JPH05157680A - Device for testing performance of separation membrane - Google Patents

Device for testing performance of separation membrane

Info

Publication number
JPH05157680A
JPH05157680A JP3349714A JP34971491A JPH05157680A JP H05157680 A JPH05157680 A JP H05157680A JP 3349714 A JP3349714 A JP 3349714A JP 34971491 A JP34971491 A JP 34971491A JP H05157680 A JPH05157680 A JP H05157680A
Authority
JP
Japan
Prior art keywords
membrane
separation membrane
outer peripheral
sealing member
separation
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
JP3349714A
Other languages
Japanese (ja)
Other versions
JPH0692930B2 (en
Inventor
Masaharu Matsuda
正治 松田
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP3349714A priority Critical patent/JPH0692930B2/en
Publication of JPH05157680A publication Critical patent/JPH05157680A/en
Publication of JPH0692930B2 publication Critical patent/JPH0692930B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To obtain a device which is suitable for testing the performance of separation membranes used for the reverse osmosis method, ultrafiltration method, and precision filtration method. CONSTITUTION:The title device is composed of a container main body 1, cap body 14, and membrane surface covering mechanism and the covering mechanism is composed of a supporting body 3, separation membrane 4, member 5 for sealing the outer peripheral section of the film 4, member 10 for sealing the central part of the film 4, stirrer 9, and membrane fixing frame body 6. The outer peripheral edge section of the membrane 4 is pressed against and fixed to the supporting body 3 by means of the outer peripheral frame section of the frame body 6 through the member 5 and the member 10 and stirrer 9 are coaxially supported by the frame body 6. The central part of the membrane 4 is pressed against and fixed to the supporting body 3 by means of the shaft section of the frame body 6 and a liquid contact section having a ring-like surface is provided between the members 5 and 10.

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、無機物質〔例えば、鉄
分、不溶性ケイ素、水酸化アルミニウム、炭酸カルシウ
ムなどの無機物質〕および有機物質〔例えば、でん粉、
蛋白質、ビタミン、カビ、菌、リグニンなどの有機物
質〕含有溶液の溶媒と溶質、とくにコロイド成分を含有
する菌体培養液〔即ち、抗生物質など医薬品の製造工程
で用いられるカビや放線菌などの培養液中に存在すると
ころの栄養源として添加した大豆粉や大豆油その他のコ
ロイド成分と菌体が生成する有価物(液状) 〕や各種産
業廃液〔例えば、でん粉二場排水 (でん粉など) 、電着
塗装水洗排水 (塗料など)、繊維加工排水 (ラノリン、
染料など) 、等の各種産業排水〕中の溶媒と溶質または
懸濁物質とを分離する逆浸透法、限外濾過法および精密
濾過法に用いる分離膜の性能試験に好適な分離膜性能試
験装置に関するものであり、近年、その用途が増大して
いる溶液処理用分離膜の性能を正確かつ迅速に判定し、
新規有効な分離膜の開発、従来既成の分離膜の改良およ
び最適な利用分野の選択と拡大に寄与せんとするもので
ある。
The present invention relates to an inorganic substance [for example, an inorganic substance such as iron, insoluble silicon, aluminum hydroxide and calcium carbonate] and an organic substance [for example, starch,
Organic substances such as proteins, vitamins, molds, fungi and lignin] Solvents and solutes of solutions containing solutions, especially cell culture medium containing colloidal components Soybean flour or soybean oil added as a nutrient source that is present in the culture solution and valuable substances generated by the bacterial cells and other colloidal components (liquid)) and various industrial waste liquids (for example, starch second-site wastewater (starch, etc.), Electro-deposition paint rinsing drainage (paint etc.), textile processing drainage (lanolin,
Separation membrane performance test device suitable for performance tests of separation membranes used in reverse osmosis method, ultrafiltration method and microfiltration method for separating solvent and solute or suspended substance in various industrial wastewater such as dye) The accuracy and speed of the performance of separation membranes for solution treatment, which has been increasing in use in recent years,
It is intended to contribute to the development of new effective separation membranes, improvement of existing separation membranes, and selection and expansion of optimum fields of use.

