# US 11,027,220 B2 · Chromatography columns and processes > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 11,027,220 B2 - Document ID: US11027220B2 - Status: Granted - Kind: B2 - Application number: 16/587,268 - Filed: 2019-09-30 - Published: 2020-01-23 - Granted: 2021-06-08 - Earliest claimed: 2016-03-18 - Assignees: Biotechflow Ltd - Applicants: Biotechflow Ltd - Inventors: Martin John Hofmann - Web page: https://patentgrep.com/patent/US11027220B2 ## CPC - B01D 15/1807: {using counter-currents, e.g. fluidised beds} - B01D 15/22: relating to the construction of the column - B01D 15/265: {Adsorption chromatography} - C07K 1/22: Affinity chromatography or related techniques based upon selective absorption processes - G01N 30/6004: {end pieces} - G01N 30/56: Packing methods or coating methods - G01N 30/6017: {Fluid distributors} - B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28) - C07K: PEPTIDES (peptides in foodstuffs A23; obtaining protein compositions for foodstuffs, working-up proteins for foodstuffs A23J; preparations for medicinal purposes A61K; peptides containing beta-lactam rings C07D; cyclic dipeptides not having in their molecule any other peptide link than those which form their ring, e.g. piperazine-2,5-diones, C07D; ergot alkaloids of the cyclic peptide type C07D519/02; macromolecular compounds having statistically distributed amino acid units in their molecules, i.e. when the preparation does not provide for a specific; but for a random sequence of the amino acid units, homopolyamides and block copolyamides derived from amino acids C08G69/00; macromolecular products derived from proteins C08H1/00; preparation of glue or gelatine C09H; single cell proteins, enzymes C12N; genetic engineering processes for obtaining peptides C12N15/00; compositions for measuring or testing processes involving enzymes C12Q; investigation or analysis of biological material G01N33/00) - G01N: INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES (measuring or testing apparatus or processes other than immunoassay, involving enzymes or microorganisms C12M, C12Q) ## Abstract A separation column for expanded bed adsorption comprises a column tube (2), a base (15) carrying an inlet rotor structure (6) for pumping in process liquid, and a top cap (3). The top cap (3) is conical in form, and has a peripheral flange 31 by which it is rigidly fixed to the top edge flange (22) of the column tube (2). The angle of the convergent interior surface (35) of the conical top cap (3) may be between 10 and 25°. A vortex-inhibitor component (8) projects down below the outlet structure (4) at the top of the cap, projecting into the operating space (15) of the column to inhibit rotation of liquid in the column interior. An expanded bed adsorption process is done with upward flow of liquid in the column through a bed of media particles. ## Claims ### Claim 1 Separation apparatus in the form of a chromatography column for expanded bed chromatography, the column having a top and a bottom and comprising: a vertical column tube having a cylindrical side wall and defining an operating space to contain a bed of particles for expanded bed chromatography in use; bottom inlet structure at the bottom of the column where process liquid, containing a cell culture product including insoluble solid material, enters the operating space and fluidises the bed of particles by upflow through the operating space; and a generally conical fixed cap plate fixed at the top of the column tube side wall to close off the top of the column, the fixed cap plate being exterior to the column tube, in that it does not extend or project inside the column tube side wall, the fixed cap plate having a peripheral fixing portion which is fixed around a top edge of the column tube side wall and has a downwardly-directed fitting surface, the column tube side wall having an upwardly-directed fitting surface, and said downwardly-directed fitting surface and said upwardly-directed fitting surface fitting together; the inner side of the fixed cap plate being an interior upwardly convergent flow surface facing onto the operating space and leading towards an outlet structure, the outlet structure being positioned centrally in the fixed cap plate, whereby said process liquid containing said insoluble solid material of the cell culture product flows up through the operating space and radially inwardly, in contact with the convergent flow surface of the fixed cap plate, from the periphery of the column tube to the outlet structure for the liquid and insoluble solid material to leave the operating space after passing through the bed of particles the convergence of the interior convergent flow surface being at an angle from 10° to 25° relative to horizontal. ### Claim 2 (depends on 1) Separation apparatus according to claim 1 in which the fixed cap plate is fixed to the column tube by threaded fasteners or clamps. ### Claim 3 (depends on 1) Separation apparatus according to claim 1 in which said downwardly- and upwardly-directed fitting surfaces are radial and perpendicular to an axis of the column tube. ### Claim 4 (depends on 1) Separation apparatus according to claim 1 in which the interior convergent flow surface of the fixed cap plate is convergent from the periphery of the fixed cap plate to the outlet structure. ### Claim 5 (depends on 1) Separation apparatus according to claim 1 in which the convergence of the interior convergent flow surface is conical. ### Claim 6 (depends on 1) Separation apparatus according to claim 1 in which the convergence of the interior convergent flow surface is at an angle from 15° to 20°. ### Claim 7 (depends on 1) Separation apparatus according to claim 1 in which the fixed cap plate consists essentially of a single conical piece comprising said peripheral fixing portion for fixing to the column tube around a top edge of the side wall thereof. ### Claim 8 (depends on 1) Separation apparatus according to claim 1 in which the outlet structure comprises a discrete conduit component fixed into the fixed cap plate. ### Claim 9 (depends on 1) Separation apparatus according to claim 1 in which the outlet structure comprises a formation for inhibiting rotational flow. ### Claim 10 (depends on 9) Separation