JPH05168874A - Leak detection for pervaporation - Google Patents

Leak detection for pervaporation

Info

Publication number
JPH05168874A
JPH05168874A JP34259191A JP34259191A JPH05168874A JP H05168874 A JPH05168874 A JP H05168874A JP 34259191 A JP34259191 A JP 34259191A JP 34259191 A JP34259191 A JP 34259191A JP H05168874 A JPH05168874 A JP H05168874A
Authority
JP
Japan
Prior art keywords
water
liquid
separation membrane
leak
reduced pressure
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
JP34259191A
Other languages
Japanese (ja)
Other versions
JP3095496B2 (en
Inventor
Taro Kobayashi
太郎 小林
Takashi Deo
隆志 出尾
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.)
Tokuyama Corp
Original Assignee
Tokuyama Corp
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 Tokuyama Corp filed Critical Tokuyama Corp
Priority to JP03342591A priority Critical patent/JP3095496B2/en
Publication of JPH05168874A publication Critical patent/JPH05168874A/en
Application granted granted Critical
Publication of JP3095496B2 publication Critical patent/JP3095496B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To promptly detect the leak of supply liquid from the liquid supply side to the reduced pressure side in a pervaporation method by measuring the temp. of permeated vapor. CONSTITUTION:In a pervaporation method (permeation vaporization method) wherein, by reducing the pressure on one side of a separation membrane and supplying a liquid mixture (water/alcohol, water/isopropylalcohol, water/ allylalcohol, etc.) to on the other side, priority is given to passing of a specified component through the separation membrane to separate (concentrate) the component, when the leak of the liquid mixture due to pinholes, rupture, etc., of the separation membrane to the reduced pressure side is detected, the temp. of permeated vapor is measured on the reduced pressure side to detect the leak of the liquid mixture to the reduced pressure side from the change of the permeated vapor temp. Thereby the leak of the liquid mixture is promptly detected and the reliability of separation treatment is improved.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、液体混合物から特定の
液体成分の分離を行うパーベーパレーション法(浸透気
化法)において、給液側から減圧側への供給液の漏洩を
検出する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for detecting leakage of a supply liquid from a supply liquid side to a decompression side in a pervaporation method (pervaporation method) for separating a specific liquid component from a liquid mixture. ..

【0002】[0002]

【従来の技術】有機液体混合物あるいは水と有機液体の
混合物等、特に沸点近接化合物、共沸混合物から特定の
液体成分を濃縮する有効な技術として、パーベーパレー
ション法が知られている。
2. Description of the Related Art A pervaporation method is known as an effective technique for concentrating a specific liquid component from an organic liquid mixture or a mixture of water and an organic liquid, especially a compound having a boiling point close to it, or an azeotropic mixture.

【0003】パーベーパレーション法は分離膜の片側を
減圧にし、反対側に液体混合物を供給することにより特
定の液体成分のみを優先的に分離膜内を通過させて分離
する方法である。従って、分離膜のピンホールや破断、
或いは分離膜とその固定手段との間に亀裂が発生した場
合には、液体混合物が減圧側に漏洩し、特定の液体成分
のみの分離が十分に行えないという問題が発生する。
The pervaporation method is a method in which one side of a separation membrane is decompressed and a liquid mixture is supplied to the other side so that only a specific liquid component is preferentially passed through the separation membrane for separation. Therefore, pinholes and breaks in the separation membrane,
Alternatively, when a crack occurs between the separation membrane and the fixing means, the liquid mixture leaks to the decompression side, and there is a problem that only a specific liquid component cannot be sufficiently separated.

【0004】[0004]

【発明が解決しようとする課題】分離膜を用いたパーベ
ーパレーション装置の組立て後には、加圧試験或いは減
圧試験を行うことによって、分離膜のピンホール、破断
等を発見することが可能である。一方、パーベーパレー
ション装置の運転中に発生する分離膜のピンホールや破
断は、現在のところ、透過液量の増加、透過液濃度の減
少、或いは、減圧側の真空度の悪化により検出されてい
る。
After assembling the pervaporation apparatus using the separation membrane, it is possible to find pinholes, breakages, etc. of the separation membrane by performing a pressure test or a pressure reduction test. .. On the other hand, pinholes and breakage of the separation membrane that occur during the operation of the pervaporation device are currently detected due to an increase in the amount of permeate, a decrease in the concentration of permeate, or a deterioration in the degree of vacuum on the pressure reducing side. There is.

