JPS5946335B2 - flow cell - Google Patents
flow cellInfo
- Publication number
- JPS5946335B2 JPS5946335B2 JP2773877A JP2773877A JPS5946335B2 JP S5946335 B2 JPS5946335 B2 JP S5946335B2 JP 2773877 A JP2773877 A JP 2773877A JP 2773877 A JP2773877 A JP 2773877A JP S5946335 B2 JPS5946335 B2 JP S5946335B2
- Authority
- JP
- Japan
- Prior art keywords
- flow
- liquid
- optical path
- portions
- width
- 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
Links
- 239000007788 liquid Substances 0.000 claims description 24
- 230000003287 optical effect Effects 0.000 claims description 17
- 238000005259 measurement Methods 0.000 description 6
- 210000004027 cell Anatomy 0.000 description 5
- 210000005056 cell body Anatomy 0.000 description 5
- 238000000926 separation method Methods 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000012530 fluid Substances 0.000 description 2
- MNWFXJYAOYHMED-UHFFFAOYSA-N heptanoic acid Chemical compound CCCCCCC(O)=O MNWFXJYAOYHMED-UHFFFAOYSA-N 0.000 description 2
- 238000004811 liquid chromatography Methods 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- FBUKVWPVBMHYJY-UHFFFAOYSA-N nonanoic acid Chemical compound CCCCCCCCC(O)=O FBUKVWPVBMHYJY-UHFFFAOYSA-N 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 230000000452 restraining effect Effects 0.000 description 2
- 238000004904 shortening Methods 0.000 description 2
- 238000002834 transmittance Methods 0.000 description 2
- 239000005643 Pelargonic acid Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 239000012531 culture fluid Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 230000001678 irradiating effect Effects 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000012780 transparent material Substances 0.000 description 1
Landscapes
- Optical Measuring Cells (AREA)
Description
【発明の詳細な説明】
本発明は流動する液体中の成分を測定する場合に使用す
るフローセルに関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a flow cell used for measuring components in a flowing liquid.
溶液の濃度或いは濁度等を測定する流路系、例えば液体
クロマトグラフィに用いる流路系または培養液のモニタ
に用いる流路系において流れを横切つて光を照射するに
あたり、通常の光路長では入射光に比べ著しく微弱な透
過光しか得られないときは光路長を単純に短かくすれば
透過光量が増大するので問題は或る程度解決される。し
かしながら、光路長を短かくすると流路断面積が減少す
るので通常は液体圧力が増大し、従つて流体の流速が高
いときにはそれだけ圧力増大が著しいのでフローセルの
耐圧性の面から光路長を充分に短かくできず、光路長の
調節可能な範囲はおのずから制限され透過光量の充分な
増加を計ることができない。また、従来液体クロマトグ
ラフィは分析の必要から感度の改良がなされていてその
普及と高速化によつて調整を目的とする使用方法も広く
行われるようになつたが、この場合従来に比べ高濃度の
液体が流されるため通常のモニタのシステムでは記録計
がスケール・アウトして分離の追跡が不可能なことがあ
る。これは高濃度溶液では入射光に比べ透過性が著しく
微弱になることに基因するもので、このような場合にも
光路長を短かくすれば透過光量が増大して安定した測定
記録を行うことは一応可能である。この濃度変化に対応
させる手段として、例えば特開昭51−109882号
公報に液体の流れ方向へ向つて流路幅が異なる部分を形
成したフローセルが開示されて居り、種種の光路長で光
の吸収を測定することができるが、液体の流れを横切る
一つの断面に特定流路幅の一つの流路のみが形成された
ものであるためすべての液体は流路幅の異なる部分のす
べてを順次通過しなければならない。従つて、流路幅の
狭い部分で圧力上昇を避けられないので光路幅をあまり
短かくすることはできず、また光路長を短かくした分だ
け光路に交叉方向の流路幅を増して流路断面積を拡げる
ことは可能であるが液体の流れが不均一になるという欠
点を生じる。本発明は液体の流れを直角に横切る光路方
向と平行な一つの断面に流路幅が異なる部分を複数形成
したことを特徴とし、光路に交叉方向の流路幅を著しく
拡げることなく充分光路長の短かい部分を形成し、しか
も圧力増大、流れの不均一等の不都合を招くことなく高
流速または高濃度の流体をj 流して安定した測定記録
