DIRECT CAPTURE USING LARGE BEAD CHROMATOGRAPHY MEDIA

Abstract

Disclosed is a continuous process in which a subset of a number of mutually identical columns, are connected in series. The process liquid, e.g. crude cell culture harvest, is supplied to the most upstream column of the subset. It flows successively through the in series connected columns and leaves the subset through the most downstream and flows into the downstream collection vessel. As soon as the packed bed of the most upstream column is become saturated with product, this column is disconnected from the subset. It is removed from the series connection. A replacement, identical, column is added such that it is connected in series downstream from the most downstream column of the subset. This process is repeated.

Claims

1-15. (canceled)

16. Method of processing a process liquid using a set of mutually identical liquid chromatography columns, each column is for liquid chromatography comprising a torus shaped packed bed of beads, the process liquid containing biologics that are captured by the beads wherein as the first processing step downstream from the process liquid creating source, being a cell culture vessel, the process liquid is fed to a subset of at least two of the set of identical columns directly from the source without any intermediate filtration or other clarification equipment, nor any harvest holding-step or holding vessel and the process liquid, depleted by the subset of columns from the product of interest, is leaving said subset of columns after having flown radially through each of the columns of the subset of columns, wherein the process liquid is concentrated crude CHO cell culture harvest, the CHO cell diameter is approximately 0,1-10% of bead diameter, the bead diameter is approximately 120-500 micrometer, the beads are hydrophilic; each liquid chromatography column of the set is designed to be radially flown through by the process liquid and comprising the packed bed of beads designed to capture product from the process liquid, the packed bed held between an inlet and outlet frit of the column wherein the inlet frit through which the liquid to be processed enters the packed bed, has a first surface area and wherein the outlet frit through which the liquid exits the packed bed has a second surface area smaller than the first surface area, wherein the column has an I/O ratio which is the ratio between the surface area of the inlet frit and the surface area of the outlet frit, and wherein the liquid to be processed flows radially inward from the inlet frit towards the outlet frit; the columns of the subset of at least two columns are connected in series with each other and the process liquid is supplied to the most upstream column of the subset, flows successively through the in series connected columns and leaves the subset through the most downstream column and after time elapse, if the most upstream column is become saturated with product, the most upstream column is disconnected from the subset and removed from the series connection and a replacement column from the set is added to the subset such that a is connected in series downstream from the most downstream column of the subset and this process is repeated and the column removed from the subset is off-line processed to reset the packed bed of this column such that this column is made ready to become available for the subset to become saturated again by connecting this column in series as the most downstream column of the subset.

17. The method according to claim 16, wherein for each column the following applies: the I/O ratio is at least 1.5:1, and not more than 4:1, such that the first surface area is at least 1.5 and not more than 4 times the second surface area; the bed height is at least 10 and not more than 200 millimetre; the bed volume is at least 10 millilitre and not more than 20 litre; the diameter of the inner frit is at least 10 and below 150 millimetre; in the space delimited by the inner frit, a core member is located, the external wall of which delimits an inner flow channel with the inner frit; the outer flow channel delimited outside the outer frit has a width at least 0.5 millimetre and the inner flow channel has a width that equals the outer flow channel width times the actual I/O ratio.

18. The method according to claim 16, wherein the inlet and outlet frit comprise exactly three woven wire layers, mutually diffusion bonded, the filter layer directly exposed to the torus shaped packed bed, the layer providing the opposite face being a reinforcement layer, the layer in between being a dispersion or reinforcement layer.

19. The method according to claim 18, the inner and outer frit are made from exactly three layers of woven wires of stainless steel, directly laid on top of each other, and providing a pore size of at least 100 micrometre and the bed height is at least 20 and below 150 millimetre and the hydrophilic beads have a size between 200 micrometre and 1 millimetre and the I/O is below 3.5:1 such that the first surface area is at least 1.5 and not more than 3.5 times the second surface area.

