JPH0230034Y2 - - Google Patents
Info
- Publication number
- JPH0230034Y2 JPH0230034Y2 JP1983133129U JP13312983U JPH0230034Y2 JP H0230034 Y2 JPH0230034 Y2 JP H0230034Y2 JP 1983133129 U JP1983133129 U JP 1983133129U JP 13312983 U JP13312983 U JP 13312983U JP H0230034 Y2 JPH0230034 Y2 JP H0230034Y2
- Authority
- JP
- Japan
- Prior art keywords
- ultrafilter
- hollow cylindrical
- membrane
- cylindrical tube
- ultrafiltration membrane
- 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
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- Separation Using Semi-Permeable Membranes (AREA)
- Centrifugal Separators (AREA)
Description
【考案の詳細な説明】
本考案は、生化学微量成分分離用の限外過器
に関する。[Detailed Description of the Invention] The present invention relates to an ultrafilter for separating biochemical trace components.
生化学分野の一例である臨床化学の分野で血清
や血漿から蛋白を除去するに際し、あるいはホル
モン、薬物、無機イオンなどの低分子物質と蛋白
質との結合に関する研究を行なうにあたつての、
結合型の低分子物質と遊離型の低分子物質との分
離に際し、ゲル過法や平衡透析法などとともに
限外過法が利用されている。 When removing proteins from serum or plasma in the field of clinical chemistry, which is an example of the field of biochemistry, or when conducting research on the binding of low-molecular substances such as hormones, drugs, and inorganic ions to proteins,
When separating bound low-molecular substances and free low-molecular substances, ultrafiltration methods are used along with gel filtration methods, equilibrium dialysis methods, and the like.
限外濾過法は、被検液を限外濾過膜に接して保
持する限外濾過器に遠心力等をかけ、被検液の低
分子画分のみを限外過膜に通過させ高分子画分
と分離するものである。 In the ultrafiltration method, centrifugal force is applied to an ultrafilter that holds the test liquid in contact with an ultrafiltration membrane, and only the low molecular weight fraction of the test liquid is passed through the ultrafiltration membrane to remove the high molecular fraction. It is separated from the minutes.
従来この限外〓過法に用いられている限外過
器は、例えば第1図に示した如く、中空円筒管2
内の下方に支持部材4を介して限外過膜3を張
設してなるものであり、使用にあたつては限外
過器1内に被検液を入れ、また過器下部に受器
5を装着し、これを遠心分離機にかけて目的とす
る物質の分離や除去を行なうのである。 The ultrafilter conventionally used in this ultrafiltering method has a hollow cylindrical tube 2, as shown in FIG.
An ultrafiltration membrane 3 is stretched across the lower part of the ultrafilter 1 through a support member 4. In use, a test liquid is put into the ultrafilter 1, and a receiver is placed in the lower part of the ultrafilter. A container 5 is attached to the container 5, and the target substance is separated and removed using a centrifugal separator.
ところで、スイングロータ遠心機を用い限外
過器に遠心力をかけて限外過を行なうと、過
が進行するに従つて被検液中に遠心ベクトル方向
の濃度分極が発生する。 By the way, when a swing rotor centrifuge is used to perform ultrafiltration by applying centrifugal force to the ultrafilter, concentration polarization occurs in the test liquid in the direction of the centrifugal vector as the ultrafiltration progresses.
従来では、限外過膜は、遠心ベクトルと直角
を成すように貼設されており、この場合限外濾過
膜近傍に高分子物質の高濃度画分が層状に偏在
し、更には特に高分子物質が高濃度となる過膜
上にゲル層が形成され、それ以上の過の進行を
妨げるため、濾過速度が著しく減少すると言う問
題があつた。 Conventionally, ultrafiltration membranes are pasted at right angles to the centrifugal vector, and in this case, high-concentration fractions of polymeric substances are unevenly distributed in a layer near the ultrafiltration membrane, and even more There was a problem in that a gel layer was formed on the filtration membrane where the concentration of the substance was high, and this prevented further filtration, resulting in a significant decrease in the filtration rate.
本考案はこの欠点の解消を目的とした、特に臨
床検査の分野で多用されるスイングローター遠心
機を用いる生化学微量成分分離用限外過器とし
て考案されたものであつて、限外過膜を平面状
とするとともに、中空円筒管内に遠心ベクトルに
対して傾斜するように張設したことを特徴とす
る。 The present invention was devised as an ultrafilter for separating trace components in biochemistry using a swing rotor centrifuge, which is often used in the field of clinical testing, with the aim of eliminating this drawback. It is characterized by having a flat shape and being stretched in a hollow cylindrical tube so as to be inclined with respect to the centrifugal vector.