【0002】[0002]

【従来の技術】従来の溶液用分離膜の性能試験装置は、
図4に示したように、主として円形状被試験分離膜30の
膜面中央上部に、所定間隔をおいて懸架設置した棒状撹
拌子31を回転させることによって、該膜表面上の試験溶
液を流動させながら膜性能を試験する方式のものであ
る。しかし、この方式の分離膜性能試験装置において
は、棒状撹拌子31の回転によって、図5に示すように、
円形状分離膜表面に渦巻状の液流を生じさせるために、
該膜の中心部と外周部とでは試験溶液の流動速度が著し
く異なるという問題点があった。即ち、該膜中心部に懸
濁物質が滞留するため、試験時間の経過と共に膜性能が
変化し、膜性能を正確に判定することができなかった。
2. Description of the Related Art A conventional performance tester for a separation membrane for solution is
As shown in FIG. 4, the test solution on the surface of the membrane is flowed mainly by rotating the rod-shaped stirrer 31 suspended above the membrane surface of the circular separation membrane 30 to be tested at a predetermined interval. This is a method of testing the membrane performance while performing the above. However, in the separation membrane performance testing device of this system, as shown in FIG.
In order to generate a spiral liquid flow on the surface of the circular separation membrane,
There is a problem that the flow rate of the test solution is significantly different between the central part and the outer peripheral part of the film. That is, since the suspended substance remains in the center of the membrane, the membrane performance changed with the lapse of the test time, and the membrane performance could not be accurately determined.

【0003】また、膜面中央部に懸濁物質が滞留しない
ようにして膜性能を試験する装置も知られている。この
装置においては、図6に示すように、円形状分離膜の中
央部に所定間隔をおいて1個または複数の吐出口33を配
設し、送液ポンプを用いてこれら吐出口33から試験溶液
を吐出させ、図7に示すように、該試験液を該膜の中央
部から外周部に向けて膜表面を放射状に流動させながら
膜性能を試験するものである。しかしながら、この方式
では、図7に示すように、円形状被試験分離膜の中央部
から外周部に向けて、放射状に試験溶液が拡散するた
め、該膜中央部から外周部に試験溶液が移動するにつれ
てその液流速が減衰する。したがって、有効膜面全域に
おいて液流速が均一にはならず、有効膜面の各部で膜透
過液量が異なり、正確に膜性能を判定することができな
かった。
There is also known a device for testing the membrane performance so that suspended matter does not stay in the central portion of the membrane surface. In this device, as shown in FIG. 6, one or a plurality of discharge ports 33 are arranged at a predetermined interval in the center of the circular separation membrane, and a test is performed from these discharge ports 33 using a liquid feed pump. A solution is discharged, and as shown in FIG. 7, the membrane performance is tested while radially flowing the test solution from the center of the membrane toward the outer periphery of the membrane. However, in this method, as shown in FIG. 7, since the test solution is radially diffused from the central portion of the circular test separation membrane toward the outer peripheral portion, the test solution moves from the central portion of the membrane to the outer peripheral portion. The liquid flow velocity decreases as the temperature rises. Therefore, the liquid flow velocity was not uniform over the entire effective membrane surface, and the amount of membrane permeated liquid was different in each part of the effective membrane surface, so that the membrane performance could not be accurately determined.

【0004】[0004]

【発明が解決しようとする課題】分離膜を用いて試験溶
液中の液成分と濁質成分とを分離する場合、液成分の膜
透過に伴って分離膜表面近傍に濁質成分が滞留して濃度
勾配が生じ、このため分離膜の性能が経時的に大きく変
動する。したがって、分離膜の性能を正確に判定するた
めには被試験分離膜の接液部、つまり有効膜面全域にお
いて、試験溶液を等速度で同一方向にかつ均一に流動さ
せることが必要不可欠の条件となる。しかるに、円形状
分離膜の中央部に設置した撹拌子の回転によって、試験
溶液を渦巻状に流動させる方式の装置や、円形状分離膜
の中央部から試験溶液を吐出し、放射状に流動させる方
式の装置では、いずれも該膜中央部と他部とでは液流速
が著しく異なり、前記必要条件を充足することはできな
い。
When a liquid component in a test solution and a turbid component are separated using a separation membrane, the turbid component stays near the surface of the separation membrane as the liquid component permeates through the membrane. A concentration gradient is created, which causes the performance of the separation membrane to vary significantly over time. Therefore, in order to accurately judge the performance of the separation membrane, it is an indispensable condition that the test solution is made to flow uniformly in the same direction at the same speed in the liquid contact portion of the separation membrane under test, that is, the entire effective membrane surface. Becomes However, by rotating the stirrer installed in the center of the circular separation membrane, a device that causes the test solution to flow in a spiral shape, or a method that discharges the test solution from the center of the circular separation membrane and causes it to flow radially In any of the above devices, the liquid flow velocity is significantly different between the central part of the membrane and the other part, and the above-mentioned requirements cannot be satisfied.