【0005】しかしながら、上記した透過液量の増加、
及び透過液濃度の減少という現象は、分離膜のピンホー
ル発生後、すぐには現れないため、発見が遅れるという
問題がある。また、減圧側の真空度の悪化という現象
は、パーベーパレーション装置の減圧側の容積が大きい
場合には顕著に現れないために、分離膜のピンホール発
生の検出手段としてはあまり適当でない。
However, the above-mentioned increase in the amount of permeated liquid,
The phenomenon that the concentration of permeated liquid and the concentration of permeate do not decrease does not appear immediately after the occurrence of pinholes in the separation membrane, so that there is a problem that the discovery is delayed. Further, the phenomenon that the degree of vacuum on the depressurization side deteriorates does not appear prominently when the volume on the depressurization side of the pervaporation apparatus is large, so it is not suitable as a means for detecting the occurrence of pinholes in the separation membrane.

【0006】このため、分離膜のピンホール、破断等に
より、液体混合物が減圧側へ漏洩するのをいち早く検出
する方法が望まれていた。
For this reason, there has been a demand for a method of quickly detecting the leakage of the liquid mixture to the depressurization side due to pinholes, breakage, etc. of the separation membrane.

【0007】[0007]

【課題を解決するための手段】本発明者らは、上記の問
題を解決するために種々検討した結果、減圧側において
透過蒸気温度の変化が、液体混合物の減圧側への漏洩現
象検出の指標になり得ることを見出し、本発明を提案す
るに到った。
As a result of various studies to solve the above problems, the inventors of the present invention have found that a change in permeated vapor temperature on the reduced pressure side is an index for detecting a leakage phenomenon of a liquid mixture to the reduced pressure side. Therefore, they have come to propose the present invention.

【0008】即ち、本発明はパーベーパレーション法に
おいて、透過蒸気温度を測定することにより給液側から
減圧側への供給液の漏洩を検知することを特徴とするパ
ーベーパレーション法の漏洩検出方法である。
That is, according to the present invention, in the pervaporation method, the leak detection method of the pervaporation method is characterized by detecting the leakage of the supply liquid from the supply liquid side to the decompression side by measuring the permeated vapor temperature. Is.

【0009】本発明のパーベーパレーション法に用いる
分離膜は、公知のものを何ら制限なく用いることがで
き、例えば、セルロース、ポリビニルアルコール、ポリ
アミド、ポリエステル、ポリスルホン、ポリカーボネー
ト、ポリイミド、キトサンなどのポリマー等を挙げるこ
とができる。分離膜の形状は、例えば、平膜を積層した
プレートアンドフレーム型、スパイラル型、中空糸をポ
ッテイングしたモジュール型などをあげることができる
がこれらに限られるものではない。
As the separation membrane used in the pervaporation method of the present invention, known separation membranes can be used without any limitation. Examples thereof include polymers such as cellulose, polyvinyl alcohol, polyamide, polyester, polysulfone, polycarbonate, polyimide and chitosan. Can be mentioned. Examples of the shape of the separation membrane include, but are not limited to, a plate-and-frame type in which flat membranes are laminated, a spiral type, and a module type in which hollow fibers are potted.

