jacket and set to a desired temperature in advance. It may be carried out under control. The jacket type module of the present invention is preferably used when the membrane area is 5 m 2 or less from the viewpoint of thermal efficiency.
本考案により、筐体の外側に与熱用ジヤケツトを有する
浸透気化法による液体混合物の分離に供するためのモジ
ユールを提供することができる。このようなモジユール
を用いて浸透気化分離法により液体混合物の分離を行う
と、実質的な等温操作が可能であり、効率よく液体混合
物を分離することができるので工業上の有用性が大き
い。According to the present invention, it is possible to provide a module for separating a liquid mixture by a pervaporation method having a heating jacket on the outside of the housing. When the liquid mixture is separated by the pervaporation separation method using such a module, a substantially isothermal operation can be performed, and the liquid mixture can be efficiently separated, which is industrially useful.
第1図は本考案の浸透気化用モジユールの一例を示す概
略図であり、第2図は別の態様を示す概略図である。 1.……被処理流体入口 2.11.……膜透過物出口 3.……膜非透過物出口 4.……与熱用流体入(出)口 5.……与熱用流体(入)出口 6.……ジヤケツト 7.……中空糸束 8.……固定用フランジ 9.……バンドルシート 10.……支持部材FIG. 1 is a schematic view showing an example of the pervaporative module of the present invention, and FIG. 2 is a schematic view showing another embodiment. 1. …… Injected fluid inlet 2.11. …… Membrane permeate outlet 3. …… Membrane non-permeate outlet 4. …… Heating fluid inlet (outlet) 5. …… Heating fluid (inlet) outlet 6. …… Jacket 7. …… Hollow fiber bundle 8. …… Fixing flange 9. …… Bundle sheet 10. …… Supporting member
Claims (1)
た浸透気化法による液体混合物の分離に供するためのモ
ジユールにおいて、筐体の外側に与熱用のジヤケツトを
有することを特徴とする外部熱交換型液体混合物分離用
モジユール。1. A module for separating a liquid mixture by a pervaporation method, which has a fluid inlet / outlet and a hollow fiber bundle is built-in, wherein a jacket for heating is provided outside the housing. External heat exchange type liquid mixture separation module.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1988106327U JPH0646497Y2 (en) | 1988-08-10 | 1988-08-10 | External heat exchange type liquid mixture separation module |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1988106327U JPH0646497Y2 (en) | 1988-08-10 | 1988-08-10 | External heat exchange type liquid mixture separation module |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0228720U JPH0228720U (en) | 1990-02-23 |
| JPH0646497Y2 true JPH0646497Y2 (en) | 1994-11-30 |
Family
ID=31339733
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1988106327U Expired - Lifetime JPH0646497Y2 (en) | 1988-08-10 | 1988-08-10 | External heat exchange type liquid mixture separation module |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0646497Y2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009066519A (en) * | 2007-09-13 | 2009-04-02 | Kiriyama Seisakusho:Kk | Separator employing distillation and membrane separation in combination |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2327106A1 (en) * | 1973-04-30 | 1974-11-21 | Charles William Skarstrom | METHOD AND DEVICE FOR SEPARATING INDIVIDUAL COMPONENTS FROM A FLOW MIXTURE |
-
1988
- 1988-08-10 JP JP1988106327U patent/JPH0646497Y2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0228720U (en) | 1990-02-23 |
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