が行われるようにしたものである。When irradiating light across the flow in a flow path system for measuring the concentration or turbidity of a solution, for example, a flow path system used for liquid chromatography or a flow path system used for monitoring culture fluid, the normal optical path length is When only transmitted light, which is extremely weak compared to light, can be obtained, simply shortening the optical path length increases the amount of transmitted light, which solves the problem to some extent. However, when the optical path length is shortened, the cross-sectional area of the flow path decreases, which usually increases the liquid pressure. Therefore, when the flow rate of the fluid is high, the pressure increase is significant, so from the viewpoint of pressure resistance of the flow cell, the optical path length must be set sufficiently. Therefore, the range in which the optical path length can be adjusted is naturally limited, and it is not possible to measure a sufficient increase in the amount of transmitted light. In addition, conventional liquid chromatography has been improved in sensitivity due to the need for analysis, and as its popularity and speed have increased, it has become widely used for the purpose of adjustment. Because the liquid is flowing, conventional monitoring systems may scale out the recorder and make it impossible to track the separation. This is due to the fact that in highly concentrated solutions, the transmittance is significantly weaker than that of the incident light.Even in such cases, shortening the optical path length increases the amount of transmitted light and enables stable measurement recording. is possible. As a means to cope with this concentration change, for example, Japanese Patent Laid-Open No. 109882/1982 discloses a flow cell in which portions with different channel widths are formed in the flow direction of the liquid, and the flow cell absorbs light with various optical path lengths. However, because only one channel with a specific channel width is formed in one cross section that crosses the liquid flow, all liquid passes sequentially through all sections with different channel widths. Must. Therefore, the pressure increase cannot be avoided in the narrow part of the channel, so the optical path width cannot be made too short, and the cross-direction width of the optical path must be increased by the amount that the optical path length is shortened. Although it is possible to widen the cross-sectional area of the passage, the disadvantage is that the flow of liquid becomes non-uniform. The present invention is characterized in that a plurality of portions with different channel widths are formed in one cross section parallel to the optical path direction that crosses the liquid flow at right angles, and the optical path has a sufficient optical path length without significantly increasing the channel width in the cross direction. It is designed to form a short section of j, and to allow stable measurement records to be performed by flowing fluid at a high flow rate or high concentration without causing problems such as increased pressure or non-uniform flow.
以下本発明の実施例を図面について説明すると、石英ガ
ラスその他の耐圧性、耐薬品性を有する透明材料によつ
て作られた二枚の板状の窓板1、2・ を平行且つ適当
な間隔で対向配置し、液体の流れ方向Aから見て前後両
端部の間にセル本体3、3の内端部をパッキング4、4
を挟んでそれぞれ液密に挿入すると共に左右両端部の間
に流路10の左右の壁面を形成する抑え部材5の内端部
を前記パツキング4を挟んでそれぞれ液密に挿入し、且
つ入射光通路6と透過光通路7とを液体の流れ方向Aと
直角に有するこの抑え部材5と窓板1,2およびセル本
体3,3との間にこれら通路6,7を囲んでパツキング
8,8を挿入し液密とする。Hereinafter, an embodiment of the present invention will be described with reference to the drawings. Two plate-shaped window plates 1 and 2 made of quartz glass or other transparent material having pressure resistance and chemical resistance are arranged parallel to each other and at an appropriate distance. The inner ends of the cell bodies 3, 3 are packed 4, 4 between the front and rear ends when viewed from the liquid flow direction A.
