Chromatography columns, systems and methods

Abstract

The present invention relates to axial flow chromatography columns, methods for separating one or more analytes in a liquid by the use of such columns, and systems employing such columns. The column comprises a first port and a second port, the first port and said second port being at essentially the same level or elevation above the level of the bed space on the chromatography column.

Claims

1. An axial flow chromatography column comprising: a housing comprising a side wall; opposed, axially spaced first and second end units separated by said side wall; the first end unit comprising a first port which is in fluid communication with an enclosed bed space for adding a liquid to or removing a liquid from the bed space; the second end unit comprising a second port which is in fluid communication with the enclosed bed space for adding a liquid to or removing a liquid from the bed space; and wherein said first port and said second port are disposed at or above the level of the bed space on said chromatography column.

2. The chromatography column according to claim 1, wherein the second port is in fluid communication with the bed space by means of a hollow member connected to a passageway in the second unit.

3. The chromatography column according to claim 2, wherein said hollow member is an integral part of the column.

4. The chromatography column according to claim 2, wherein said passageway extends from the bed space through a lateral wall of the second end unit.

5. The chromatography column according to claim 1, wherein the first end unit additionally comprises a valve which is in fluid communication with the enclosed bed space, the valve being operably openable and closable to allow filing of the bed space with the particulate medium through a passageway.

6. The chromatography column according to claim 5, wherein a longitudinal member of said valve comprises a nozzle.

7. The chromatography column according to claim 6, wherein said nozzle is fixed within the bed space or retractable to a position outwith the bed space.

8. The chromatography column according to claim 5, wherein said valve does not allow emptying of the bed space of particulate medium.

9. The chromatography column according to claim 1, wherein said column is pre-packed with particulate medium.

10. The chromatography column according to claim 9, wherein said column is a disposable column.

11. The chromatography column according to claim 1, further comprising a first filter which is adjacent to said first end unit and a second filter which is adjacent to said second end unit wherein said filters together with the side wall define an enclosed bed space for containing a bed of particulate medium therein.

12. The chromatography column according to claim 1, further comprising at least one distribution channel therein.

13. The chromatography column according to claim 12, wherein said at least one distribution channel comprises a transverse distribution channel.

14. The chromatography column according to claim 1, wherein at least one of the housing, the first end unit, the second end unit, the first port and/or the second port comprise stainless steel or a high-strength/reinforced polymeric material.

15. The chromatography column according to claim 14, wherein the polymeric material comprises polypropylene.

16. A method for separating one or more analytes in a liquid from each other, comprising applying said liquid containing said one or more analytes to an axial chromatography column according to claim 1, said column containing a bed of particulate medium therein, eluting said one or more analytes with a mobile phase, and collecting fractions of said mobile phase eluting from the column.

17. A system for separating one or more analytes in a liquid from each other, said system comprising: an inlet or inlet manifold in fluid communication with said liquid; a pump; a chromatography column according to claim 1; and an outlet or outlet manifold.

18. A system according to claim 17, additionally comprising a valve which is operably openable and closable to allow the addition of liquid to, or the removal of liquid from, the column bed space.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 is a schematic transverse sectional view of a chromatography column of the prior art showing the basic features thereof.

(2) FIG. 2a, FIG. 2b and FIG. 2c are simplified schematic diagrams illustrating prior art (FIGS. 2a and 2b) columns and a column in accordance with the invention (FIG. 2c).

(3) FIG. 3 is a transverse section of a column in accordance with the invention.

(4) FIG. 4 is a three-dimensional schematic of a chromatography column according to the invention.

(5) FIG. 5 a is a schematic diagram of a system using a column known in the prior art.

(6) FIG. 5b is a schematic diagram of a system employing a column in accordance with the invention.

(7) FIG. 6 is a chromatogram showing the chromatographic separation of acetone on a chromatography column according to the invention, both in upflow (dotted line) and downflow (solid line) mode.

(8) FIG. 7 describes a method for calculating the reduced plate height and asymmetry factor from an eluted peak.

