JPH0291563A - Supercritical fluid chromatograph - Google Patents
Supercritical fluid chromatographInfo
- Publication number
- JPH0291563A JPH0291563A JP63245382A JP24538288A JPH0291563A JP H0291563 A JPH0291563 A JP H0291563A JP 63245382 A JP63245382 A JP 63245382A JP 24538288 A JP24538288 A JP 24538288A JP H0291563 A JPH0291563 A JP H0291563A
- Authority
- JP
- Japan
- Prior art keywords
- column
- pressure
- pump
- fluid
- column outlet
- 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.)
- Pending
Links
- 239000012530 fluid Substances 0.000 title claims abstract description 18
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract description 8
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract description 4
- 239000001569 carbon dioxide Substances 0.000 abstract description 4
- 229910021529 ammonia Inorganic materials 0.000 abstract description 2
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 2
- 239000000463 material Substances 0.000 abstract 3
- 230000008021 deposition Effects 0.000 abstract 2
- 238000004458 analytical method Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 6
- 239000000126 substance Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
Landscapes
- Treatment Of Liquids With Adsorbents In General (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は超臨界流体クロマトグラフ(以下「5FCJと
いう)に関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a supercritical fluid chromatograph (hereinafter referred to as "5FCJ").
(従来の技術)
従来のSFCではカラムの下流に流路抵抗を取付はカラ
ム上流側の流体ポンプにより移動相を加圧2送液して、
ポンプ出口よりカラム内までの流路内に超臨界状態を作
り出している。第3図は従来のSFCを示す流路図であ
る。第3図中1は移動相を収納したボンベでありボンベ
中の移動相は移動相用ポンプ2により試料導入口3を通
ってカラム4に送られる。5はカラム恒温槽でありカラ
ム4は恒温に保たれている。図中6は抵抗管であり内径
を数マイクロメータ程度に細(したキャピラリ管が使用
される。7は検出器である。移動相用ポンプ2は抵抗管
6の流路抵抗に抗して移動相を送液するのでポンプ2.
試料導入口3.カラム4、抵抗管6間の移動相が超臨界
状態に保たれる。(Prior art) In conventional SFC, a flow path resistance is installed downstream of the column, and the mobile phase is pumped under pressure by a fluid pump upstream of the column.
A supercritical state is created in the flow path from the pump outlet to the inside of the column. FIG. 3 is a flow path diagram showing a conventional SFC. In FIG. 3, reference numeral 1 denotes a cylinder containing a mobile phase, and the mobile phase in the cylinder is sent to a column 4 through a sample inlet 3 by a mobile phase pump 2. 5 is a column constant temperature bath, and column 4 is kept at constant temperature. In the figure, 6 is a resistance tube, and a capillary tube with an inner diameter of several micrometers is used. 7 is a detector. The mobile phase pump 2 moves against the flow path resistance of the resistance tube 6. Since the phase is pumped, pump 2.
Sample introduction port 3. The mobile phase between the column 4 and the resistance tube 6 is maintained in a supercritical state.
(発明が解決しようとする課題) SFCに使用するカラムは流路の抵抗として作用する。(Problem to be solved by the invention) The column used in SFC acts as a resistance in the flow path.
従ってカラム内では圧力降下が生じ、カラム入口側に比
べてカラム出口付近ではかなり圧力が低くなっている。Therefore, a pressure drop occurs within the column, and the pressure is considerably lower near the column outlet than at the column inlet.
SFCでは移動相として通常二酸化炭素が使用されるが
、化学物質の二酸化炭素への溶解度は移動相流体の密度
が大きい程高いので、圧力が低いカラム出口付近では移
動相流体の密度が小さくなって試料成分が溶けきれなく
なり、析出してしまう結果、検出器まで試料成分が運ば
れず検出されない場合がある。また、析出した試料成分
がカラムに蓄積されカラムの詰まりゃ劣化の原因となる
。入口圧を高くすればカラム出口側での圧力が高くなる
けれどもカラム使用圧角範囲を越えて入口圧を上げるこ
とはできない。Carbon dioxide is usually used as the mobile phase in SFC, but the solubility of a chemical substance in carbon dioxide increases as the density of the mobile phase fluid increases, so the density of the mobile phase fluid decreases near the column outlet where the pressure is low. As a result, the sample components cannot be completely dissolved and precipitate, resulting in the sample components not being carried to the detector and not being detected. Furthermore, if the precipitated sample components accumulate in the column and the column becomes clogged, it may cause deterioration. Although increasing the inlet pressure increases the pressure at the column outlet, it is not possible to increase the inlet pressure beyond the column operating pressure angle range.
