DE19902697A1 - Dynamic mixing chamber for high pressure liquid chromatography process has minimum dwell volume and exactly reproduces liquid gradients - Google Patents

Dynamic mixing chamber for high pressure liquid chromatography process has minimum dwell volume and exactly reproduces liquid gradients

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Publication number
DE19902697A1
DE19902697A1 DE1999102697 DE19902697A DE19902697A1 DE 19902697 A1 DE19902697 A1 DE 19902697A1 DE 1999102697 DE1999102697 DE 1999102697 DE 19902697 A DE19902697 A DE 19902697A DE 19902697 A1 DE19902697 A1 DE 19902697A1
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Germany
Prior art keywords
mixer
mixing chamber
chamber
volume
liquids
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DE1999102697
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German (de)
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Guenter J Eppert
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Individual
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Individual
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Priority to DE1999102697 priority Critical patent/DE19902697A1/en
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    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N30/00Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
    • G01N30/02Column chromatography
    • G01N30/26Conditioning of the fluid carrier; Flow patterns
    • G01N30/28Control of physical parameters of the fluid carrier
    • G01N30/34Control of physical parameters of the fluid carrier of fluid composition, e.g. gradient
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N30/00Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
    • G01N30/02Column chromatography
    • G01N30/26Conditioning of the fluid carrier; Flow patterns
    • G01N30/28Control of physical parameters of the fluid carrier
    • G01N30/34Control of physical parameters of the fluid carrier of fluid composition, e.g. gradient
    • G01N2030/347Control of physical parameters of the fluid carrier of fluid composition, e.g. gradient mixers

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  • Physics & Mathematics (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • General Physics & Mathematics (AREA)
  • Immunology (AREA)
  • Pathology (AREA)

Abstract

In a high pressure liquid chromatography (HPLC) process a low dwell-volume mixer unit continually prepares a supply of an elution agent. The dynamic mixer operates at pressures of up to 500 bar. The liquids are mixed by a rotating mixer assembly which has the same geometric shape as the mixer chamber, but is fractionally smaller than the chamber, leaving a tiny gap between the two. In a high pressure liquid chromatography (HPLC) process a low dwell-volume mixer unit continually prepares a supply of an elution agent. The dynamic mixer operates at pressures of up to 500 bar. The liquids are mixed by a rotating mixer assembly which has the same geometric shape as the mixer chamber, but is fractionally smaller than the chamber, leaving a tiny gap between the two. The fluid ingredients are able to flow through the gap when the rotor is turning at high speed. The mixing action between the fluids is effected by the tangential forces existing between the two faces, and by turbulence generated by milled surface irregularities in the cylindrical, ellipsoid or conical rotor. The liquid ingredients enter the mixer chamber at A and emerge at B. the mixing process takes place between the chamber wall W and mixer face R. The average gap width is 0.1 mm.

Description

Es ist bekannt, Flüssigkeiten in Rührgefäßen mit Hilfe rotierender Körper kontinuierlich oder diskontinuierlich zu vermischen, wozu meist Rührstäbe dienen, deren Abmessungen in bezug auf das verwendete Mischungsvolumen vergleichsweise klein sind. Sie werden durch äußere Magnetfelder in Rotation versetzt.It is known to rotate liquids in stirred vessels Mixing bodies continuously or discontinuously, which is usually the case Stirring bars serve, their dimensions in relation to the used Mix volumes are comparatively small. You will be through external magnetic fields set in rotation.

In der Flüssigchromatographie benutzt man zum Vermischen strömender Flüssigkeiten nach dem gleichen Prinzip arbeitende geschlossene Rührgefäße, sog. dynamische Mischkammern.In liquid chromatography, mixing is used flowing liquids working on the same principle closed mixing vessels, so-called dynamic mixing chambers.

Eine andere in der Flüssigchromatographie praktizierte Möglichkeit zum Vermischen strömender Flüssigkeiten besteht in der Anwendung spezieller T-Stücke oder Fritten. Man nennt die darauf basierenden Vorrichtungen statisch (Literatur zum Stand der Technik: Einschlägige Monographien über HPLC).Another possibility for liquid chromatography practiced Mixing flowing liquids is the application special tees or frits. They are called the ones based on it Devices static (literature on the prior art: relevant Monographs on HPLC).