DETAILED DESCRIPTION OF THE INVENTION

(9) FIG. 1 shows schematically the general components of a chromatography column 1 as known from the prior art (for example, see FTS 6,524,484). The column has a cylindrical fluid-impermeable side wall 11, e.g. of stainless steel or a high-strength/reinforced polymeric material which may be translucent. The open top and bottom ends of the side wall 11 are closed by top and bottom end assemblies or units 12, 13. Each end unit has a fluid-impermeable end plate 3 fitting sealingly to plug the opening of the cylindrical wall 11, and preferably made of stainless steel or high-strength engineering plastics material, e. g polypropylene. The end plates are backed up by metal retaining plates 2 bearing against their outer surfaces and projecting radially beyond the side wall as retaining flanges 22 through which adjustable tension rods 14 are secured. These link the top and end assemblies 12, 13 and help the construction to withstand high fluid pressures.

(10) Each end plate 3 has a central through-opening 31 for communication between the exterior of the column and the packing bed space 9 defined by the side wall 11 and end assemblies 12, 13. Access through the opening 31 is subdivided into separate conduits, connected externally through a connection manifold 8.

(11) A filter layer 4, typically of filtered or woven plastics or steel, extends across the area of the bed space 9 at the inner surface of the end plate 3. The inner surface 35 of the end plate 3 is recessed behind the filter layer 4, e.g. conically as illustrated, and preferably with the use of support ribs (not indicated) supporting the filter layer 4 from behind, to define between them a distribution channel 34. One of the communication conduits, a mobile phase conduit 33, opens inwardly into this distribution channel 34, as well as outwardly to a mobile phase connector 81 of the manifold 8.

(12) From the manifold 8, an access valve device 5 projects inwardly through the end plate opening 31 and sealingly through a central orifice 41 of the filter layer 4. The access valve 5, governs the communication of one or more conduits from the manifold 8 directly to the bed space 9, i.e. bypassing the filter layer 4. Indicated here are first and second valved conduits 51, 61 governed by the valve 5, and connected externally through connectors 82 of the manifold 8.

(13) In a typical operation of the column, a packed bed of particulate stationary phase material fills the bed space 9 between the top and bottom filter layers 4. The valve devices 5 being closed, a mobile phase is fed in through mobile phase connector 81 (arrow A), passes through conduit 33 into the distribution channel 34 and through the filter layer 4 to elute down through the packed bed, effecting separation of its components or analytes. Liquid eluate passes thought the filter layer 4 of the bottom end assembly 13 and out through the mobile phase connector 81 thereof (arrow B) for collection as appropriate. While this is an example of downflow chromatography, in that chromatographic separation is effected by the downward movement of the mobile phase through the column, the skilled person will understand that separation may alternatively be achieved by upflow chromatography, simply by pumping mobile phase upwards through the column and thus reversing the direction of flow. In this mode, mobile phase would enter the column at connector 81 (arrow B), move upwards through the stationary phase or particulate medium, and be collected from connector 81 (arrow A) at the top of the column.

(14) When installing the column, it is essential to avoid any draining of the column from liquid as well as to avoid introduction of air into the column and the packed bed, respectively. Furthermore, it may be necessary to purge the system employing the column of any air upstream of the column. This is achieved by means of a vent valve 5 which is located at the bottom of the column.

(15) FIG. 1 and the above explanation are to illustrate general relationships of components and a typical mode of operation. The skilled person will understand, and it will also appear from the following description, that other specific constructions and modes of operation may be appropriate for different kinds of process.

(16) FIGS. 2a and 2b show simplified and schematic representations of the configuration of a prior art column. The column 101 has a first port 133 and a second port 140 for the introduction or collection of mobile phase. After installation of the column and prior to use, air needs to be removed from the column by means of venting/purging. This may be achieved by means of a vent valve 105 with a vent outlet which is either an integral part of the column 101 (as shown in FIG. 2b) or is connected to it at a point beyond the second port 140 (not shown in FIG. 2a).

(17) FIG. 2c is a simplified and schematic representation of a configuration of a column 101 in accordance with the invention. The first port 133, which is intended for the introduction or collection of mobile phase, is located at the top of the column 101 (as with columns of the prior art). The second port 140, which is in fluid communication with the bottom of the column, is at essentially the same level or elevation as the first port 133. This is achieved by means of a hollow member 160 which allows fluid such as air or mobile phase to flow between the bottom of the column 101 and second port 140. This configuration eliminates the need for a vent valve and reduces the risk of both siphoning from the column and introducing air into the column.