【0010】また、パーベーパレーション法により分離
される液体混合物は、有機液体混合物あるいは水と有機
液体の混合物等が何ら制限なく用いられる。具体的には
水/エチルアルコール、水/イソプロピルアルコール、
水/n−プロピルアルコール、水/アリルアルコール、
水/2,3−ジクロロ−1−プロパノール、水/2−メ
トキシエタノール、水/イソブチルアルコール、水/1
−ブタノール、水/2−ブタノール、水/フルフリルア
ルコール、水/ペンタノール、水/2−ペンタノール、
水/4−メチル−1−ブタノールなどの水/アルコール
系混合物:水/テトラヒドロフラン、水/メチルエチル
ケトンなどをあげることができる。
As the liquid mixture separated by the pervaporation method, an organic liquid mixture or a mixture of water and an organic liquid can be used without any limitation. Specifically, water / ethyl alcohol, water / isopropyl alcohol,
Water / n-propyl alcohol, water / allyl alcohol,
Water / 2,3-dichloro-1-propanol, water / 2-methoxyethanol, water / isobutyl alcohol, water / 1
-Butanol, water / 2-butanol, water / furfuryl alcohol, water / pentanol, water / 2-pentanol,
Water / water / alcohol-based mixture such as 4-methyl-1-butanol: water / tetrahydrofuran, water / methyl ethyl ketone, and the like.

【0011】本発明における給液側から減圧側への供給
液の漏洩は、主として分離膜から生じるものである。漏
洩箇所の形態は、ピンホール状、シミ状、裂けているも
の等がある。分離膜がガスケット等でプレスされている
平膜状のものは、ガスケットのシール面から発生する漏
洩もあり、また、接着剤によりポッティングされている
中空糸膜状のものは接着剤で固着された部分からの漏洩
もある。
The leakage of the supply liquid from the supply liquid side to the decompression side in the present invention mainly occurs from the separation membrane. There are pinholes, spots, cracks, and the like in the form of leakage points. The flat membrane-like one in which the separation membrane is pressed with a gasket or the like has leakage that occurs from the sealing surface of the gasket, and the hollow fiber membrane-like one that is potted with an adhesive is fixed with an adhesive. There is also a leak from the part.

【0012】本発明においては、透過蒸気の温度を測定
することにより、供給液の漏洩を即時に発見することが
可能である。一般的に透過蒸気温度は供給される液温か
ら分離膜上での蒸気に消費される潜熱を引いた値にな
る。本発明者らは、分離膜が漏洩を生じた時は透過する
液量が著しく多くなることに着目して実験を繰返した結
果、漏洩した液が減圧側で蒸発する時に非常に多くの熱
量を消費するため透過蒸気温度が極端に下がるという現
象を見出した。そのため透過蒸気温度を測定することに
より分離膜の漏洩を容易にみつけ得る。ここで透過蒸気
温度は、分離膜種、供給液濃度、供給液温度が異なれば
当然変化するが、これらの条件が一定である定常状態の
運転時には透過蒸気量は常に一定であるため、透過蒸気
温度は必ず一定になる。したがって、定常運転時の一定
温度よりも透過蒸気温度が低下したことにより、供給液
の漏洩を発見することができる。
In the present invention, it is possible to immediately detect the leakage of the feed liquid by measuring the temperature of the permeated vapor. Generally, the permeated vapor temperature is a value obtained by subtracting the latent heat consumed by the vapor on the separation membrane from the temperature of the supplied liquid. The inventors of the present invention have repeated the experiment by paying attention to the fact that the amount of liquid that permeates when the separation membrane leaks is remarkably large, and as a result, a very large amount of heat is generated when the leaked liquid evaporates on the reduced pressure side. It was discovered that the permeated vapor temperature drops extremely as it is consumed. Therefore, the leakage of the separation membrane can be easily found by measuring the permeated vapor temperature. Here, the permeated vapor temperature naturally changes when the separation membrane type, the feed liquid concentration, and the feed liquid temperature differ, but the permeated vapor amount is always constant during steady-state operation where these conditions are constant, so the permeated vapor temperature is The temperature is always constant. Therefore, it is possible to detect the leakage of the supply liquid because the permeated vapor temperature is lower than the constant temperature during the steady operation.

【0013】混合液体の漏洩時の透過蒸気温度の低下巾
は、上記した運転条件によって異なるが、一般には5℃
以上の低下巾のときには、混合液体の漏洩が生じている
と判断できる。
The range of decrease in the permeated vapor temperature when the mixed liquid leaks varies depending on the above operating conditions, but is generally 5 ° C.
It can be determined that the leakage of the mixed liquid has occurred when the width of the decrease is within the above range.