Dynamische Mischkammern ergeben wesentlich effektivere Flüssigkeitsvermischungen als statische Mischer. Sie besitzen aber den großen Nachteil, daß in Abhängigkeit vom effektiven Mischkammervolumen VKeff (Mischkammervolumen minus Rührkörpervolumen) immer ein mehr oder weniger großer exponentieller Verdünnungseffekt auftritt. Dadurch kommt es bei der Anwendung solcher Vorrichtungen zur Herstellung von Elutionsmittelgradienten für die Chromatographie (unter Elutionsmittelgradient ist die kontinuierliche Konzentrationsänderung des Elutionsmittels durch Vermischen mehrerer Lösungsmittel zu verstehen) zum verzögerten Einsetzen und zu einer Verzerrung des tatsächlich in der Apparatur wirksamen Ist-Gradienten gegenüber dem vorgegebenen und gewünschten Soll-Gradienten.Dynamic mixing chambers result in much more effective liquid mixing than static mixers. However, they have the great disadvantage that, depending on the effective mixing chamber volume V Keff (mixing chamber volume minus stirring body volume ), there is always a more or less exponential dilution effect. As a result, when using such devices for the production of eluent gradients for chromatography (eluent gradient is to be understood as the continuous change in the concentration of the eluent by mixing several solvents), there is a delay in the onset and a distortion of the actual gradient actually effective in the apparatus compared to the given one and desired target gradients.

Das wirksame sog. Dwell-Volumen VD und die sog. Dwell-Zeit tD sind mit dem Lösungsmittel Gesamt-Volumenfluß verknüpft gemäß tD = VD/. Näherungsweise kann man setzen VD ≈ VKeff, da die übrigen Beiträge zum Dwell-Volumen bei modernen Geräten gegenüber VKeff zu vernachlässigen sind.The effective so-called Dwell volume V D and the so-called Dwell time t D are linked to the solvent total volume flow according to t D = V D /. Approximately one can set VD ≈ V Keff , since the other contributions to the Dwell volume in modern devices are negligible compared to V Keff .

VKeff muß stets wesentlich kleiner sein als der für die vorgesehene chromatographische Trennsäule notwendige Volumenfluß , andernfalls werden die oben angeführten Nachteile sehr relevant. Da man heute zunehmend kleine Volumenflüsse benötigt, sind die üblichen dynamischen Mischkammern, die in der Regel Mischkammervolumina von einigen Zehntel Millilitern bis zu einem Milliliter aufweisen, nicht brauchbar (Tabelle 1).V Keff must always be significantly smaller than the volume flow required for the intended chromatographic separation column, otherwise the disadvantages mentioned above become very relevant. Since increasingly small volume flows are required today, the usual dynamic mixing chambers, which generally have mixing chamber volumes of a few tenths of a milliliter to one milliliter, cannot be used (Table 1).

Die vorliegende Erfindung vermeidet die vorstehend diskutierten Nachteile und Probleme durch die erfindungsgemäße Realisierung der in Hinblick auf die heute zur Chromatographie notwendigen Volumenflüsse hinreichend kleinen effektiven Mischkammervolumina (Tabelle 1). Auf diese Weise läßt sich eine gute Übereinstimmung zwischen Soll- und Ist-Gradienten immer erreichen. Allerdings sind für sehr kleine Mischkammervolumina hochwertige, pulsationsarm fördernde Pumpen erforderlich.The present invention avoids those discussed above Disadvantages and problems due to the implementation of the invention with regard to those necessary for chromatography today Volume flows of sufficiently small effective mixing chamber volumes (Table 1). In this way, a good match can be made always achieve between target and actual gradients. However, are for very small mixing chamber volumes high quality, low pulsation promotional pumps required.

Ein weiterer Vorteil der Erfindung besteht darin, daß die erfindungsgemäß für geringe Volumenflüsse gestalteten dynamischen Mischkammern bei Bedarf auch mit wesentlich höheren Flüssen, beispielsweise mit mehreren Millilitern pro Minute betrieben werden können, wodurch ein flexibler Einsatz erreicht wird.Another advantage of the invention is that the Dynamic designed according to the invention for low volume flows Mixing chambers with significantly higher flows if required, for example, operated at several milliliters per minute can, whereby a flexible use is achieved.

Ein Ausführungsbeispiel der Erfindung wird in Abb. 1 erläutert. An embodiment of the invention is illustrated in Fig. 1.

Die Skizze (Schnittbild) verdeutlicht das Prinzip der Erfindung.The sketch (sectional view) illustrates the principle of the invention.

Der Rotationskörper, in dessen Innerem sich ein kleiner Magnet oder Stahlkörper befindet, ist im Beispiel als Rotationszylinder ausgebildet. Dieser wird durch die bei A unvermischt eintretenden und bei B vermischt austretenden Flüssigkeiten in der Schwebe gehalten und durch ein starkes äußeres Magnetfeld in schnelle Rotation versetzt, was mit dem kreisförmig abgebildeten Pfeil angedeutet wurde. Die Mischungsvorgänge spielen sich im Spaltsystem zwischen Kammerwand W und Rührkörperwand R ab. Jeder der gebildeten Spalte besitzt nur eine Breite von etwa 0,1 mm. Das für das Dwell- Volumen der dynamischen Mischkammer maßgebende effektive Kammervolumen VKeff beträgt auf diese Weise je nach Kammergröße beispielsweise 0,03 ml (30 µl), 0,02 ml (20 µl) oder 0,01 ml (10 µl). Effektive Kammervolumina unter 10 µl sind erfindungsgemäß ebenfalls möglich, jedoch ist ihre praktische Realisierung relativ aufwendig. The rotating body, inside of which there is a small magnet or steel body, is designed as a rotating cylinder in the example. This is kept in suspension by the liquids entering A unmixed and leaving M mixed B and is set in rapid rotation by a strong external magnetic field, which was indicated by the circular arrow. The mixing processes take place in the gap system between chamber wall W and stirring body wall R. Each of the gaps formed is only about 0.1 mm wide. The effective chamber volume V Keff, which is decisive for the Dwell volume of the dynamic mixing chamber, is in this way, depending on the chamber size , for example 0.03 ml (30 μl), 0.02 ml (20 μl) or 0.01 ml (10 μl). Effective chamber volumes below 10 μl are also possible according to the invention, but their practical implementation is relatively complex.

Tabelle 1 Table 1

Claims (2)

1. Vorrichtung zum dwellvolumenarmen kontinuierlichen Vermischen von Flüssigkeiten zur Herstellung von Elutionsmitteln für die Flüssigchromatographie (HPLC), vorzugsweise bis 500 bar, mit Hilfe des Prinzips der dynamischen Mischkammer, dadurch gekennzeichnet, daß ein minimales effektives Mischkammer­ volumen in der Weise realisiert wird, daß der zum Vermischen der Flüssigkeiten verwendete Rührkörper als Rotationskörper ausgebildet ist und die gleiche geometrische Form wie die Mischkammer erhält, wobei das Rotationskörpervolumen nur um soviel kleiner als das Mischkammervolumen sein soll, daß zwischen Mischkammerwand und Rotationskörperwand ein sehr enges Spaltsystem entsteht, durch das die Flüssigkeiten bei hoher Drehzahl des Rotationskörpers strömen.1. Device for low dwell volume continuous mixing of liquids for the production of eluents for liquid chromatography (HPLC), preferably up to 500 bar, using the principle of the dynamic mixing chamber, characterized in that a minimum effective mixing chamber volume is realized in such a way that the Stirring body used to mix the liquids is designed as a rotating body and receives the same geometric shape as the mixing chamber, the rotating body volume should only be so much smaller than the mixing chamber volume that a very narrow gap system is created between the mixing chamber wall and the rotating body wall, through which the liquids at high Flow speed of the rotating body. 2. Vorrichtung nach Anspruch 1, dadurch gekennzeichnet, daß die Flüssigkeitsvermischung zwischen den parallelen Spaltflächen von Mischkammerwand und Rotationskörperwand nicht allein durch Tangentialkräfte zustande kommt, sondern auch durch Turbulenz infolge von eingefrästen Oberflächenprofilen auf dem vorzugsweise zylindrisch, ellipsoidisch oder kugelförmig gestalteten Rotationskörper.2. Device according to claim 1, characterized in that the Liquid mixing between the parallel gap surfaces of Mixing chamber wall and rotating body wall not only through Tangential forces comes about, but also through turbulence due to milled surface profiles on the preferred cylindrical, ellipsoidal or spherical Rotational body.
DE1999102697 1999-01-14 1999-01-14 Dynamic mixing chamber for high pressure liquid chromatography process has minimum dwell volume and exactly reproduces liquid gradients Withdrawn DE19902697A1 (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2021034874A1 (en) * 2019-08-21 2021-02-25 Waters Technologies Corporation Method for determining a dwell volume of a chromatographic system
US11185830B2 (en) 2017-09-06 2021-11-30 Waters Technologies Corporation Fluid mixer
US11555805B2 (en) 2019-08-12 2023-01-17 Waters Technologies Corporation Mixer for chromatography system
US11821882B2 (en) 2020-09-22 2023-11-21 Waters Technologies Corporation Continuous flow mixer
US11898999B2 (en) 2020-07-07 2024-02-13 Waters Technologies Corporation Mixer for liquid chromatography
US11988647B2 (en) 2020-07-07 2024-05-21 Waters Technologies Corporation Combination mixer arrangement for noise reduction in liquid chromatography

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11185830B2 (en) 2017-09-06 2021-11-30 Waters Technologies Corporation Fluid mixer
US11555805B2 (en) 2019-08-12 2023-01-17 Waters Technologies Corporation Mixer for chromatography system
WO2021034874A1 (en) * 2019-08-21 2021-02-25 Waters Technologies Corporation Method for determining a dwell volume of a chromatographic system
US11709085B2 (en) 2019-08-21 2023-07-25 Waters Technologies Corporation Method for determining a dwell volume of a chromatographic system
US11898999B2 (en) 2020-07-07 2024-02-13 Waters Technologies Corporation Mixer for liquid chromatography
US11988647B2 (en) 2020-07-07 2024-05-21 Waters Technologies Corporation Combination mixer arrangement for noise reduction in liquid chromatography
US11821882B2 (en) 2020-09-22 2023-11-21 Waters Technologies Corporation Continuous flow mixer

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