(18) FIG. 3 shows a transverse sectional view of a column in accordance with the invention. The column 201 comprises a tubular housing 211, a first end unit 212 (partially shown) and a second end unit 213, secured together to form a fluid tight seal by means of tension rods 214 with heads 216. First filter 204 and second filter 206 are adjacent to the first end unit 212 and second end unit 213, respectively. These filters 204, 206, together with side wall 211, define a bed space 209 for containing a bed of particulate medium.

(19) The housing 211 and end units 212, 213 are typically composed of stainless steel or a high-strength plastic material such as polypropylene. In a preferred embodiment, where the column is to be used for the separation of biologically active substances, the material is biologically inert such that it does not elicit an immune response in humans in accordance with United States Pharmacopia (PTSP) <88> class VI. Tension rods 214, with heads 216, secure the end units 212, 213 to the housing 211 to form a fluid-tight bed space 209 which is capable of withstanding high operating pressures.

(20) Valve means 220 and first port 233 are shown in the figure. The second port 240 comprises a passageway 242 which extends through second end unit 213 to, and is in fluid communication with (via hollow member 260), bed space 209 from which liquid can be added or collected. As is evident from the figure, the second port 240 is at essentially the same level or elevation as the first port 233, thus facilitating the addition and collection of mobile phase to/from the column. This arrangement has further advantages in that it assists in the installation of the column, decreases the risk of syphoning and reduces the likelihood of introduction of air into the column.

(21) The column can be packed with particulate medium in the form of a slurry through valve means 220, the valve means 220 comprising a central bore 221 and nozzle 224. A bed of packed particulate medium is obtained by conventional means well known in the art, for example by the movement of one of the end units to compress the bed. In FIG. 3 the nozzle 224 is shown in its retracted position but it will be understood that it can be moved to a position within the bed space 209 to facilitate filling of the column. A wide range of nozzles can be used which facilitate the distribution and even packing of slurry within the bed space. One alternative for achieving an open/closed functionality at the packing valve and nozzle respectively is to have a nozzle that is fixed in the bed space (and thus not retractable) and located adjacent to a moveable element or sleeve on the inside or outside of the nozzle that opens and/or closes the nozzle depending upon its position. Filters 204, 206 are each positioned on the interior face of the end units 212, 213 and act to define the bed space (together with side wall 211) and to prevent leakage of particulate medium from the bed space 209.

(22) Mobile phase or liquid containing one or more analytes or substances for separation on the column is added via first port 233. The liquid then passes through the filter 204 into the bed space 209 that is packed with particulate medium (not shown). Chromatographic separation of analyte(s) which has been introduced onto the particulate medium in this manner is effected by introduction of, and elution by, mobile phase. The mobile phase will finally exit the column through second filter 206 and via passageway 242 to second port 240. The resulting fractions of mobile phase, which contain different analytes, can then be collected.

(23) It will be understood by the skilled person that the column may be operated in either a downflow mode, as described above, or in an upflow mode where the direction of flow of the mobile phase is reversed such that it moves up the column. In upflow mode, mobile phase will enter the column via second port 240, move along passageway 242 and upwards through the bed of particulate medium in bed space 209, to exit the column for collection at first port 233.

(24) In the embodiment shown, hollow member 260 is an integral part of the column. However, it will be understood that by means of connectors and appropriate tubing made from a suitable material (e.g. polypropylene, polyurethane, etc.) that the hollow member 260 need not be integral to the column.

(25) The application and collection of mobile phase at the same elevation on a single end unit simplifies use, in terms of operator access and handling, reduces the risk of air accessing the system and decreases the space necessary to set up the column.

(26) The embodiment shown in FIG. 3 comprises a valve means (220) for the introduction and/or removal of particulate medium from the column. It will be understood that such a valve is not an essential feature of the claimed invention as some columns (e.g. pre-packed, disposable columns) may not require the addition or removal of particulate medium to be performed by the end user or are prepared (packed) with a different technique not requiring the use of such a valve means.

