Method and apparatus for hydrodynamic relaxation and sample concentration NIN field-flow fraction using permeable wall elements

• US 5,193,688 A
• Filed: 07/05/1991
• Issued: 03/16/1993
• Est. Priority Date: 12/08/1989
• Status: Expired due to Fees

• Current Assignee: University of Utah (State of Utah)
• Original Assignee: University of Utah (State of Utah)
• Inventors: Giddings, John C.
• Primary Examiner(s): Hajec, Donald T.
• Application Number:
  US07/726,370
• Time in Patent Office: 620 Days
• Field of Search: 209/1, 209/155, 209/208-210, 209/156, 209/39, 209/40, 209/127.1, 209/129, 209/130, 209/422, 209/12, 209/454, 209/11, 210/478, 210/495, 210/511, 210/222, 73/865.5
• US Class Current: 209/155
• CPC Class Codes: B03B 5/00 Washing granular, powdered or lumpy materials; Wet separating separating by pneumatic tables or by pneumatic jigs B03B4/00
• CPC Class Codes: G01N 30/0005 Field flow fractionation
• CPC Class Codes: G01N 30/16 Injection G01N30/24 takes precedence
• CPC Class Codes: G01N 30/6017 Fluid distributors

Abstract

A new field flow fractionation process for the separation of particles using a modified channel structure to achieve hydrodynamic relaxation without involving a stop-flow procedure and thus provide improved speed of operation as well as improved sample concentration, the new improved channel structure comprising a thin channel having one or more permeable wall sections contained in the enclosing wall or walls of the channel, the permeable wall sections making up not more than 25% of the total wall area of the channel, and adjustable flow control valves for controlling the flowrate of any fluid at the inlet end of the channel and independent flow control valves for controlling the flow rate of the fluid being introduced into or withdrawn from the permeable wall sections.

Claims

1. In a field-flow fractionation process for the separation of particles and polymers wherein a carrier fluid containing the particles to be separated is forced through a thin elongated flow channel having an enclosing wall, an inlet end and an outlet end, and a field or gradient is used to induce a driving force on the particles acting across the thin dimension of the channel perpendicular to the direction of the main channel axis and the particles entering the channel at the inlet end undergo fractionation as they are carried through the channel by flow and emerge as particles fractions at the outlet end, the improvement which comprises feeding at least two independent substreams of carrier fluid into the channel through at least two inlets located at the inlet end, one being the sample inlet, introducing the sample particles into one substream called the sample inlet substream that is forced to enter the channel through the sample inlet, forcing the carrier fluid of the remaining substream or substreams to enter the channel through one or more permeable wall sections whose combined areas constitute less than 25% of the total enclosed wall area of the channel, adjusting the relative flowrates of the different substreams to such proportions that the sample experiences a substantial measure of hydrodynamic relaxation as the substreams merge near the sample inlet.

2. A process as in claim 1 wherein the driving force is generated by a crossflow of fluid in the channel.

3. A process as in claim 1 wherein the driving force is sedimentation.

4. A process as in claim 1 wherein the permeable wall section is made up of a ceramic material having a pore size varying from 1 um to 20 um.

5. A process as in claim 1 in which the substreams enter the channel continuously without interruption for the stopflow procedure.

6. A process as in claim 1 wherein the enclosing wall includes both a depletion wall and an accumulation wall and wherein at least one permeable wall section is incorporated in the depletion wall at the inlet end of the channel.

7. A process as in claim 6 wherein there is an inlet end at the accumulation wall wherein at least one permeable wall section is located at the inlet end of the accumulation wall.

8. A process as in claim 6 wherein the flowrate entering through the permeable wall section or sections is greater than the flowrate entering by means of the sample inlet substream.

25. An apparatus as in claim 2 in which the enclosing wall includes both a depletion wall and an accumulation wall.

26. An apparatus as in claim 25 in which at least one permeable wall section is located near the outlet end of the depletion wall.