20. The method according to claim 19, the filter layer of a frit is woven according to plain dutch weave.

21. Method of processing a process liquid using a set of mutually identical liquid chromatography columns, each column is for liquid chromatography comprising a torus shaped packed bed of beads, the process liquid containing biologics that are captured by the beads wherein as the first processing step downstream from the process liquid creating source, being a cell culture vessel, the process liquid is fed to a subset of at least two of the set of identical columns directly from the source without any intermediate filtration or other clarification equipment, nor any harvest holding-step or holding vessel and the process liquid, depleted by the subset of columns from the product of interest, is leaving said subset of columns after having flown radially through each of the columns of the subset of columns, wherein the process liquid is concentrated crude CHO cell culture harvest, the CHO cell diameter is approximately 0.1-10% of bead diameter, the bead diameter is approximately 120-500 micrometer, the beads are hydrophilic; each liquid chromatography column of the set is designed to be radially flown through by the process liquid and comprising the packed bed of beads designed to capture product from the process liquid, the packed bed held between an inlet and outlet frit of the column wherein the inlet frit through which the liquid to be processed enters the packed bed, has a first surface area and wherein the outlet frit through which the liquid exits the packed bed has a second surface area smaller than the first surface area, wherein the column has an I/O ratio which is the ratio between the surface area of the inlet frit and the surface area of the outlet frit, and wherein the liquid to be processed flows radially inward from the inlet frit towards the outlet frit; the columns of the subset of at least two columns are connected in series with each other and the process liquid is supplied to the most upstream column of the subset, flows successively through the in series connected columns and leaves the subset through the most downstream column and after time elapse, if the most upstream column is become saturated with product, the most upstream column is disconnected from the subset and removed from the series connection and a replacement column from the set is added to the subset such that it is connected in series downstream from the most downstream column of the subset and this process is repeated and the column removed from the subset is off-line processed to reset the packed bed of this column such that this column is made ready to become available for the subset to become saturated again by connecting this column in series as the most downstream column of the subset; wherein the most upstream column of the subset is connected directly to the cell culture exit of the cell culture vessel in which cell culturing takes place and which cell culture vessel contains between 1,000 and 10,000 litre of mixture of cell culture media and the crude CHO cell culture harvest and wherein for each column the following applies: the I/O ratio is at least 1.5:1 and not more than 3.5:1, such that the first surface area is at least 1.5 and not more than 3.5 times the second surface area; the bed height is at least 10 and not more than 200 millimetre; the bed volume is at least 10 millilitre and not more than 20 litre; the diameter of the inner frit is at least 10 and below 150 millimetre; in the space delimited by the inner frit, a core member is located, the external wall of which delimits an inner flow channel with the inner frit; the outer flow channel delimited radially outside the outer frit has a width at least 0.5 millimetre and the inner flow channel has a width that equals the outer flow channel width times the actual I/O ratio.

22. The method according to claim 21, wherein the inlet and outlet frit each comprise exactly three woven wire layers of stainless steel, mutually diffusion bonded and directly laid on top op each other, of which the filter layer provides and outer layer of the frit and which filter layer is directly exposed to the torus shaped packed bed, of which the layer providing the opposite outer face of the frit being a reinforcement layer, and of which the layer in between being a dispersion layer and each frit providing a pore size of at least 100 micrometre; and the bed height is at least 20 and below 150 millimetre and the hydrophilic beads have a size between 200 micrometre and 1 millimetre and the filter layer of a frit is woven according to plain dutch weave.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0053] The accompanying drawings, which are incorporated and form a part of the specification, illustrate an embodiment of the invention and, together with the description, serve to explain the principles of the invention. Shown is in:

[0054] FIG. 1-3 examples of the column in sectional side view;

[0055] FIG. 4 the column of FIG. 3 in top view;

[0056] FIG. 5 another column in perspective view from below, partly cut away;

[0057] FIGS. 6 and 13 two examples of a continuous process wherein a subset of three columns in series are applied;

[0058] FIGS. 7(a-d) and 8(a-c) illustrate weave patterns for a layer of a frit;

[0059] FIG. 9 a perspective, exploded view, of a prior art frit;

[0060] FIG. 10-11 sectional side views of prior art frits;

[0061] FIG. 12 a perspective view of a torus shaped filter bed.

DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0062] The following reference numbers are used: column 1; cylindrical housing wall 2; axial housing end plate 3; seal 4; liquid inlet 5; liquid outlet 6; packed bed 7; inner flow channel 8; packed bed fill opening 9; connector 10; fill tube 11 for packed bed; seal 12; seal 13; outer flow channel 14; core 15; inner frit 16; outer frit 17; axial bed end plate 18; distribution space 19; collector space 20; outflow channel 21; liquid outlet 22; bead height H; outer frit radius R1; inner frit radius R2; axial direction arrow A (FIG. 3). The radial direction is perpendicular to the axial direction.

[0063] Each of the liquid chromatography columns shown in FIG. 1-5 comprises: a housing, of cylindrical shape, defining a chamber therein and including a removable axial end plate 3 of circular shape; a first (outer) and second (inner) porous frits 16, 17 or membranes of cylindrical shape; a bed 7 or packing of particulate chromatographic separation material positioned intermediate said porous frits; optionally an axially extending core 15. The axially extending cylindrical external housing wall 2, first 17 and second 16 frit and core 15 are coaxial.

[0064] The first or outer frit 17 is adjacent the axially extending cylindrical external housing wall 2 and defines with said wall a cylindrical shaped ring type outer flow channel 14, e.g. 0.5 millimetre wide. The second or inner frit 16 is adjacent the core member 15 and defines with said core member a cylindrical or conical shaped ring type inner flow channel 8, e.g. 1.0 millimetre wide. In FIG. 1 a core member 15 is absent.

[0065] The axially top end plate 3 is, in an embodiment, penetrated by both a supply and exhaust channel 5, 6. These channels are coaxial with the frits.

[0066] The first and second frit can be part of a cartridge removably contained in the housing.

[0067] At both axial ends the first and second frit are connected by a radial extending end wall 18 closing the space between the first and second frit 16, 17 to capture the doughnut shaped packing providing the filter bed.

