The present invention provides rapid, sensitive high-throughput methods and systems for characterizing peptides or proteins using hydrophobic interaction chromatography-coupled native mass spectrometry to improve manufacturing process of biopharmaceutical products, such as identifying impurities during antibody purification, monitoring post-translational modification variants during production, or characterizing drug-to-antibody ratio of antibody-drug conjugates. The separation profiles of the peptides or proteins are generated and compared to identify or qualify the peptides or proteins.

Provided herein are methods of reducing bioburden of (e.g., sterilizing) a chromatography resin that include exposing a container including a composition including a chromatography resin and at least one antioxidant agent and/or chelator to a dose of gamma-irradiation sufficient to reduce the bioburden of the container and the chromatography resin, where the at least one antioxidant agent and/or chelator are present in an amount sufficient to ameliorate the loss of binding capacity of the chromatography resin after/upon exposure to the dose of gamma-irradiation. Also provided are reduced bioburden chromatography columns including the reduced bioburden chromatography resin, compositions including a chromatography resin and at least one chelator and/or antioxidant agent, methods of performing reduced bioburden column chromatography using one of these reduced bioburden chromatography columns, and integrated, closed, and continuous processes for reduced bioburden manufacturing of a purified recombinant protein.

The invention discloses a functionalised chromatography medium, comprising: i) at least one non-woven layer (10) of polymeric nano fibres (20) comprising a plurality of nanofibre-nano fibre fusion points (30); ii) a grafted polymer coating covering the polymeric nanofibres and the nanofibre-nanofibre fusion points; iii) a plurality of ligand groups covalently bound to the grafted polymer coating, wherein the ligand groups are capable of interacting with a target biomolecule.

A method for refining vasopressin, including: subjecting a crude vasopressin solution to reversed-phase enrichment, reversed-phase salt conversion and reversed-phase purification sequentially using reversed-phase high performance liquid chromatography. The crude vasopressin solution is obtained by oxidizing a crude reduced vasopressin prepared by solid phase synthesis. A super water-resistant packing material is used in the reversed-phase high performance liquid chromatography.

Chromatography resins having mixed mode ligands and methods of using such resins are provided.

Chromatography resins having mixed mode ligands and methods of using such resins are provided.

The present disclosure relates to a method for obtaining purified bacterial polysaccharides. The method comprises simultaneous removal of impurities as well as sizing of bacterial polysaccharides using an acid instead of conventional mechanical sizing methods. The method is simple, rapid and cost effective. The method results in high polysaccharide recovery and low impurity content. The purified polysaccharide obtained by the method of the present disclosure may be used for large scale production of polysaccharide-protein conjugate vaccines.

Chromatography resins having anionic exchange-hydrophobic mixed mode ligands and methods of using such resins are provided.

Chromatography resins having anionic exchange-hydrophobic mixed mode ligands and methods of using such resins are provided.

The present disclosure relates to, inter alia, a method of quantitating an amount of an antibody molecule from a mixture comprising two or more antibody molecules, comprising separating each of the two or more antibody molecules from the mixture by hydrophobic interaction chromatography high performance liquid chromatography (HIC-HPLC) and quantitating an amount of each antibody molecule, wherein the molecular weight of each antibody molecule is within 15 kDa of any other antibody molecule in the mixture and either each antibody molecule is different from another antibody molecule in the mixture by more than about 0.25 unit on the Kyte & Doolittle hydropathy scale or each of the antibody molecules when nm alone on HIC-HPLC elutes at distinct run time with little overlap from the other antibody molecules in the mixture, or both.