The inner ends of the restraining members 5, which form the left and right walls of the channel 10 between the left and right ends, are inserted in a liquid-tight manner with the packing 4 in between, and the incident light is Packing 8, 8 is provided between the suppressing member 5, which has a passage 6 and a transmitted light passage 7 perpendicular to the liquid flow direction A, and the window plates 1, 2 and the cell bodies 3, 3, surrounding these passages 6, 7. Insert it to make it liquid-tight.
前後のセル本体3,3は液体の流れる管路と接続される
接手9,9がねじ込み固着されていると共に流路10と
接手9,9とを連通する液通路11,11が設けられ、
且つ抑え部材5とセル本体3,3とはねじ12によつて
互いに締付け固定されている。流路10の前後部分は拡
げられていて広い流路断面積を有し、第1図、第2図の
実施例においては通路10の中央部分に流れ方向Aと直
交する方向へ向つて流路幅の小さい部分10aとその両
側の大きい部分10b,10bとを形成したものである
。The front and rear cell bodies 3, 3 are screwed and fixed with joints 9, 9 that are connected to a pipe through which liquid flows, and are provided with liquid passages 11, 11 that communicate the flow path 10 and the joints 9, 9.
Further, the restraining member 5 and the cell bodies 3, 3 are fastened and fixed to each other by screws 12. The front and rear portions of the flow path 10 are widened and have a wide cross-sectional area, and in the embodiment shown in FIGS. A small width portion 10a and large portions 10b, 10b on both sides thereof are formed.
二枚の窓板1,2の光が通過する全ての入射面および出
射面は互いに平行であつて、光はこれらの面に直角に照
射されるようになつている。第3図の実施例は流路の中
央部分に流れ方向と直交する方向へ向つて流路幅の小さ
い部分10a大きい部分10bおよびそれらの中間大き
さの部分10cを順に形成したものである。前記二つの
実施例では二枚の窓板1,2は対称の形状に作られそれ
ぞれに肉厚の異なる部分を設け同一肉厚部分を対向させ
ることによつて流路幅の異なる部分を形成している。All the incident surfaces and exit surfaces of the two window plates 1 and 2 through which light passes are parallel to each other, and the light is irradiated perpendicularly to these surfaces. In the embodiment shown in FIG. 3, a portion 10a with a small width, a portion 10b with a large width, and a portion 10c with an intermediate size are formed in order in the central portion of the flow path in a direction perpendicular to the flow direction. In the two embodiments described above, the two window plates 1 and 2 are made in a symmetrical shape, each having a portion with a different wall thickness, and portions with the same thickness facing each other to form portions with different channel widths. ing.
第4図の実施例は流路に向つて入射側の窓板1を均一厚
さとすると共に出射側の窓板2に肉厚の異なる部分を設
けることによつて流れ方向と直交する方向へ向つて流路
幅の中間大きさの部分10c、小さい部分10a、大き
い部分10bを順に形成したものである。In the embodiment shown in FIG. 4, the window plate 1 on the entrance side has a uniform thickness toward the flow path, and the window plate 2 on the exit side has portions with different thicknesses, so that the window plate 1 can be directed in the direction perpendicular to the flow direction. A portion 10c having an intermediate size, a small portion 10a, and a large portion 10b are formed in this order.
第5図の実施例は流路に向つて入射側の窓板1に肉厚の
異なる部分を設けると共に出射側の窓板2を均一厚さと
することによつて流れ方向と直交する方向へ向つて流路
幅の大きい部分10b、中間大きさの部分10C1小さ
い部分10aを順に形成したものである。In the embodiment shown in FIG. 5, the entrance side window plate 1 toward the flow path is provided with portions with different wall thicknesses, and the exit side window plate 2 is made to have a uniform thickness, so that the window plate 1 facing the flow path is directed in the direction perpendicular to the flow direction. A portion 10b having a large passage width, a portion 10C having an intermediate size, and a portion 10a having a small passage width are formed in this order.
