The present invention relates to a method and production system for dealcoholization of beverages such as beers and wines.

A method of operating a chromatography column is described for use in methods of manufacture for producing anti-IL-12/IL-23p40 antibodies, e.g., the anti-IL-12/IL-23p40 antibody STELARA® (ustekinumab). This method involves collecting column outlet signal and accumulated flow parameters at two or more intervals of at least one mobile phase transition front during operation of the chromatography column comprising column packing. A model gamma cumulative distribution curve is calculated based on the collected column outlet signal and accumulated flow parameters for the at least one mobile phase transition front. A height equivalent theoretical plate (HETP) value is calculated for the at least one mobile phase transition front using parameters of the model gamma cumulative distribution curve and the quality of the chromatography column packing is assessed based on the calculated HETP value.

The present invention provides a method for hydrophobization of a hydrophilic material, the method including introducing a hydrophobic group into a hydroxyl group (—OH group) on a surface of the hydrophilic material. A method for hydrophobization of a hydrophilic material, the method comprising reacting a hydrophilic material to be hydrophobized with a hydrophobic group-containing silylating agent in presence of an amino acid as a reaction accelerator, to introduce a hydrophobic group-containing silyl group to a surface of the hydrophilic material. A hydrophobized silica gel column filler is produced by using the method. Further, a hydrophobized silica gel column is produced by filling a column with the hydrophobized silica gel column filler.

Systems and methods for automatically packing resin into and unpacking resin from a reusable separation column for sample analysis are described. A reusable sample separation column embodiment includes, but is not limited to, a column body having a first end and a distal second end and defining an interior fluid flow pathway; a first port adjacent the first end and coupled to an inlet coupled to an expanded interior region, the inlet positioned between the first port and the expanded interior region to introduce resin slurry; an outlet coupled to a frit positioned between the outlet and the first port, the frit configured to retain resin of the resin slurry within the expanded interior region; and a second port coupled to a channel having a smaller cross-section than the second port, the channel configured to introduce a jet of fluid to resin positioned in the expanded interior region.

Disclosed herein is a packing method for high efficiency chromatography columns starting from dry swellable particles, as well as columns packed by the method and the use of the columns in separation of biomolecules. In the packing method, an amount of dry swellable particles sufficient to give a swollen volume in a liquid of about 105-120% of the column chamber volume is transferred to the column, the column is closed and the liquid is provided to the column.

Liquid chromatography techniques are disclosed. Specifically, the liquid chromatography technique includes providing a liquid chromatography system having a coated metallic fluid-contacting element, and transporting a fluid to contact the coated metallic fluid-contacting element. Conditions for the transporting of the fluid are selected from the group consisting of the temperature of the fluid being greater than 150° C., pressure urging the fluid being greater than 60 MPa, the fluid having a protein-containing analyte incompatible with one or both of titanium and polyether ether ketone, the fluid having a chelating agent incompatible with the one or both of the titanium or the polyether ether ketone, and combinations thereof

A process for producing a TCH stream, the process comprising: separating, in a first column, an adiponitrile process stream comprising TCH and optionally adiponitrile, to form an adiponitrile stream comprising greater than 5 wt. % adiponitrile and a first TCH stream comprising TCH, and optionally a heavies stream comprising high-boiling components and solid impurities; and optionally purifying the first TCH stream, via one or more columns, to form a purified TCH stream comprising greater than 50 wt. % TCH; wherein the first column is operated at a pressure drop less than 25 mmHg.

An extracellular vesicle separation method, a colloidal particle, and a preparation method thereof are provided. The colloidal particle is used for extracellular vesicle separation, and includes 2 wt % to 6 wt % of agarose. The colloidal particle has a particle size of 25 μm to 500 μm, and is surface-modified with biocompatible molecules. The biocompatible molecules include sodium carboxymethyl cellulose (CMC), methyl cellulose (MC), glycine, aspartic acid, glutamic acid, bovine serum albumin (BSA), fetal bovine serum (FBS), or a combination thereof.

A particulate plug for removing a preservative from a solution, suspension, or emulsion comprising a drug is presented. The plug comprises microparticles of a hydrophobic polymer/fatty acid blend. The microparticles of hydrophobic polymer/fatty acid blend selectively absorb preservative allowing the drug to remain in solution for delivery.

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.