9. In a field-flow fractionation process for the separation of particles and polymers wherein a carrier fluid containing the particles to be separated is forced through a thin elongated flow channel having an enclosing wall, an inlet end and a field or gradient is used to induce a driving force on the particles acting across the thin dimension of the channel perpendicular to the direction of the main channel axis, and the particles entering the channel by flow and emerge as particle fractions at the outlet end, the improvement which comprises withdrawing the flowstream consisting of carrier fluid and contained particles flowing along the channel axis through at least two outlets located at the outlet end of the channel, one of the outlet streams called the sample streams detecting the particle fractions emerging in the sample outlet substream, withdrawing the remaining fluid in the flowstream through one or more outlets consisting of one or more permeable wall sections whose combined areas constitute less than 25% of the total wall area of the channel, adjusting the relative flowrates of the different substreams to such proportions that the sample emerging in the sample outlet substrate is more concentrated than it is in the absence of flow through the permeable wall section or sections.

10. A process as in claim 9 wherein the particle fractions emerging from the sample outlet are collected.

11. An improved apparatus for the field flow fractionation comprising an elongated flow channel having an enclosed wall, means for applying a driving force in a direction perpendicular to the direction of the main channel axis, an inlet end and an outlet end, the improvement which comprises at least two separate inlets at the inlet end of the channel, one consisting of the sample inlet through which the sample inlet substream is introduced, and the remainder consisting of at least one permeable wall section, whose combined area constitutes of less than 25% of the total wall area of the channel, through which carrier fluid is introduced for the purpose of hydrodynamic relaxation.

12. An apparatus as in claim 11 wherein the enclosing wall includes both a depletion wall having an inlet end and an accumulation wall.

13. An apparatus as in claim 12 in which there is one permeable wall section located near the inlet end of the depletion wall.

14. An apparatus as in claim 12 in which there is a single permeable wall section located near the inlet end of the depletion wall.

15. An apparatus as in claim 12 wherein at least one permeable wall section is located near the inlet end of the accumulation wall.

16. An apparatus as in claim 12 in which the area of the permeable wall section is less than 10% of the total area of the enclosed wall.

17. An apparatus as in claim 12 wherein the said permeable wall section is made up of ceramic frit material having a pore size between 1 um and 20 um.

18. An apparatus as in claim 12 wherein the driving force is sedimentation.

19. An apparatus as in claim 12 wherein the driving force is generated by a temperature gradient.

20. An apparatus as in claim 12 wherein the driving force is an electrical field.

21. An apparatus as in claim 12 wherein the driving force is generated by a crossflow of fluid in the channel.

22. An apparatus as in claim 12 in which the permeable wall section has a chamber constructed on their backside opposite the channel that serves to distribute fluid over or collect fluid from the permeable wall area.

23. An apparatus as described in claim 12 in which at least one permeable wall element is located near the inlet end and at least one permeable wall element is located near the outlet end.

24. An improved apparatus for field-flow fractionation comprising an elongated flow channel having an enclosing wall, means for applying a driving force in a direction perpendicular to the direction in which the introduced fluid will flow in the channel, an inlet end and an outlet end, the improvement which consists of at least two separate outlets at the outlet end of the channel, consisting of the sample outlet through which the said sample outlet substream is withdrawn, and the remainder consisting of one or more permeable wall section, whose combined area constitute less than 25% of the total wall area of the channel, through which carrier fluid is withdrawn in order to increase the particle concentration in the sample outlet substream.

27. An improved apparatus for field-flow fractionation comprising an elongated flow channel having a permeable depletion wall and a permeable accumulation wall and a driving force wherein the driving force is generated by a crossflow of fluid and on the opposite side of the depletion wall is a flow chamber which extends almost the whole length of the depletion wall, said flow chamber being partitioned into at least 2 separate chambers by impermeable dams, each of the said chambers having its own means for flow ingress or egress.