【0014】本発明において、透過蒸気温度は分離膜の
減圧側の温度である。この温度は分離膜、液体混合物に
より異なるが、一般には供給液温度より幾分低い温度で
ある。透過蒸気温度の測定場所としては、外部からの伝
熱の影響を受けにくい分離膜近傍が好ましい。
In the present invention, the permeated vapor temperature is the temperature on the reduced pressure side of the separation membrane. This temperature varies depending on the separation membrane and the liquid mixture, but is generally somewhat lower than the temperature of the feed liquid. The location for measuring the temperature of the permeated vapor is preferably near the separation membrane, which is less susceptible to heat transfer from the outside.

【0015】[0015]

【効果】本発明のパーベーパレーション法の漏洩検出方
法によれば、分離膜種、供給液濃度、供給液温度等に関
係なく分離膜及びその周辺に発生した漏洩を検知するこ
とができる。従って、漏洩が発生した時には即座に分離
を中止して、漏洩箇所をみつけて修理することが可能で
ある。
According to the leakage detection method of the pervaporation method of the present invention, it is possible to detect the leakage that has occurred in the separation membrane and its surroundings irrespective of the separation membrane species, the supply liquid concentration, the supply liquid temperature and the like. Therefore, when a leak occurs, it is possible to immediately stop the separation, find the leaked portion, and repair it.

【0016】[0016]

【実施例】以下、本発明の内容を具体的に実施例によっ
て説明するが、本発明はこれらの実施例に制限されるも
のではない。
EXAMPLES The contents of the present invention will be specifically described below with reference to examples, but the present invention is not limited to these examples.

【0017】実施例1 内径0.8mm、全長30cmのポリイミド系中空糸膜
150本をポッティングしたモジュールを分離膜とした
パーベーパレーション装置でイソプロピルアルコールに
含まれている水の脱水を行った。60℃に加温されたイ
ソプロピルアルコールと水の混合液は中空糸膜の内側に
供給され、外側には減圧に引かれて7mmHgに保たれ
た。スタート時の供給液は量が50l、濃度がイソプロ
ピルアルコール:水=90:10(質量%)で、バッチ
運転をすることによりイソプロピルアルコールの濃度を
高めていった。運転中の供給液濃度に対する透過蒸気温
度を測定したところ、表1に示す値が得られた。供給液
濃度がイソプロピルアルコール:水=99.5:0.5
(重量%)になった時、濃度がイソプロピルアルコー
ル:水=90:10(重量%)になるまで水を加えて再
び脱水を続けた。この操作を繰り返し行ったところ、8
02回目に供給液濃度がイソプロピルアルコール:水=
90:10(重量%)の時に透過蒸気温度が32℃に急
激に低下したので脱水を停止してモジュールを調べたと
ころ、1本の中空糸からピンホールが発見された。
Example 1 Water contained in isopropyl alcohol was dehydrated by a pervaporation device using a module having 150 modules of a polyimide-based hollow fiber membrane having an inner diameter of 0.8 mm and a total length of 30 cm as potting. The mixed liquid of isopropyl alcohol and water heated to 60 ° C. was supplied to the inside of the hollow fiber membrane, and the outside was pulled to a reduced pressure and kept at 7 mmHg. The amount of the supply liquid at the start was 50 l, and the concentration was isopropyl alcohol: water = 90: 10 (mass%), and the concentration of isopropyl alcohol was increased by performing batch operation. When the permeated vapor temperature with respect to the feed liquid concentration during operation was measured, the values shown in Table 1 were obtained. Supply liquid concentration is isopropyl alcohol: water = 99.5: 0.5
When (wt%) was reached, water was added until the concentration became isopropyl alcohol: water = 90: 10 (wt%), and dehydration was continued again. When this operation was repeated, 8
At the 02nd time, the supply liquid concentration was isopropyl alcohol: water =
At 90:10 (% by weight), the permeation vapor temperature dropped sharply to 32 ° C., so when dehydration was stopped and the module was examined, pinholes were found in one hollow fiber.