(27) FIG. 4 presents a three dimensional schematic representation of the column of FIG. 3, from which the external features of the column are evident. The column comprises a first end unit 312, second end unit 313 and housing 311 which are secured together to form a fluid-tight seal by tension rods 314 and heads 316. Particulate medium in the form of a slurry can be introduced into the bed space (not shown) via valve means 320. First port 333 serves as a conduit for mobile phase or liquid containing analyte(s) to be separated on the particulate medium. Hollow member 360, which is in fluid communication with the bed space via an outlet at the base of the column (not shown), ends in second port 340 from which appropriate fractions of mobile phase eluted from the column may be collected. As can be seen, second port 340 is at essentially the same level or elevation as the first port 333 through which mobile phase can be introduced (or collected). This arrangement facilitates user operation and sample handling. In the embodiment shown in FIG. 4, the capacity of the column is approximately 10 liters; it will be understood that a wide range of column capacities is possible, typically ranging from 0.1 to 2000 liters. Preferred capacities when using the column as a disposable column are in the range of 0.5 to 50 liters.

(28) FIGS. 5a and 5b schematically compare a system incorporating a prior art column (FIG. 5a) having an integrated vent valve to a system using a column in accordance with the invention (FIG. 5b). The vent valve shown in FIG. 5a is a rotary valve type, but it will be understood that other valve principles (pinch valves, membrane valves, etc) may also be employed to achieve the vent valve functionality.

(29) Following installation of the prior art system (FIG. 5 a), air must be removed from the system by priming it. The system comprises an inlet manifold 408, pump 470, sensors 472-476, column valve 407, outlet manifold 409 and column 401 (the dotted rectangle shown enclosing the column 401 and vent/purge valve 405 indicates that the column and the vent valve are used as a combined unit such that the vent valve is attached to the packed and primed column when installing the column in a chromatography system). As described above, the purpose of the vent valve is to protect the column from draining and/or the introduction of air when installing it in a system or when removing/disconnecting the column from a system. The column valve 407 controls connection of the column 401 to the inlet 408 and/or outlet 409 manifolds and thus governs whether the column 401 is offline or online. In FIGS. 5a and 5b, the column valve is of a rotary valve type, but it will be understood that other valve principles (e.g. pinch valves, membrane valves, etc) may also be employed to achieve the column valve functionality. Fluid connectivity with the column 401 and inlet 408/outlet 409 manifolds is controlled by means of several gateways within the valve 407 as indicated by positions 1-4 in the diagram). When valve 407 makes connection between positions 3 and 4 and positions 1 and 2, the column is bypassed. When the rotary valve is turned by 90 degrees, connection between positions 3 and 1 and in between positions 4 and 2 is made, which means that the column is inline or online and connected in upflow mode/flow direction. As explained above, other valve principles (e.g. pinch valves, membrane valves, etc) and a wide range of other valve configurations (upflow and/or downflow modes as well as connection of multiple columns) may be employed to achieve the column valve functionality.

(30) Air is removed from the system by means of vent/purge valve 405 which allows priming of the system, in particular priming of conduit 480, and purging of any air within it.

(31) The system shown in FIG. 5a is intended to be used in an upflow mode; thus liquid from inlet manifold 408 enters column 401 via conduit 480 at second port 440 and moves upwards through the packed bed (not shown) exiting at first port 420. Liquid (e.g. mobile phase or sample containing analytes to be separated on the column) is taken up from inlet manifold 408 and transferred to the column 401 under pressure by means of pump 470 via column valve 407. Sensors 472-476 can be used to measure environmental, physical and chemical conditions in the system (e.g. pressure, flow, conductivity, temperature, pH, LTV absorbance, air etc). These sensors can be used to control the operation of the column, for example by regulating flow rates of mobile phase through the column. Liquid emerging from the column from first port 420 is transferred via column valve 407 to outlet manifold 409 for collection.

(32) FIG. 5b exemplifies a system using a column in accordance with the invention. The component parts are the same as described above for FIG. 5 a except that there is no vent/purge valve 405. In this configuration the level or elevation of the first port 420 and the second port 440 above the level of the bed space (not shown) in the column is essentially the same, the second port 440 being connected to the base of the column 401 by means of hollow member 460. While hollow member 460 is part of the column in accordance with the invention, the corresponding liquid conduit 480 in FIG. 5a, which shows the prior art configuration, is part of the chromatography system. The column according to the invention with its hollow member 460 is already purged of air and may be ready for use when installed in the system. Especially for disposable, ready-to-use columns, the invention avoids the need for a disposable purge valve delivered with each individual column, which significantly reduces cost.