以下図面に従い本考案を具体的に説明する。 The present invention will be explained in detail below with reference to the drawings.
第2図は本考案の一実施例を示す断面図であ
り、限外過器1は中空円筒管2の内部下方に支
持部材4を介して限外過膜3を傾斜して張設す
る。 FIG. 2 is a sectional view showing an embodiment of the present invention, in which the ultrafilter 1 has an ultrafilter membrane 3 slanted and stretched downwardly inside a hollow cylindrical tube 2 with a support member 4 interposed therebetween.
中空円筒管2は合成樹脂、例えばアクリル、ポ
リスチレン、ポリエチレン、ポリプロピレン等を
用いることができ、また限外過膜3は目的に応
じた孔径のものを適宜選択して使用する。限外
過膜の傾斜角は遠心時において遠心ベクトルに対
して傾斜し得る角度のいずれであつても良く、例
えば20〜70゜、好ましくは30〜60゜である。 The hollow cylindrical tube 2 can be made of synthetic resin, such as acrylic, polystyrene, polyethylene, polypropylene, etc., and the ultrafiltration membrane 3 can be used by appropriately selecting one with a pore size depending on the purpose. The angle of inclination of the ultrafiltration membrane may be any angle that can be inclined with respect to the centrifugal vector during centrifugation, and is, for example, 20 to 70 degrees, preferably 30 to 60 degrees.
限外過膜を支持する支持部材4は、例えば格
子状のものであり、中空円筒管2と一体成形する
ことができる。 The support member 4 that supports the ultrafiltration membrane is, for example, in the form of a lattice, and can be integrally molded with the hollow cylindrical tube 2.
限外過膜の装着は例えば、第2図A部の拡大
図である第3図に示した如く、中空円筒管2″と
一体成形した格子状の支持部材4の上に限外過
膜3を載置し、上部から中空円筒管2′を嵌合さ
せ、中空円筒管2′と2″を超音波融着することに
よつて装着することができる。 For example, as shown in FIG. 3, which is an enlarged view of part A in FIG. 2, the ultrafiltration membrane 3 is mounted on a lattice-shaped support member 4 integrally formed with the hollow cylindrical tube 2''. The hollow cylindrical tube 2' is fitted from above, and the hollow cylindrical tubes 2' and 2'' are ultrasonically fused.
第4図は本考案の他の実施例を示すものであ
り、中空円筒管2はフランジ6′,6″を有する中
空円筒管2′及び2″に分割されており、中空円筒
管2″は支持部材4と一体成形されている。 FIG. 4 shows another embodiment of the present invention, in which the hollow cylindrical tube 2 is divided into hollow cylindrical tubes 2' and 2'' having flanges 6' and 6'', and the hollow cylindrical tube 2'' is It is integrally molded with the support member 4.
そして支持部材4上に載置した限外過膜3
は、Oリング7を介して上部中空円筒管2′のフ
ランジ6′によつて押さえられ、両フランジ6′及
び6″は適宜のクランプ8によつて固定された限
外過器1を形成する。 And the ultrafiltration membrane 3 placed on the support member 4
is held by a flange 6' of the upper hollow cylindrical tube 2' via an O-ring 7, and both flanges 6' and 6'' form an ultrafilter 1 which is fixed by a suitable clamp 8. .
以上の生化学微量成分分離用の限外過器1に
よれば、限外過膜3は遠心ベクトルに対して常
に傾斜角を有しているため、遠心時密度の高い被
検液中の高濃度画分はこの限外過膜3の傾斜に
沿つて移動し一方側(遠心機の回転軸から見て先
端側)に偏る。 According to the ultrafilter 1 for separating biochemical trace components described above, since the ultrafilter membrane 3 always has an inclination angle with respect to the centrifugation vector, it is possible to The concentration fraction moves along the slope of the ultrafiltration membrane 3 and is biased to one side (the tip side when viewed from the rotation axis of the centrifuge).
従つて、限外過膜3の他方側領域(遠心機の
回転軸から見て手前側の領域)は常に被検液中の
高分子物質低濃度画分と接することとなり、この
部分でのゲル層の発生を抑えることができる。 Therefore, the region on the other side of the ultrafiltration membrane 3 (the region on the near side when viewed from the rotation axis of the centrifuge) is always in contact with the low concentration fraction of the polymer substance in the test solution, and the gel in this region The formation of layers can be suppressed.