[0068] The filter bed 7 plus the core 15 almost completely fill the housing 1. Between the top face 18 of the filter bed 7 and the bottom face of the axial end plate 3 there is a distribution space 19 into which the outer flow channel 14 debouches. This distribution space possibly tapers in the radial outward direction and merges at the thus narrowed radial outer circumference with the circumferential extending outer flow channel 14. The circumferential inner flow channel 8, surrounding the core 15, tapers in the axial direction from the one to the opposite axial bed end plate 18 along the core 15 and merges at the lower end of the core with a collector space 20 delimited between the lower core end and the bottom end 3 of the housing or the end wall 18. This tapered shape of the inner flow channel 8, providing a wide and a narrow axial end, is due to the axial taper of the core. The taper of the distribution space 19 and of the inner flow channel 8 optimises flow characteristics. An outflow channel 21 extends lengthwise through the core 15 (FIG. 2) and connects to the liquid outlet 6 and the collector space 20.

[0069] FIG. 3 shows an embodiment wherein part of the liquid entering through liquid inlet 5 exits the column 1 without passing the outer frit 17, but in stead flows via the outer flow channel 14 to the liquid outlet 22, thus exits the column 1 without being processed. In an alternative embodiment such liquid outlet 22 could be absent and the outer flow channel 14 could be sealed at its axial end remote from space 19, e.g. by connecting the wall 18 to the wall 22.

[0070] The bottom end of the filter bed 7 contains a centrally located closable fill port 9, to supply the space between the frits 16, 17 with packing material for column packing purposes. This fill port 9 and associated seals and parts 10 and 11 could be absent, e.g. if the filter bed 7 is filled with packing material in a different manner.

[0071] O-ring type seals are applied to seal the core to the axial end plate and the filter bed and to seal the lid to the axial extending housing wall.

[0072] FIG. 7a shows plain weave (PL), FIG. 7b twilled weave (TL), FIG. 7c plain dutch weave (PDW), FIG. 7d twilled dutch weave (TDW). FIG. 8a shows reversed plain dutch weave (PZ), FIG. 8b reversed twilled dutch weave (KPZ), FIG. 8c five-heddle weave (FHD). FIG. 9 shows a four layer (from top to bottom: protective layer, filter layer, distribution layer, single reinforcement layer), FIG. 10 a five layer (double reinforcement layer) and FIG. 11 a six layer (triple reinforcement layer) frit. Compared to the frits of FIG. 9-11, a frit of the invention is obtained as follows: In case of FIG. 9, by cancelling one or both of the top and bottom most layer (as seen in the drawing). In case of FIG. 10 or FIG. 11 by cancelling at least one of the top layer (protective layer) and one, two or all of the reinforcing layers. FIG. 12 illustrates a bed segment taken from the torus shaped bed filter.

[0073] The column operates as follows: Fluid is introduced through the supply channel into the distribution space and from there flows radially outward towards the inlet channel. In the inlet channel the fluid flows axially downward to be evenly distributed across the complete surface of the outer frit. Then, passing the outer frit, the fluid flows radially inward through the packing to arrive at the inner frit. Subsequently the fluid flows evenly distributed across the complete surface of the inner frit through the inner frit to arrive into the outlet channel. The fluid flows axially downward through the outlet channel, along the outer face of the core to be collected in the collection space. From there the fluid flows into the exhaust channel. If the core contains the exhaust channel, e.g. as in FIG. 5, the fluid flows axially upward through the core.

[0074] Further embodiments are also covered by the attached claims. E.g. the flow direction of the introduced fluid can be opposite, for which the supply, exhaust, inlet and outlet elements are interchanged. Also different embodiments belong to the invention. Features of different in here disclosed embodiments can in different manners be combined and different aspects of some features are regarded mutually exchangeable. All described or in the drawing disclosed features provide as such or in arbitrary combination the subject matter of the invention, also independent from their arrangement in the claims or their referral. The drawing, the specification and claims contain many features in combination. The skilled person will consider these also individually and combine them to further embodiments.

[0075] Conclusion: preferably a liquid chromatography column, utilizing horizontal or radial flow of sample material passing there through, preferably in inward direction, comprising: a housing defining a chamber therein; a first and second axially or longitudinally extending porous frits positioned within said chamber of said housing; a bed or packing of, preferably particulate, chromatographic separation material positioned within said chamber of said housing and intermediate said porous frits, the first of said porous frits being adjacent said housing and an outer flow channel, the second of said porous frits being positioned adjacent an optional a core member and an inner flow channel; the bed is torus shaped; distribution means operatively connected to said outer flow channel; collector means operatively connected to said inner flow channel, said distribution means and said outer flow channel being constructed to direct associated material to be separated in said bed evenly across a longitudinal length of said bed in a substantially horizontal direction preferably said porous frits are coaxially positioned with respect to one another, said first porous frit having a larger cross-section than said second porous frit, and said core member is centrally located in said housing chamber.