尚、流れ方向と直交する方向即ち光路方向の流路幅の異
なる部分は図示の配列に限られるものでなく任意の複数
に且つ任意の配列に形成できることは言うまでもなく、
光は矢印Ba,Bb,Bcのようにそれぞれ流路幅の異
なる部分へ適宜照射される。It goes without saying that the portions having different channel widths in the direction perpendicular to the flow direction, that is, the optical path direction, are not limited to the arrangement shown in the drawings, but can be formed in any number and in any arrangement.
The light is appropriately irradiated onto portions having different channel widths as indicated by arrows Ba, Bb, and Bc.
以上のように構成した本発明によると、測定しようとす
る液体は流路内に形成された液体の流れを横切る方向の
流路幅が異なる部分のそれぞれを流れぬこととなり、流
路断面積は全体として大きく縮小されないと共に流路幅
の小さい部分を通過する液体は全液体の一部分であるの
で流れの不均一を招くことがなく、しかも高流速で大量
の液体を流しても著しい圧力上昇を招くということがな
く、このため特別に耐圧性を考慮することなく流路幅の
小さい部分を充分に小さくして透過光量の増加を計るこ
とができ、従つてまた高濃度溶液の測定記録も安定よく
行うことができるのである。According to the present invention configured as described above, the liquid to be measured does not flow through each of the portions formed in the flow path where the width of the flow path in the direction across the flow of the liquid differs, and the cross-sectional area of the flow path is Since the liquid is not greatly reduced as a whole and the liquid that passes through the narrow part of the channel is only a portion of the total liquid, it does not cause uneven flow, and even if a large amount of liquid is flowed at a high flow rate, it will not cause a significant pressure increase. Therefore, it is possible to measure the increase in the amount of transmitted light by making the small part of the flow path sufficiently small without considering pressure resistance in particular, and therefore the measurement records of high concentration solutions are also stable. It can be done.
また、流路幅の小さい部分と大きい部分との間で液体の
交換が速かに行われるので、流路幅の小さい部分におい
て光の透過率をモニタすることにより全溶液の濃度を遅
れることなく追跡できるのである。即ち本発明によると
、液体の流速を高くしても大きな圧力上昇を招かないた
め大量の液体のモニタが可能であると同時に、調整を目
的とした流路において特に高濃度、高濁度の溶液の分離
の様子をスケール・アウトの心配なく測定記録できる他
に、流路幅の小さい部分と大きい部分との寸法比を測定
個所と他の個所との濃度差が測定目的に支障ない限り任
意に設定できることからなり大容量高流速の液体の測定
に使用できる、流路幅の異なる部分が複数形成されてい
るので所望の光路長の流路幅の部分を選んで測定が可能
であり同一のフローセルに複数の計測装置を組合せるこ
とによつて測定可能な濃度範囲が大幅に増大する等の効
果を有するものである。In addition, since liquid exchange occurs quickly between the narrow and wide channel width sections, the light transmittance in the narrow channel width sections can be monitored without delay in determining the concentration of the total solution. It can be tracked. That is, according to the present invention, even if the flow rate of the liquid is increased, it does not cause a large pressure increase, so it is possible to monitor a large amount of liquid, and at the same time, it is possible to monitor a large amount of liquid. In addition to being able to measure and record the state of separation without worrying about scale-out, it is also possible to adjust the size ratio between the small and large channel widths arbitrarily as long as the concentration difference between the measurement location and other locations does not interfere with the measurement purpose. The same flow cell can be used for measuring liquids with large volumes and high flow rates.It has multiple sections with different channel widths, so it is possible to select and measure the channel width section with the desired optical path length. By combining a plurality of measuring devices, the measurable concentration range can be greatly increased.
次に本発明の試験結果を述べる。Next, test results of the present invention will be described.