本発明はカラムの圧力降下に起因するカラム出口付近で
の試料成分の析出を生じないSFCを得ることを目的と
した。The object of the present invention is to obtain an SFC that does not cause precipitation of sample components near the column outlet due to column pressure drop.
(課題を解決するための手段)
本発明の超臨界流体クロマトグラフにあってはカラム出
口流路に加圧手段を接続した0本発明において加圧手段
とはポンプあるいはカラム入口側とカラム出口側を接続
する抵抗管を包含する。(Means for Solving the Problems) In the supercritical fluid chromatograph of the present invention, a pressurizing means is connected to the column outlet flow path.In the present invention, the pressurizing means is a pump, or a column inlet side and a column outlet side. Includes a resistance tube that connects the
(作用)
本発明のSFCにあってはカラム出口流路が強制的に加
圧される。カラム入口圧は移動相ポンプの送液圧力で制
御されるので、出口側加圧によりカラム内の圧力降下は
小さくなる。加圧手段の負荷によりカラム出口側が加圧
分だけ圧力がかさ上げされた状態が生じる。一方移動相
流体の密度は圧力の絶対値に依存するので圧力がかさ上
げされた分だけ移動相流体の密度があがり化学物質の移
動相への溶解度が大きくなる。(Function) In the SFC of the present invention, the column outlet channel is forcibly pressurized. Since the column inlet pressure is controlled by the liquid feeding pressure of the mobile phase pump, the pressure drop within the column is reduced by pressurizing the outlet side. Due to the load on the pressurizing means, a state occurs in which the pressure on the column outlet side is increased by the amount of pressure applied. On the other hand, since the density of the mobile phase fluid depends on the absolute value of the pressure, the density of the mobile phase fluid increases by the amount that the pressure is increased, and the solubility of the chemical substance in the mobile phase increases.
(実施例)
第1図は本発明の一実施例であるSFCの流路図である
。第1図中のSFC構成部品で第3図に示した従来のS
FCと同様な構成部品には同一の番号を付した。第1図
中9はカラム下流側の流路の一部分であり加圧用ポンプ
10がら圧力調整用流体11が合流される。圧力調整用
流体11は二酸化炭素、アンモニヤ、窒素等の物質が使
用できるが移動相流体と同一の物質を使用することが好
ましい、移動相用ポンプ2と加圧用ポンプ10は共に定
圧制御方式のポンプであり圧力センサ8と12の信号を
とり込むポンプ制御部13により制御される。(Example) FIG. 1 is a flow path diagram of an SFC that is an example of the present invention. The conventional SFC components shown in Fig. 3 are the SFC components in Fig. 1.
Components similar to those of the FC are given the same numbers. Reference numeral 9 in FIG. 1 is a part of the flow path on the downstream side of the column, into which the pressure adjusting fluid 11 is merged from the pressurizing pump 10. For the pressure adjustment fluid 11, substances such as carbon dioxide, ammonia, and nitrogen can be used, but it is preferable to use the same substance as the mobile phase fluid.Both the mobile phase pump 2 and the pressurization pump 10 are constant pressure control type pumps. It is controlled by a pump control section 13 which receives signals from pressure sensors 8 and 12.
また、1分析中に圧力を変更する分析法である圧カプロ
グラミング法分析中はポンプ制御部13は当該プログラ
ムに従い移動相用ポンプ2を制御すると共に圧力センサ
8と12の信号をとり込み。Furthermore, during analysis using the pressure programming method, which is an analysis method that changes the pressure during one analysis, the pump control unit 13 controls the mobile phase pump 2 according to the program and also takes in the signals of the pressure sensors 8 and 12.