【0005】[0005]

【課題を解決するための手段】本発明は、前記従来装置
における問題点を解決するためになされたものであり、
本発明の分離膜性能試験装置は、容器本体、蓋体および
この両間に介在する膜面被覆機構からなり、前記膜面被
覆機構は、支持体、分離膜、分離膜外周部シーリング部
材、分離膜中央部シーリング部材、攪拌子および膜固定
枠体により構成され、前記分離膜の外周端部は、前記分
離膜外周部シーリング部材を介して前記膜固定枠体の外
周枠部で前記支持体に押圧固定され、前記分離膜中央部
シーリング部材および前記攪拌子は前記膜固定枠体に同
軸的に枢支され、前記分離膜中央部は前記膜固定枠体の
軸部で前記支持体に押圧固定され、前記分離膜外周部シ
ーリング部材と前記分離膜中央部シーリング部材との間
に円環面の接液部が設定され、前記円環面の接液部は、
前記攪拌子で円周に沿って流動が形成され、前記容器本
体は、円形凹部を有し、該凹部の底面部に容器本体外に
至る集水管を有し、前記蓋体は、外部への導通孔を有す
ることを特徴とするものである。
SUMMARY OF THE INVENTION The present invention has been made to solve the problems in the conventional device described above.
The separation membrane performance testing device of the present invention comprises a container body, a lid, and a membrane surface coating mechanism interposed between the container body and the lid. The membrane surface coating mechanism includes a support, a separation membrane, a separation membrane outer peripheral sealing member, and a separation membrane. A membrane central portion sealing member, a stirrer and a membrane fixing frame body, and an outer peripheral end portion of the separation membrane is attached to the support at the outer peripheral frame portion of the membrane fixing frame body via the separation membrane outer peripheral sealing member. The separation membrane central portion sealing member and the agitator are coaxially supported by the membrane fixing frame body, and the separation membrane central portion is pressed and fixed to the support body by the shaft portion of the membrane fixing frame body. The liquid contact portion of the annular surface is set between the separation membrane outer peripheral sealing member and the separation membrane central sealing member, and the liquid contact portion of the annular surface is
A flow is formed along the circumference by the stirrer, the container body has a circular recess, and a water collecting pipe reaching the outside of the container body is provided on the bottom surface of the recess, and the lid body is connected to the outside. It is characterized by having a through hole.

【0006】[0006]

【実施例】以下に本発明の実施例を図面に基づいて詳細
に説明する。図1は本発明の一実施例を示す膜性能試験
装置の側断面図、図2は図1に示した装置の構成部材の
拡大斜視図、図3は図1に示した装置の一使用例を示し
たものである。
Embodiments of the present invention will be described in detail below with reference to the drawings. FIG. 1 is a side sectional view of a membrane performance test apparatus showing an embodiment of the present invention, FIG. 2 is an enlarged perspective view of constituent members of the apparatus shown in FIG. 1, and FIG. 3 is a usage example of the apparatus shown in FIG. Is shown.