apparatus according to claim 9 in which the formation for inhibiting rotational flow comprises one or more vanes extending both axially and radially. ### Claim 11 (depends on 9) Separation apparatus according to claim 9 in which the formation for inhibiting rotational flow projects below the convergent flow surface of the fixed cap plate, down into the operating volume. ### Claim 12 (depends on 9) Separation apparatus according to claim 9 in which the formation for inhibiting rotational flow is comprised in a vortex inhibitor structure having one or more vanes and a downwardly-directed axial nose portion below the level of said one or more vanes. ### Claim 13 (depends on 12) Separation apparatus according to claim 12 in which the vortex inhibitor structure extends down below the outlet structure at least to the axial position where the fixed cap plate begins to converge. ### Claim 14 (depends on 1) Separation apparatus according to claim 1 in which the bottom inlet structure defines an array of process liquid injection holes distributed across the column tube. ### Claim 15 (depends on 1) Expanded bed adsorption separation process carried out in separation apparatus according to claim 1, the method comprising: providing a bed of particulate medium in the operating space in the column tube; causing a process liquid, the process liquid containing a cell culture product including insoluble solid material, to flow up through the column tube, from the bottom inlet structure to the outlet structure, through the bed of particulate medium with expansion of the bed; causing said process liquid containing said insoluble solid material of the cell culture product, having flowed up through the operating space, to flow radially inwardly in contact over the convergent flow surface of the fixed cap plate from the periphery of the column tube to the outlet structure where the process liquid including said insoluble solid material leaves the operating space, and separating a target substance from the process liquid by adsorption onto the media particles. ### Claim 16 Separation apparatus in the form of a chromatography column for expanded bed chromatography, the column having a top and a bottom and comprising: a vertical column tube having a cylindrical side wall and defining an operating space to contain a bed of particles for expanded bed chromatography in use, there being no mesh retainer for particles in the operating space at the top of the column; bottom inlet structure at the bottom of the column for process liquid to enter the operating space and fluidise the bed of particles by upflow through the operating space; and a generally conical fixed cap plate fixed at the top of the column tube side wall to close off the top of the column, the inner side of the fixed cap plate being an interior upwardly convergent conical flow surface facing onto the operating space and leading towards an outlet structure defining an outlet opening, the outlet structure being positioned centrally in the fixed cap plate whereby said process liquid flows up through the operating space and radially inwardly, in contact with the convergent conical flow surface of the fixed cap plate, from the periphery of the column tube to the outlet structure for said liquid to leave the operating space through the outlet opening after passing through the bed of particles, the convergence of the interior convergent conical flow surface being at an angle from 10° to 25° relative to horizontal, and the outlet structure comprising a vortex inhibitor structure to inhibit rotational flow of said liquid leaving the operating space through the outlet opening, the vortex inhibitor structure comprising one or more vanes extending both axially and radially, and projecting down below the outlet opening into the operating space. ### Claim 17 (depends on 16) Separation apparatus according to claim 16 in which the vortex inhibitor structure comprises a downwardly-directed axial nose portion extending down below said one or more vanes. ### Claim 18 (depends on 16) Separation apparatus according to claim 16 in which the vortex inhibitor structure comprises a downwardly-directed axial nose portion extending down below the outlet opening at least down to the axial position where the fixed cap plate begins to converge upwardly. ### Claim 19 Separation apparatus in the form of a chromatography column for expanded bed chromatography, the column having a top and a bottom and comprising: a vertical column tube having a cylindrical side wall and defining an operating space to contain a bed of particles for expanded bed chromatography in use, there being no mesh retainer for particles in the operating space at the top of the column; bottom inlet structure at the bottom of the column for process liquid to enter the operating space and fluidise the bed of particles by upflow through the operating space; a generally conical fixed cap plate fixed at the top of the column tube side wall to close off the top of the column, the inner side of the fixed cap plate being an interior upwardly convergent conical flow surface facing onto the operating space and leading towards an outlet structure defining an outlet opening, the outlet structure being positioned centrally in the fixed cap component whereby said process liquid flows up through the operating space and radially inwardly, in contact with the convergent conical flow surface of the fixed cap plate, from the periphery of the column tube to the outlet structure for said liquid to leave the operating space through the outlet opening after passing through the bed of particles, the convergence of the interior convergent conical flow surface being at an angle from 10° to 25° relative to horizontal, and the outlet structure comprising a vortex inhibitor structure to inhibit rotational flow of said liquid leaving the operating space through the outlet opening, the vortex inhibitor structure comprising: one or more vanes extending both axially and radially, and projecting down below the outlet opening into the operating space, and a downwardly-directed axial nose portion extending down below the outlet opening at least down to the axial position where the fixed cap plate begins to converge upwardly.