試料としてヘプタノイツク酸とペラルゴン酸を用い、溶
出に使用する移動相として75%メタノールに苛性ソー
ダを0.2モル濃度に溶したものを用い、移動相を流速
0.29TfL1/Minl圧力31〜15k9/C7
lの割で流した。Heptanoic acid and pelargonic acid were used as samples, and the mobile phase used for elution was a solution of caustic soda dissolved in 75% methanol at a concentration of 0.2 mol.
I drained it at a rate of l.
比較のため盛進製薬(株)製カルボン酸分析計を使用し
て測定したところ、第6図イのように記録紙上でピーク
附近がスケール・アウトしその部分の分離は不明であつ
た。これに対し第1図、第2図に示す本発明品(流路幅
の小さい部分10aの光路長を1mmとした)を使用し
たところ、第6図口のように記録されピーク附近での分
離が明かである。For comparison, measurement was performed using a carboxylic acid analyzer manufactured by Seishin Pharmaceutical Co., Ltd., and as shown in FIG. 6A, the area near the peak was scaled out on the recording paper, and the separation of that portion was unclear. On the other hand, when the product of the present invention shown in Figs. 1 and 2 (the optical path length of the narrow channel width portion 10a was set to 1 mm) was used, the separation near the peak was recorded as shown in Fig. 6. is clear.
第1図は本発明の実施例を示す縦断面図、第2図は第1
図の矢印X−X方向の拡大断面部分図、第3図、第4図
および第5図は本発明のそれぞれ異なる実施例を示す第
2図と同様の断面図、第6図は試験結果を示すグラフで
ある。
1,2・・・・・・窓板、3・・・・・・セル本体、5
・・・・・・抑え部材、6・・・・・・入射光通路、7
・・・・・・透過光通路、10・・・・・・流路、10
a・・・・・・通路幅の小さい部分、10b・・・・・
・通路幅の大きい部分。FIG. 1 is a vertical sectional view showing an embodiment of the present invention, and FIG.
FIG. 3, FIG. 4, and FIG. 5 are sectional views similar to FIG. 2 showing different embodiments of the present invention, and FIG. 6 shows the test results. This is a graph showing. 1, 2...Window plate, 3...Cell body, 5
... Suppressing member, 6 ... Incident light path, 7
...Transmitted light path, 10...Flow path, 10
a... Part where the passage width is small, 10b...
・Parts with large aisle widths.
Claims (1)
断面に流路幅が異なる部分を複数形成したことを特徴と
するフローセル。1. A flow cell characterized in that a plurality of portions having different channel widths are formed in one cross section parallel to the optical path direction that crosses the flow of liquid at right angles.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2773877A JPS5946335B2 (en) | 1977-03-14 | 1977-03-14 | flow cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2773877A JPS5946335B2 (en) | 1977-03-14 | 1977-03-14 | flow cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS53112785A JPS53112785A (en) | 1978-10-02 |
| JPS5946335B2 true JPS5946335B2 (en) | 1984-11-12 |
Family
ID=12229364
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2773877A Expired JPS5946335B2 (en) | 1977-03-14 | 1977-03-14 | flow cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5946335B2 (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57156542A (en) * | 1981-03-23 | 1982-09-27 | Olympus Optical Co Ltd | Photometric device for automatic analyzing device |
| JPS58123355U (en) * | 1982-02-12 | 1983-08-22 | 株式会社島津製作所 | flow cell |
| JPH0517547U (en) * | 1991-02-22 | 1993-03-05 | 日本分光株式会社 | Flow cell |
| JP4712745B2 (en) * | 2007-03-06 | 2011-06-29 | 倉敷紡績株式会社 | Flow cell for transmitted light measurement |
| JP6983709B2 (en) * | 2018-03-29 | 2021-12-17 | 株式会社日立製作所 | Analytical system and analytical method |
-
1977
- 1977-03-14 JP JP2773877A patent/JPS5946335B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS53112785A (en) | 1978-10-02 |
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