【0007】図1においては、容器本体1は耐圧、耐腐
食性の材質からなる円筒型の容器であり、上面部はOリ
ング15を捜着できる構造からなるフランジとなってお
り、容器本体内底部には円柱状の溝が施工されている。
また、該溝の底面部には容器本体外に至る集水管7が連
通していて、例えば幅1mm、深さ1mmの細溝2が縦およ
び横方向に互いに交錯して多数本施工されている。この
ため膜透過液は容易にかつすみやかに容器本体1の外部
に誘導して採取することができる。細溝2の上面部に接
して、例えば多孔質ステンレス板の如き透水性を有する
支持体3、支持体3の上面部に接して分離膜4、さらに
分離膜4の外周上面部に接して、例えばフッソ樹脂の如
き耐腐食性でかつ分離膜を押圧固定するために充分な弾
力性を有する基材からなるガスケット5がそれぞれ設置
されている。また、ガスケット5の上面部に接して容器
本体1と同様な材質からなる膜固定枠体6があり、止め
ネジ8によって容器本体1に押圧固定されている。さら
に、磁性体を内蔵し、フッソ樹脂などの如き耐腐食性、
耐摩耗性を有する基材からなる撹拌子9が中央部に施孔
された貫通孔を通して、分離膜中央部シーリング部材10
に円滑に回転可能に嵌合されている。なお該分離膜中央
部シーリング部材10は膜固定枠体6の中央部の挿入穴11
に挿入され、該分離膜中央シーリング部材10の底面部が
分離膜4の上面中央部に密着するように、膜固定枠体6
の頭頂部から押ネジ12によって押圧固定されている。
In FIG. 1, the container body 1 is a cylindrical container made of a pressure-resistant and corrosion-resistant material, and the upper surface is a flange having a structure capable of finding the O-ring 15. A cylindrical groove is formed on the bottom.
Further, a water collecting pipe 7 extending to the outside of the container body is communicated with the bottom surface of the groove, and a large number of narrow grooves 2 having a width of 1 mm and a depth of 1 mm, for example, are crossed with each other in the vertical and horizontal directions. .. Therefore, the membrane-permeated liquid can be easily and promptly guided to the outside of the container body 1 and collected. In contact with the upper surface of the narrow groove 2, a support 3 having water permeability, such as a porous stainless plate, in contact with the upper surface of the support 3, a separation membrane 4, and in contact with the outer peripheral upper surface of the separation membrane 4, For example, gaskets 5 made of a base material having corrosion resistance such as fluorine resin and having sufficient elasticity to press and fix the separation membrane are installed. Further, there is a film fixing frame body 6 made of the same material as the container body 1 in contact with the upper surface of the gasket 5, and is fixed to the container body 1 by a set screw 8. Furthermore, it has a built-in magnetic material, and it has corrosion resistance such as fluorine resin.
The separation member central part sealing member 10 is provided with a stirrer 9 made of a base material having abrasion resistance through a through hole formed in the central part.
It is fitted so that it can rotate smoothly. The separation membrane central sealing member 10 has an insertion hole 11 in the central portion of the membrane fixing frame 6.
The membrane fixing frame 6 so that the bottom surface of the separation membrane central sealing member 10 is closely attached to the center of the upper surface of the separation membrane 4.
It is pressed and fixed by a set screw 12 from the top of the head.

【0008】しかうして、ガスケット5および膜中央部
シーリング部材10によって、分離膜4の外周端末上面部
と中央上面部とに対液シールが施され、該膜4の上面接
液部つまり有効膜面は円環面となる。また、磁性体を内
蔵した撹拌子9は膜中央部シーリング部材10の中央突起
軸を中心軸として、例えば電磁撹拌器24の如き回転伝達
手段を用いて、容器本体1の底面外部から磁気誘導によ
って、任意の速度で容易に回転させることが可能であ
り、容器本体1に注入した試験溶液を分離膜4上面部に
形成された円環面の円周に沿って、等流速で同一方向に
かつ均一に流動させることができる。また、撹拌子9の
下面端部のいずれか一方には、膜中央部シーリング部材
10の基板部外周面とガスケット5の内周面および分離膜
4の円環面とで形成される矩形状間隙の断面寸法より
も、わずかに小さめの寸法からなる撹拌羽13が付設され
ており、該撹拌羽13は撹拌子9の回転に伴って、有効膜
面近傍に介在する試験溶液を一定方向に効率よく流動さ
せる機能をもっている。さらに、撹拌羽13の構成基材
は、通常は耐腐食性の金属板または樹脂板が用いられる
が、該基材の下端部にスポンジなどの柔軟材からなる洗
浄部材を張設することにより、試験溶液の流動作用のみ
ならず膜表面部の洗浄作用も合わせて行う機能を有して
いる。
Thus, the gasket 5 and the membrane central sealing member 10 provide liquid-proof sealing between the upper surface of the outer peripheral end and the upper surface of the center of the separation membrane 4, and the upper surface of the membrane 4 in contact with the liquid, that is, the effective membrane. The surface becomes an annular surface. Further, the stirrer 9 containing a magnetic material is magnetically guided from the outside of the bottom surface of the container body 1 by using a rotation transmitting means such as an electromagnetic stirrer 24 with the central projection axis of the membrane central portion sealing member 10 as the central axis. The test solution injected into the container body 1 can be easily rotated at an arbitrary speed, and along the circumference of the annular surface formed on the upper surface of the separation membrane 4 in the same direction at the same flow rate. It can be made to flow uniformly. In addition, at either one of the lower end portions of the stirrer 9, a membrane central sealing member is provided.
An agitating blade 13 having a size slightly smaller than the cross-sectional size of the rectangular gap formed by the outer peripheral surface of the substrate portion 10, the inner peripheral surface of the gasket 5, and the annular surface of the separation membrane 4 is provided. The stirring blade 13 has a function of efficiently flowing the test solution in the vicinity of the effective membrane surface in a certain direction as the stirring bar 9 rotates. Furthermore, the constituent base material of the stirring blade 13 is usually a corrosion-resistant metal plate or resin plate, but by stretching a cleaning member made of a soft material such as sponge at the lower end of the base material, It has the function of not only the flow action of the test solution but also the action of cleaning the membrane surface.