【0018】[0018]

【表1】 [Table 1]

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】パーベーパレーション法において、透過蒸
気温度を測定することにより給液側から減圧側への供給
液の漏洩を検知することを特徴とするパーベーパレーシ
ョン法の漏洩検出方法。
1. A leak detection method of the pervaporation method, characterized in that the leak of the supply liquid from the supply liquid side to the decompression side is detected by measuring the permeation vapor temperature in the pervaporation method.
JP03342591A 1991-12-25 1991-12-25 Leak detection method of pervaporation method Expired - Fee Related JP3095496B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP03342591A JP3095496B2 (en) 1991-12-25 1991-12-25 Leak detection method of pervaporation method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP03342591A JP3095496B2 (en) 1991-12-25 1991-12-25 Leak detection method of pervaporation method

Publications (2)

Publication Number Publication Date
JPH05168874A true JPH05168874A (en) 1993-07-02
JP3095496B2 JP3095496B2 (en) 2000-10-03

Family

ID=18354956

Family Applications (1)

Application Number Title Priority Date Filing Date
JP03342591A Expired - Fee Related JP3095496B2 (en) 1991-12-25 1991-12-25 Leak detection method of pervaporation method

Country Status (1)

Country Link
JP (1) JP3095496B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998013890A1 (en) * 1996-09-25 1998-04-02 Ballard Power Systems Inc. Method and apparatus for detecting and locating perforations in membranes employed in electrochemical cells
JP2009219996A (en) * 2008-03-14 2009-10-01 Kurita Water Ind Ltd Method of detecting deterioration of gas permeable membrane, and method of operating gas permeable membrane module
CN105929112A (en) * 2016-04-19 2016-09-07 刘小红 Sensor for detecting leakage of liquid chemicals

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998013890A1 (en) * 1996-09-25 1998-04-02 Ballard Power Systems Inc. Method and apparatus for detecting and locating perforations in membranes employed in electrochemical cells
JP2009219996A (en) * 2008-03-14 2009-10-01 Kurita Water Ind Ltd Method of detecting deterioration of gas permeable membrane, and method of operating gas permeable membrane module
CN105929112A (en) * 2016-04-19 2016-09-07 刘小红 Sensor for detecting leakage of liquid chemicals
CN105929112B (en) * 2016-04-19 2018-04-10 刘小红 A kind of sensor for detecting liquid chemical leakage

Also Published As

Publication number Publication date
JP3095496B2 (en) 2000-10-03

Similar Documents

Publication Publication Date Title
EP0273267B1 (en) Method of separating a particular component from its liquid solution
Van Veen et al. Pushing membrane stability boundaries with HybSi® pervaporation membranes
US5616247A (en) Method for separating a liquid mixture using a pervaporation membrane module unit
JPH025849A (en) Method and apparatus for reducing alcohol content of alcoholic beverage
KR920011550A (en) Liquid mixture separation method
JP6576546B2 (en) Virus removal membrane and method for producing virus removal membrane
WO2015156401A1 (en) Virus removal membrane
JPH05168874A (en) Leak detection for pervaporation
WO2009090929A1 (en) Dehydrator
JP2020138119A (en) Raw material liquid concentration system
JPS62241527A (en) Dehumidifying method for air
JPH0536092B2 (en)
Mencarini Jr et al. Separation of tetrahydrofuran from aqueous mixtures by pervaporation
CN117425619A (en) Process for producing purified aqueous hydrogen peroxide solution
JP2003033633A (en) Method for producing hollow fiber membrane and hollow fiber membrane module
JP2003112018A (en) Method of detecting membrane breakage of membrane separator and membrane separating system
JP3336150B2 (en) How to recover the performance of a permselective pervaporation membrane
KR102464360B1 (en) The dehydration apparatus for organic solvent using membrane
JPH06262042A (en) Apparatus for purification of liquid
JP4148190B2 (en) Gas separation method and gas separation apparatus for vapor mixture
JP2532869Y2 (en) Permeation vaporizer
JPH06226002A (en) Azeotrope separator
JPH057743A (en) Hollow yarn membrane module
SU1729561A1 (en) Method of producing porous membrane
JPS5763102A (en) Membrane separator

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees