Automated conversion between SFC and HPLC

• US 9,163,618 B2
• Filed: 06/22/2012
• Issued: 10/20/2015
• Est. Priority Date: 06/24/2008
• Status: Active Grant

• Current Assignee: Agilent Technologies, Inc.
• Original Assignee: Agilent Technologies, Inc.
• Inventors: Wikfors, Edwin E., Fogelman, Kimber D., Berger, Terry A.
• Primary Examiner(s): Williams, Hezron E
• Assistant Examiner(s): Frank, Rodney T
• Application Number:
  US13/530,931
• Publication Number:
  US 20130048095A1
• Time in Patent Office: 1,215 Days
• Field of Search: 73/615.6
• US Class Current: 1/1
• CPC Class Codes: B01D 15/40 using supercritical fluid as mobile phase or eluent
• CPC Class Codes: F04B 11/0075 connected in series
• CPC Class Codes: F04B 23/06 the pumps being all of reciprocating positive-displacement type
• CPC Class Codes: G01N 2030/326 pumps
• CPC Class Codes: G01N 2030/342 fluid composition fixed during analysis
• CPC Class Codes: G01N 30/32 of pressure or speed G01N30/36 takes precedence
• CPC Class Codes: G01N 30/34 of fluid composition, e.g. gradient G01N30/36 takes precedence
• CPC Class Codes: Y10T 137/0352 Controlled by pressure
• CPC Class Codes: Y10T 137/7722 Line condition change responsive valves

Abstract

An apparatus, system, and process of converting a standard, high performance liquid chromatography (HPLC) flow path to a flow path suitable for supercritical fluid chromatography (SFC) are described. This reversible technique is applied to a variety of flow configurations including binary, high pressure solvent mixing systems and quaternary, low pressure solvent mixing systems than can be conventionally operated or automated. The technique is generally applied to the fields of supercritical fluid chromatography and high pressure liquid chromatography, but users skilled in the art will find utility for any flow system where pressurization components must be periodically applied to and removed from both ends of a flow stream in an automated manner.

Claims

1. An apparatus, comprising:

a source of CO2 supply; and

a fluidic switch configured to be selectively switched between;

a first switch position which provides a first flow path configuration through the switch for a liquid chromatographic (LC) system, and further provides a secondary flow path configuration; and

a second switch position which provides a second flow path configuration through the switch for a supercritical fluid chromatographic system,

wherein the source of CO2 supply communicates with the secondary flow path configuration when the switch is in the first position, and with the second flow path configuration when the switch is in the second position.

2. The apparatus of claim 1, further comprising:

a backpressure regulation module,

wherein the switch provides the capability to maintain fluidic communication between said source of CO2 supply and said backpressure regulation module in both first and second said switch positions.

3. The apparatus of claim 1, wherein said source of CO2 supply comprises a CO2 metering pump.

4. The apparatus of claim 2, wherein said source of CO2 supply comprises a CO2 booster pump.

5. The apparatus of claim 1, further comprising:

an HPLC pump and a collection of HPLC modules for dual use within the supercritical fluid system and the liquid chromatographic system,

wherein said HPLC pump and HPLC modules remain in the first flow path configuration when the fluidic switch is in the first position and remain in the second flow path configuration when the fluidic switch is in the second position.

6. The apparatus of claim 5, wherein said HPLC pump is a high pressure positive displacement pump.

7. The apparatus of claim 6, wherein said high pressure positive displacement pump is one of a quaternary pump module, an isocratic pump module, or one unit of a binary pump module.

8. The apparatus of claim 5, wherein at least one pump in each of the first and second flow path configurations is capable of rinsing the flow path with a mobile phase compatible with both chromatographic systems.

9. The apparatus of claim 5, wherein the first and the second flow path configurations each terminate through a mass spectrometer.

10. A system, comprising:

a plurality of modules comprising a liquid chromatography (LC) system and a supercritical fluid chromatography (SFC) system; and

a fluidic switch,

wherein the plurality of modules include;

a back pressure regulator, and

a pump for compressible fluids,

wherein the switch is configured to be selectively switched between a first switch position and a second switch position to convert a flowpath between the LC system and the SFC system, and

wherein fluidic communication is maintained between the pump and the backpressure regulator module in both the first and second switch positions.

11. The system in claim 10, wherein the LC system modules are configured for dual use within the SFC system and the LC system and are included in the flow path for each of the SFC system and the LC system.

12. The system of claim 10, wherein at least one pump is configured to rinse the flow path with a mobile phase compatible with both the SFC system and the LC system.

13. The system of claim 10, wherein the modules further comprise:

a mass spectrometer, wherein each of the LC system and the SFC system is fluidically connected to said mass spectrometer.

14. The system of claim 10, wherein the LC system includes a high performance liquid chromatography system of modules.

15. The system of claim 10, wherein the LC system includes an ultra high performance liquid chromatography system of modules.

16. The system of claim 10, wherein the LC system includes modules capable of operating within system pressures up to 600 bar.

17. A process, comprising:

selectively switching a liquid chromatography (LC) pump, chromatographic system components, an upstream LC solvent source, a supercritical fluid chromatography (SFC) compressible fluid mobile phase source, and SFC system components including a back pressure regulator between a first flow path configuration for an LC mode of operation, and a second flow path configuration for an SFC mode of operation; and

maintaining fluidic communication between the SFC compressible fluid phase source and the back pressure regulator.

18. The process of claim 17, further comprising:

rinsing a flowpath of the first flow path configuration and second flow path configuration to a state compatible with both modes of operation from either mode of operation.

19. The process of claim 17, further comprising:

directing flow of each mode of operation to a mass spectrometer.

20. The process of claim 17, wherein the first flow path configuration includes a high performance liquid chromatography flow path or an ultra high performance liquid chromatography flow path.