【0009】容器本体1の上面部には容器本体1と同様
な材質からなる蓋体14がOリング15を介してクランプ16
によって押圧固定されており、試験溶液および圧力流体
の容器外への漏洩を防止できると共に、両者の結合およ
び分割が極めて簡便に行なえることから、試験溶液の注
入および排出作業も容易に行うことができる。また、蓋
体14の上面部には容器外部への導通孔17, 18, 19が、例
えば流体導入管20および流体導出管21さらに圧力計22あ
るいは開閉バルブを接手を介してネジで連結できるよう
に開口している。
On the upper surface of the container body 1, a lid body 14 made of the same material as that of the container body 1 is clamped via an O-ring 15.
The test solution and pressure fluid can be prevented from leaking out of the container, and the two can be combined and separated very easily, making it easy to inject and discharge the test solution. it can. Further, on the upper surface of the lid body 14, there are provided through holes 17, 18, 19 to the outside of the container so that, for example, the fluid introducing pipe 20, the fluid outlet pipe 21, the pressure gauge 22 or the opening / closing valve can be connected with a screw through a joint. It has an opening.

【0010】図2は図1に示した分離膜性能試験装置の
各構成部材を組立て順に明示したものであり、図2から
明らかなように、本発明に係わる分離膜性能試験装置に
おける組立および分解作業は極めて簡便におこなえるこ
とから、容器本体1の内部洗浄操作はもとより、分離膜
4の交換操作も容易にかつすみやかに行える。したがっ
て、分離膜の性能試験を迅速に繰り返して実施すること
ができる。
FIG. 2 shows each component of the separation membrane performance testing device shown in FIG. 1 in the assembling order. As is apparent from FIG. 2, assembling and disassembling in the separation membrane performance testing device according to the present invention. Since the work can be performed very easily, not only the internal cleaning operation of the container body 1 but also the exchange operation of the separation membrane 4 can be easily and promptly performed. Therefore, the performance test of the separation membrane can be rapidly repeated.

【0011】図3は図1に示した分離膜性能試験装置の
一使用例を示したものであり、容器本体1に被試験分離
膜を装着し、試験溶液を注入して密閉する。ついで、容
器本体1の底面外部に設置した回転伝達手段、例えば電
磁撹拌器24などを用いて外部から磁気誘導によって、撹
拌子9を所定速度で回転させて試験溶液を流動させなが
ら、導入孔17から加圧流体を導入して該試験溶液を所定
の圧力に加圧する。膜透過液は捕集器27に採取し、計量
および分析すればよい。また、導入孔17から容器本体1
に導入して試験溶液に圧力を伝達するための圧力流体と
しては、通常は純水を加圧して用いるが、好ましくは試
験溶液と同種の溶媒、さらに望ましくは該試験溶液を分
離膜で処理した膜透過液を加圧して使用するのがよい。
なお、圧力流体に試験溶液と同種の溶媒もしくは膜透過
液を加圧して供した場合には、容器本体1内の試験溶液
の溶質濃度あるいはコロイド成分濃度や濁質成分濃度を
常時一定に保持することが可能となり、試験時間の経過
に拘らず常に同一の条件下で安定に膜性能の判定ができ
る。圧力伝達媒体として使用する前記圧力流体は、耐圧
性および耐腐食性の基材からなる貯槽23に所定の流体を
貯えて、例えば窒素ガスなどの不活性ガスを用いて所定
の圧力に加圧して用いればよい。
FIG. 3 shows an example of use of the separation membrane performance testing device shown in FIG. 1, in which the separation membrane to be tested is mounted on the container body 1 and the test solution is injected and sealed. Then, the stirring bar 9 is rotated at a predetermined speed by magnetic induction from the outside by using a rotation transmission means installed outside the bottom surface of the container body 1, for example, an electromagnetic stirrer 24 or the like, and the test solution is allowed to flow, while introducing the inlet 17 A pressurized fluid is introduced from above to pressurize the test solution to a predetermined pressure. The membrane permeate may be collected in the collector 27, weighed and analyzed. In addition, from the introduction hole 17 to the container body 1
As the pressure fluid for introducing pressure into the test solution and transmitting the pressure to the test solution, pure water is usually used under pressure, but preferably the same solvent as the test solution, and more preferably the test solution is treated with a separation membrane. It is preferred to pressurize the membrane permeate before use.
When the pressure fluid is pressurized with a solvent of the same type as the test solution or a membrane permeate, the solute concentration or colloid component concentration or turbid component concentration of the test solution in the container body 1 is always kept constant. This makes it possible to stably judge the membrane performance under the same conditions regardless of the elapsed test time. The pressure fluid used as a pressure transmitting medium is a predetermined fluid stored in a storage tank 23 made of a pressure-resistant and corrosion-resistant base material and pressurized to a predetermined pressure with an inert gas such as nitrogen gas. You can use it.

