Direct capture using large bead chromatography media

A method of processing a process liquid using a set of mutually identical liquid chromatography columns, each of the mutually identical chromatography columns including a torus-shaped packed bed of beads, the process liquid containing biologics that are captured by the beads, the method comprising:

• feeding the process liquid, downstream from a process liquid creating source that is a cell culture vessel, the process liquid is fed to a subset of at least two columns of the set of mutually identical chromatography columns directly from the process liquid creating source without intermediate filtration or other clarification equipment and without harvest holding or a holding vessel, the process liquid being removed from a product by the subset of columns and exiting said subset of columns after having passed 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 micrometer-1 millimeter,
• the beads are hydrophilic,
• each of the liquid chromatography columns of the set of mutually identical liquid chromatography columns is configured to be radially passed through by the process liquid and includes the torus-shaped packed bed of beads configured to capture the product from the process liquid, the packed bed being held between an inner frit and an outer frit of the respective column, the outer frit being adjacent an axially extending external housing wall of the respective column, the inner frit being disposed closer to a central longitudinal axis of the respective column, a core member being disposed in the space delimited by the inner frit, the core member having an external wall delimiting an inner flow channel with the inner frit, the inner flow channel having a width along the entire length of the core member of at least 0.5 mm, the inner flow channel tapering in an axial direction from one end to an opposite end of the respective column along the core member, the outer frit through which the liquid to be processed enters the packed bed having a first surface area, the inner frit having a second surface area smaller than the first surface area, the respective column having an I/O ratio which is the ratio between the first surface area of the outer frit and the second surface area of the inner frit, the liquid to be processed flowing radially outward toward an inlet channel, being distributed across the surface of the outer frit, passing the outer frit, flowing radially inward through the packed bed to arrive at the inner frit, through the inner frit to the inner flow channel and axially downward toward the opposite end of the respective column, the columns of the subset of at least two of the columns are connected in series with each other, the process liquid being supplied to the most upstream column of the subset, flowing successively through the in-series connected columns, and leaving the subset through the most downstream column and after time elapse, when the most upstream column becomes saturated with product,
• wherein the method further comprises:
• repeatedly,
• disconnecting the most upstream column from the subset and removing the most upstream column from the series connection, and
• adding a replacement column from the set to the subset such that the replacement column is connected in series downstream from the most downstream column of the subset, and
• off-line processing the disconnected column to reset the packed bed of the disconnected column such that the disconnected column is configured to become saturated again by being reconnected in series as the most downstream column of the subset,
• wherein the most upstream column of the subset is connected directly to a cell culture exit of the cell culture vessel in which cell culturing takes place, the cell culture vessel containing between 1,000 and 10,000 liters of mixture of cell culture media and the crude CHO cell culture harvest, and
• wherein, for each of the columns:
• the I/O ratio is at least 1.5:1 and not more than 5:1, such that the first surface area is at least 1.5 and not more than 5 times the second surface area,
• the bed height is at least 10 and not more than 200 millimeters,
• the bed volume is at least 10 milliliters and not more than 20 liters,
• the diameter of the inner frit is at least 10 and below 150 millimeters, and
• the outer flow channel delimited outside the outer frit has a width at least 0.5 millimeters and the inner flow channel has a width that equals the outer flow channel width times the actual I/O ratio.