(33) Following installation, the system is purged upstream of the column valve 407 when the column 401 is bypassed (i.e. the column is offline). When switching the column inline, only a negligible volume of air will remain between the column valve 407 and conduit 480.

(34) The system shown in FIG. 5b can then be used in essentially the same manner as described above for the prior art system. In upflow mode, liquid will be aspirated from manifold 408 by pump 470 and directed, via valve 407, into second port 440 of column 401. The liquid will then move up the column through a bed of particulate medium (not shown) to exit at first port 420 and be directed, by column valve 407, to outlet manifold 409 for collection. Sensors 472-476 can be used to monitor environmental, physical and chemical conditions within the system and thus to regulate its operation.

(35) FIG. 6 shows the chromatographic separation efficiency by example of a tracer pulse experiment achieved on a 10 litre column in accordance with the invention, operated in both downflow (solid line) and upflow (dotted line) mode. The column was packed with a bed of CAPTO Q anion exchange resin (GE Healthcare, Uppsala, Sweden) of 85 pm agarose particle diameter. The column had a volume of 10.8 l, a diameter of 263 mm and a bed height of 200 mm. Acetone (1% of packed bed volume) was used as a tracer substance and eluted from the column using water as mobile phase and the absorbance monitored at 280 nm. As can be seen from Table 1 below, excellent column efficiency was observed with the 85 pm agarose medium used, either in downflow (solid line) or upflow (dotted line) mode.

(36) The data shown in Table 1 and FIG. 6 were obtained using a chromatography column in accordance with the invention which further comprises a transverse distribution channel and wherein the outlet of the first port and the transverse distribution channel have an asymmetric configuration. A chromatography column having such an arrangement is the subject of the Applicant's (GE Healthcare Bio-Sciences AB) copending patent application entitled Axial Chromatography Columns and Methods filed on the same day herewith as GB 0614316.8.

(37) TABLE-US-00001 TABLE 1 Observed Acceptance Plates/meter (N/m) 4430 >3700 (for 85 pm) Reduced plate height (h) 2.5 <3.0 Peak asymmetry (Af) 1.14 0.8-1.8
The data from Table 1 were derived from the chromatogram of FIG. 6 as described below.

(38) As a measure for column efficiency, the reduced plate height is determined with help of the peak width w.sub.h at half the height of the eluted peak, as shown in FIG. 7. This procedure is an approximation valid for the gaussian-shaped. In practice, eluted peaks often deviate from this ideal gaussian shape and peak skewness is described qualitatively by a so-called asymmetry factor A.sub.f, where leading in the RTD is indicated by A.sub.f<1 and tailing by A.sub.f>1. Commonly applied acceptance criteria for the asymmetry factor are 0.8<A.sub.f<1.5-1.8, depending on the type of application.

(39) $h=\frac{\mathrm{HETP}}{d_p}=\frac{L}{d_p}\frac{1}{5.54}{\left(\frac{w_h}{V_R}\right)}^2$$A_f=b/a$
(see FIG. 7)

(40) As a rule of thumb, the characteristic dispersion of the medium typically gives a reduced plate height in the range h=1.5-2.0 at an optimized superficial velocity when considering the highly porous medium used for protein chromatography in biotechnological downstream processing. The ideal efficiency of the medium has to be compared to the experimentally determined efficiency of the chromatographic system, where an increase in the reduced plate height is a result of additional dispersion from peripherals, sample volume, bed heterogeneities and distribution system. In practice, a typical standard installation qualification of a chromatographic unit used in ion exchange separations of proteins is an experimentally determined reduced plate height of h.sub.Unit,Apparent<3.0.

(41) A.sub.f asymmetry factor

(42) d.sub.p particle diameter

(43) h reduced plate height

(44) HETP height equivalent of a theoretical plate

(45) L bed height, packed bed

(46) u.sub.s superficial velocity in packed bed

(47) V.sub.R retention volume

(48) W.sub.h peak width at 50% of max. peak height

(49) It is apparent that many modifications and variations of the invention as hereinabove set forth may be made without departing from the spirit and scope thereof. The specific embodiments described are given by way of example only, and the invention is limited only by the terms of the appended claims.