【0012】上記実施例における分離膜性能試験装置と
従来法装置による膜性能試験結果の一例を表1に示す。
Table 1 shows an example of the results of the membrane performance test by the separation membrane performance test apparatus and the conventional method apparatus in the above embodiment.

【0013】使用した被試験用分離膜は通常用いられて
いるポリスルホン素材 (分画分子量;50,000) の限外濾
過膜であり、試験溶液は蒸留水および湖水 (水素イオン
濃度7.5、濁度5.0、炭酸カルシウム80mg/L、鉄0.1
mg/L、ケイ酸11.8mg/L、SS成分45.4mg/L) を用
いた。試験条件は両方とも同一条件とし、液温20℃、操
作圧力0.5kg/cm2 、試験液の膜面平均流動速度1.0m
/sec であり、膜性能試験は分離膜が充分安定化したの
ち、1時間毎に膜透過液を採取して計測した。その結
果、試験液の膜面流動速度が関与しない蒸留水による膜
透過試験では本法が125.83L/m2 ・ hr、従来法が125.
84L/m2 ・ hrとなり、両方とも膜透過性能値は殆ど等
しい値となったが、湖水による試験では有効膜面の外周
部と中央部での試験液の膜面流動速度が異なる従来法で
は膜透過液流速が常に低い値となり、しかも試験時間の
経過と共にその値が軽減するために定常値が得られない
という欠点があった。
The separation membrane used for the test is an ultrafiltration membrane of a polysulfone material (fraction molecular weight: 50,000) which is usually used, and the test solutions are distilled water and lake water (hydrogen ion concentration 7.5, turbidity). 5.0, calcium carbonate 80mg / L, iron 0.1
mg / L, silicic acid 11.8 mg / L, SS component 45.4 mg / L) were used. The test conditions were the same for both, the liquid temperature was 20 ° C, the operating pressure was 0.5 kg / cm 2 , and the average flow velocity on the film surface of the test liquid was 1.0 m.
In the membrane performance test, the membrane permeated liquid was sampled every hour after the separation membrane was sufficiently stabilized and measured. As a result, in the membrane permeation test with distilled water that does not involve the flow velocity of the test solution on the membrane surface, this method is 125.83 L / m 2 · hr, and the conventional method is 125.83 L / m 2 · hr.
It was 84 L / m 2 · hr, and the membrane permeation performance values were almost the same in both cases, but in the test with lake water, in the conventional method in which the flow velocity of the test liquid on the outer peripheral portion and the central portion of the effective membrane surface is different. The membrane permeate flow rate always has a low value, and it has a drawback that a steady value cannot be obtained because the value decreases as the test time elapses.

【0014】一方、本法による試験結果は表1に示した
ように膜透過液流速が常に一定値となり、しかもこの傾
向は他の試験液例えばパン酵母水溶液やでん粉水溶液な
ど濁質成分を含む溶液についても同様な結果が得られて
いることから、本発明に係わる分離膜性能試験装置によ
れば長時間に亘って安定した膜性能試験値が得られると
いう利点がある。
On the other hand, the test results by this method show that the membrane permeate flow rate is always a constant value as shown in Table 1, and this tendency tends to occur in other test solutions, for example, solutions containing turbid components such as baker's yeast aqueous solution and starch aqueous solution. Since similar results were obtained also in the above, the separation membrane performance testing device according to the present invention has an advantage that stable membrane performance test values can be obtained for a long time.