両者の差が等しくなるように加圧用ポンプ10を制御す
る。あるいはまた、圧カプログラミング法分析の終了直
前まで加圧用ポンプ10を動作させず、移動相ポンプの
送液圧力がプログラムの最終圧力に達したのち分析終了
直前に加圧用ポンプを動作させ出口側を加圧するという
一連のポンプ繰作を行えば、試料成分が最適分離された
のち難溶性成分を追出すことができる。第2図は本発明
の他の実施例であるSFCの流路図である。第2図中の
流路構成部品で第3図に示した従来のSFCと同様な構
成部品には同一の番号を付した。第2図中14は試料導
入口3の上流部とカラム下流部流路の両者を接続する抵
抗管である。この抵抗管14はカラム4の持つ流路抵抗
より小さい抵抗を持つ管が選択される。The pressurizing pump 10 is controlled so that the difference between the two becomes equal. Alternatively, the pressurizing pump 10 may not be operated until just before the end of the pressure programming method analysis, and after the liquid delivery pressure of the mobile phase pump has reached the final pressure of the program, the pressurizing pump may be operated just before the end of the analysis to close the outlet side. By performing a series of pump operations to apply pressure, the sample components can be optimally separated and then the poorly soluble components can be expelled. FIG. 2 is a flow path diagram of an SFC that is another embodiment of the present invention. Components of the flow path in FIG. 2 that are similar to those of the conventional SFC shown in FIG. 3 are given the same numbers. Reference numeral 14 in FIG. 2 is a resistance tube that connects both the upstream portion of the sample introduction port 3 and the column downstream flow path. As this resistance tube 14, a tube having a resistance smaller than the flow path resistance of the column 4 is selected.
(発明の効果)
本発明のSFCにあってはカラム出口付近の流路内も高
圧に保たれる結果、カラム出口付近での試料成分の析出
が防がれる。このため圧力降下の大きい比較的長いバツ
クドカラムも使用することができる。また加圧用ポンプ
を使用する本発明の一実施態様にあっては圧力プログラ
ミング分析中もカラム内の流速を最適の一定値に保つこ
ともできる。(Effects of the Invention) In the SFC of the present invention, the inside of the flow path near the column outlet is also maintained at a high pressure, so that precipitation of sample components near the column outlet is prevented. For this reason, relatively long backed columns with large pressure drops can also be used. Furthermore, in an embodiment of the present invention using a pressurizing pump, the flow rate within the column can be maintained at an optimal constant value even during pressure programming analysis.
第1図は本発明の一実施例である超臨界流体クロマトグ
ラフの流路図であり、第2図は本発明の他の実施例であ
る超臨界流体クロマトグラフの流路図であり、第3図は
従来の超臨界流体クロマトグラフを示す流路図である。
図中1は移動相ボンベ、2は移動相用ポンプ。
4はカラム、6は抵抗管、10は加圧用ポンプ。
14は抵抗管である。
特許出願人 株式会社 島津製作所FIG. 1 is a flow path diagram of a supercritical fluid chromatograph that is an embodiment of the present invention, and FIG. 2 is a flow path diagram of a supercritical fluid chromatograph that is another embodiment of the present invention. FIG. 3 is a flow path diagram showing a conventional supercritical fluid chromatograph. In the figure, 1 is a mobile phase cylinder, and 2 is a mobile phase pump. 4 is a column, 6 is a resistance tube, and 10 is a pressurizing pump. 14 is a resistance tube. Patent applicant: Shimadzu Corporation
Claims (1)
トグラフ。A supercritical fluid chromatograph with a pressurizing means connected to the column outlet channel.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63245382A JPH0291563A (en) | 1988-09-29 | 1988-09-29 | Supercritical fluid chromatograph |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63245382A JPH0291563A (en) | 1988-09-29 | 1988-09-29 | Supercritical fluid chromatograph |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0291563A true JPH0291563A (en) | 1990-03-30 |
Family
ID=17132829
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63245382A Pending JPH0291563A (en) | 1988-09-29 | 1988-09-29 | Supercritical fluid chromatograph |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0291563A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010243215A (en) * | 2009-04-01 | 2010-10-28 | Jasco Corp | Supercritical fluid chromatography apparatus and density adjusting method of the same |
-
1988
- 1988-09-29 JP JP63245382A patent/JPH0291563A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010243215A (en) * | 2009-04-01 | 2010-10-28 | Jasco Corp | Supercritical fluid chromatography apparatus and density adjusting method of the same |
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