The invention relates to a separation matrix comprising at least 11 mg/ml Fc-binding ligands covalently coupled to a porous support, wherein: a) the ligands comprise multimers of alkali-stabilized Protein A domains, and b) the porous support comprises cross-linked polymer particles having a volume-weighted median diameter (d50,v) of 56-70 micrometers and a dry solids weight of 55-80 mg/ml.

Herein disclosed is an economical standalone system that replaces conventional monomer purification methods needed to perform chemical reactions that require reactants with a high degree of purity. Chemical reactions, such as anionic polymerization, can produce highly monodisperse homopolymers and block copolymers, however to do so they require very high purity reactants along with a moisture and oxygen free atmosphere. The system and method uses traditional column purification methods, but incorporates them into an economical, standalone, compact, and hazard free system. This method is different in view of safety, cost of cleaning procedure, time commitment, space availability, design and operational ease; helping researchers save time by cutting down the operating commitment by 90% and most importantly making it safer.

The present invention relates to a multimodal adsorption medium, in particular a multimodal chromatography medium, a method for its production, as well as use of the adsorption medium according to the invention or an adsorption medium produced according to the invention for the purification of biomolecules.

A process for removing iodine using gold particles includes contacting a solution including iodine, with gold particles. The iodine is adsorbed onto the gold particles and then removed. A device for removing iodine using gold particles includes gold particles in a stationary phase and is configured to contact a solution including iodine, with gold particles, to thus adsorb the iodine onto the gold particles and remove the iodine.

Ligand functionalized substrate including a solid substrate, which has been modified to provide grafted catching ligand groups covalently bound via a linker, methods of preparing the ligand functionalized substrate and the use thereof, such as to increase binding rate and the dynamic binding capacity (DBC).

A diatomite product and method of using such is disclosed. The diatomite product may comprise sodium flux-calcined diatomite, wherein the diatomite product has a crystalline silica content of less than about 1 wt %, and the diatomite product has a permeability between 0.8 darcy and about 30 darcy. In some embodiments, the diatomite product may be in particulate or powdered form. This disclosure also concerns flux-calcined silica products containing low or non-detectable levels of crystalline silica. Some of these products can be further characterized by high permeabilities and a measurable content of opal-C, a hydrated form of silicon dioxide.

There is provided a method of identifying a resin for isolating or enriching a protein of interest using affinity chromatography. The method comprises the steps of: i) providing the three-dimensional structure of the protein of interest; ii) determining and/or calculating one or more parameters of the protein of interest in its two- and/or three-dimensional form; iii) determining and/or calculating one or more parameters of one or more resin in their two- and/or three-dimensional form; and iv) selecting a resin expected to bind complementarily to the protein of interest based upon one or more of the parameters of the protein of interest.

The subject invention pertains to proteins are purified by a mixed-mode chromatography system formed by attaching a ligand with cation exchange and hydrophobic 1,3-droxoisoindolin-2-yl group functionalities to a large-pore support matrix, the only linkage between the ligand and the support matrix being a chain having a backbone of one, two, three, four, or five atoms between the hydrophobic group and the support matrix.

A separation medium for removing small molecules from biomacromolecule in aqueous mixtures comprises gel filtration chromatography beads having a nominal protein fractional range of about 1000 Da to about 5000 Da and having an internal adsorbent matrix derived from a hydrophobicized scaffold. The gel filtration chromatography beads remove small molecules that are less than 1500 Da and have log Pow values greater than about −0.5 from biomacromolecules in aqueous mixtures. Devices containing the separation medium are also provided.

This application discloses the method for separating element or isotopes such as protactinium and gallium and isotopes thereof from a corresponding mixture which method comprises contacting the mixture with a carbon-based separation material, wherein the carbon-based separation material selectively associates with the element or isotope thereof.