【0015】[0015]

【発明の効果】以上説明したように本発明の分離膜性能
試験装置は、被試験分離膜の接液部つまり有効膜面を円
環面とし、円環面に沿ってループ状に試験溶液を移動さ
せることによって、有効膜面全域において等速度でしか
も同一方向にかつ均一に試験溶液を流動させることを可
能にしたものであり、膜性能を正確に判定できると共
に、上記有効膜面全域において試験溶液が均一に流動す
るため、従来法の如く有効膜面上の一部に発生する不均
質な汚れを防止でき、分離膜の性能試験を長期間安定に
実施できるという利点がある。
As described above, in the separation membrane performance testing device of the present invention, the liquid contact portion of the separation membrane to be tested, that is, the effective membrane surface is an annular surface, and the test solution is looped along the annular surface. By moving the test solution, it is possible to flow the test solution uniformly at the same speed and in the same direction over the entire effective film surface, so that the film performance can be accurately determined and the test can be performed over the entire effective film surface. Since the solution flows uniformly, there is an advantage that non-uniform fouling that occurs on a part of the effective membrane surface can be prevented as in the conventional method, and the performance test of the separation membrane can be stably performed for a long period of time.

【0016】さらに、該分離膜性能試験装置の構成要素
の一部である導通孔17を用いて、圧力流体例えば試験溶
液と同種の溶媒あるいは膜透過液などを導入して試験を
実施すれば、試験溶液濃度を経時変化させることなく、
長期に亘って正確に膜性能を判定できるという利点があ
り、従来法の如き試験溶液濃度を保持するために必要と
された高価な送液ポンプおよび複雑な配管設備を全く要
せず、経済的にも有利なものである。さらに加えて、該
分離膜性能試験装置の構成要素の一部である撹拌羽13に
洗浄部材を付設することによって、従来法では成し得な
かった分離膜表面の洗浄が可能となる。
Further, if the test is carried out by introducing a pressure fluid, for example, a solvent of the same kind as the test solution or a membrane permeate, using the through hole 17 which is a part of the constituent elements of the separation membrane performance testing device, Without changing the test solution concentration over time,
It has the advantage of being able to accurately determine the membrane performance over a long period of time, and does not require the expensive liquid feed pump and complicated piping equipment required to maintain the concentration of the test solution as in the conventional method. It is also advantageous. In addition, by attaching a cleaning member to the stirring blade 13 which is a part of the constituent elements of the separation membrane performance testing device, it becomes possible to clean the surface of the separation membrane which cannot be achieved by the conventional method.

【図面の簡単な説明】[Brief description of drawings]

【図1】分離膜性能試験装置の説明図である。FIG. 1 is an explanatory diagram of a separation membrane performance testing device.

【図2】分離膜性能試験装置の各構成部材および装置の
組立、分解図である。
FIG. 2 is an assembly and exploded view of each component and device of the separation membrane performance testing device.

【図3】分離膜性能試験装置の一使用例を示す説明図で
ある。
FIG. 3 is an explanatory diagram showing a usage example of a separation membrane performance testing device.

【図4】従来の分離膜性能試験装置の一例を示す説明図
である。
FIG. 4 is an explanatory diagram showing an example of a conventional separation membrane performance testing device.

【図5】図4に示した分離膜性能試験装置における液流
を示す説明図である。
5 is an explanatory diagram showing a liquid flow in the separation membrane performance testing device shown in FIG.

【図6】従来の分離膜性能試験装置の他の一例を示す説
明図である。
FIG. 6 is an explanatory diagram showing another example of a conventional separation membrane performance testing device.

【図7】図6に示した分離膜性能試験装置における液流
を示す説明図である。
FIG. 7 is an explanatory view showing a liquid flow in the separation membrane performance testing device shown in FIG.