以上詳しく説明した如く、本考案の生化学微量
成分分離用限外〓過器によれば、限外過膜を遠
心ベクトルに対して傾斜する平面上に張設したた
め、濃度分極及びゲル層発生に起因する限外過
速度の低下を有効に抑制できる。 As explained in detail above, according to the ultrafilter for biochemical trace component separation of the present invention, the ultrafilter membrane is stretched on a plane that is inclined with respect to the centrifugal vector, which prevents concentration polarization and gel layer formation. It is possible to effectively suppress the decrease in the ultra-high overspeed caused by this.
また、過器断面積あたりの過膜面積が大と
なるため過能力を向上させることができ、更に
中空円筒管内に、特別な成形等を必要としない平
面状の限外過膜を貼設した点で従来と同様の簡
単な構成であるため、容易且つ低コストで製造で
きる等多大な効果を奏する。 In addition, since the membrane area per cross-sectional area of the tube is large, the capacity can be improved, and a flat ultrafiltration membrane that does not require special shaping is pasted inside the hollow cylindrical tube. Since it has a simple structure similar to the conventional one, it has great effects such as being able to be manufactured easily and at low cost.
第1図は従来の限外過器の説明図、第2図及
び第4図は本考案の限外過器の断面図である。
第3図は第2図A部の拡大図として示したもので
あり、これにより限外過膜装着の一例を示す。
1……限外過器、2……中空円筒管、3……
限外過膜、4……支持部材、5……受器。
FIG. 1 is an explanatory diagram of a conventional limiter, and FIGS. 2 and 4 are sectional views of the limiter of the present invention.
FIG. 3 is an enlarged view of section A in FIG. 2, and shows an example of how the ultrafiltration membrane is attached. 1... Limiter, 2... Hollow cylindrical tube, 3...
Ultrafiltration membrane, 4... support member, 5... receiver.
Claims (1)
に通過させ高分子画分と分離する生化学微量成分
分離用限外過器において、 前記限外過膜を平面状とするとともに、中空
円筒管内に遠心ベクトルに対して傾斜するように
張設したことを特徴とする生化学微量成分分離用
限外過器。[Scope of Claim for Utility Model Registration] In an ultrafiltration device for biochemical trace component separation in which a low molecular fraction of a test liquid is passed through an ultrafiltration membrane and separated from a high molecular fraction by centrifugal force, An ultrafilter for separating trace components of biochemistry, characterized in that the membrane is flat and is stretched in a hollow cylindrical tube so as to be inclined with respect to a centrifugal vector.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13312983U JPS6042302U (en) | 1983-08-30 | 1983-08-30 | ultrafilter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13312983U JPS6042302U (en) | 1983-08-30 | 1983-08-30 | ultrafilter |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6042302U JPS6042302U (en) | 1985-03-25 |
| JPH0230034Y2 true JPH0230034Y2 (en) | 1990-08-13 |
Family
ID=30300421
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13312983U Granted JPS6042302U (en) | 1983-08-30 | 1983-08-30 | ultrafilter |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6042302U (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0337720Y2 (en) * | 1985-02-19 | 1991-08-09 | ||
| JPS6318443Y2 (en) * | 1985-02-09 | 1988-05-24 | ||
| JP2004188348A (en) * | 2002-12-12 | 2004-07-08 | Jfe Engineering Kk | Centrifugal sedimentation tube for sludge and drainage and slurry dewatering evaluation method |
| FR2992227B1 (en) * | 2012-06-20 | 2022-04-01 | Commissariat Energie Atomique | FILTRATION ASSEMBLY FOR FILTERING NANOPARTICLES COMPRISING A FILTER AND A FILTER SUPPORT, ASSOCIATED APPARATUS AND METHOD FOR ASSEMBLING THE ASSEMBLY AND METHOD FOR COLLECTING AND ANALYZING ASSOCIATED NANOPARTICLES. |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4323667Y1 (en) * | 1964-06-01 | 1968-10-05 | ||
| JPS5848351U (en) * | 1981-09-24 | 1983-04-01 | 日東電工株式会社 | Centrifuge tube for liquid concentration |
-
1983
- 1983-08-30 JP JP13312983U patent/JPS6042302U/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6042302U (en) | 1985-03-25 |
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