【符号の説明】[Explanation of symbols]

1 容器本体 2 細溝 3 支持体 4 分離膜 5 ガスケット 6 膜固定枠体 7 集水管 9 撹拌子 10 膜中央部シーリング部材 13 撹拌羽 14 蓋体 17 導通孔 18 導通孔 19 導通孔 1 Container Main Body 2 Narrow Groove 3 Support 4 Separation Membrane 5 Gasket 6 Membrane Fixing Frame 7 Water Collection Tube 9 Stirrer 10 Membrane Center Sealing Member 13 Stirring Blade 14 Lid 17 Conduction Hole 18 Conduction Hole 19 Conduction Hole

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 容器本体、蓋体およびこの両間に介在す
る膜面被覆機構からなり、前記膜面被覆機構は、支持
体、分離膜、分離膜外周部シーリング部材、分離膜中央
部シーリング部材、攪拌子および膜固定枠体により構成
され、前記分離膜の外周端部は、前記分離膜外周部シー
リング部材を介して前記膜固定枠体の外周枠部で前記支
持体に押圧固定され、前記分離膜中央部シーリング部材
および前記攪拌子は前記膜固定枠体に同軸的に枢支さ
れ、前記分離膜中央部は前記膜固定枠体の軸部で前記支
持体に押圧固定され、前記分離膜外周部シーリング部材
と前記分離膜中央部シーリング部材との間に円環面の接
液部が設定され、前記円環面の接液部は、前記攪拌子で
円周に沿って流動が形成され、前記容器本体は、円形凹
部を有し、該凹部の底面部に容器本体外に至る集水管を
有し、前記蓋体は、外部への導通孔を有することを特徴
とする分離膜性能試験装置。
1. A container main body, a lid, and a membrane surface coating mechanism interposed between the both, wherein the membrane surface coating mechanism comprises a support, a separation membrane, a separation membrane outer peripheral sealing member, and a separation membrane central sealing member. , A stirrer and a membrane fixing frame, the outer peripheral end of the separation membrane is pressed and fixed to the support by the outer peripheral frame of the membrane fixing frame via the separation membrane outer peripheral sealing member, The separation membrane central portion sealing member and the stirrer are coaxially supported by the membrane fixing frame body, and the separation membrane central portion is pressed and fixed to the support body by the shaft portion of the membrane fixing frame body. A liquid contact part of the annular surface is set between the outer peripheral sealing member and the separation membrane central part sealing member, and the liquid contact part of the annular surface forms a flow along the circumference by the stirrer. , The container body has a circular recess, the bottom surface of the recess A separation membrane performance testing device, characterized in that a water collecting pipe reaching the outside of the container main body is provided in the portion, and the lid body has a conducting hole to the outside.
【請求項2】 前記攪拌子の一端部に、膜面洗浄部材を
膜面と接触しかつ摺動可能に配設したことを特徴とする
請求項1に記載した分離膜性能試験装置。
2. The separation membrane performance testing device according to claim 1, wherein a membrane surface cleaning member is disposed at one end of the stirring bar so as to be in contact with and slidable with the membrane surface.
JP3349714A 1991-12-06 1991-12-06 Separation membrane performance tester Expired - Lifetime JPH0692930B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3349714A JPH0692930B2 (en) 1991-12-06 1991-12-06 Separation membrane performance tester

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3349714A JPH0692930B2 (en) 1991-12-06 1991-12-06 Separation membrane performance tester

Publications (2)

Publication Number Publication Date
JPH05157680A true JPH05157680A (en) 1993-06-25
JPH0692930B2 JPH0692930B2 (en) 1994-11-16

Family

ID=18405603

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3349714A Expired - Lifetime JPH0692930B2 (en) 1991-12-06 1991-12-06 Separation membrane performance tester

Country Status (1)

Country Link
JP (1) JPH0692930B2 (en)

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Publication number Priority date Publication date Assignee Title
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Publication number Priority date Publication date Assignee Title
WO2006002500A1 (en) * 2004-07-06 2006-01-12 K.U.Leuven Research And Development High throughput screening for rapid development of membranes and membrane processes
US7818996B2 (en) 2004-07-06 2010-10-26 K.U. Leuven Research And Development High throughput screening for rapid development of membranes and membrane processes
CN102323200A (en) * 2011-08-29 2012-01-18 南通市飞宇石油科技开发有限公司 Rotation mechanism of long rock core gripper
JP2014223613A (en) * 2013-04-26 2014-12-04 ポール・コーポレーションPallCorporation Agitation cell module and usage method of the same
WO2016157360A1 (en) * 2015-03-30 2016-10-06 三菱重工業株式会社 Membrane separation apparatus
JPWO2018155678A1 (en) * 2017-02-27 2020-01-16 国立研究開発法人産業技術総合研究所 Gas barrier property evaluation apparatus and gas barrier property evaluation method

Also Published As

Publication number Publication date
JPH0692930B2 (en) 1994-11-16

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