In various aspects, the present disclosure pertains to materials (e.g., kits, column assemblies, liquid chromatography systems, etc.) methods for performing liquid chromatography that employ a first column (e.g., a trapping column) and a second column (e.g., an analytical column). The first column comprises a first chromatographic material having a first chromatographic surface that comprises first hydrophobic surface groups and first ionizable surface groups having a first pKa value. The second column comprises a second chromatographic material having a second chromatographic surface that comprises second hydrophobic surface groups and (a) permanently ionized surface groups or (b) second ionizable surface groups having a second pKa value. The first hydrophobic surface groups have a hydrophobicity that is less than a hydrophobicity of the second hydrophobic surface groups. Moreover, where the second chromatographic surface comprises second ionizable surface groups, the first pKa value may differ from the second pKa value by 1-12 units.

A system for producing steam includes a source of superheated water with superheated water output; a membrane filtration system in fluid communication with the superheated water output and including a membrane filter with a permeate side and an opposing retentate side. The membrane filter includes a separation membrane constructed to reject organic molecules. The system may be used for removing organic compounds, such as anti-corrosion agents or contaminants, from superheated water to produce steam. A method for producing steam includes directing a cross-flow of heated pressurized water including a first concentration of an organic compound across a membrane filter. The membrane filter includes a separation membrane constructed to reject the organic compound; and one or more support layers adjacent the separation membrane. A steam permeate including a second concentration of the organic compound is collected, where the second concentration is lower than the first.

A chromatography device is provided comprising a filter housing having an inlet and an outlet and defining a fluid flow path between the inlet and the outlet; a porous filter arranged in the filter housing across the fluid flow path, the filter comprising first porous filter element; and a second porous filter element in contact with the first porous filter element, wherein the first porous filter element comprises at least one anionic exchange (AEX) layer, and the second porous filter element comprises at least one hydrophobic interaction (HIC) layer. A method of purifying nucleic acid using the device is also provided.

Methods of preparing steviol glycosides, including Rebaudioside D, Rebaudioside E, Rebaudioside M, Rebaudioside N and Rebaudioside O are provided herein. Sweetener and sweetened consumables containing Rebaudioside D, Rebaudioside E, Rebaudioside M, Rebaudioside N and Rebaudioside O are also provided herein.

A method of separating actinium and/or radium from proton-irradiated thorium metal. The thorium metal is irradiated to produce isotopes including thorium, actinium and/or radium. The resultant product is dissolved in solution and a selective precipitant is used to precipitate a bulk portion of the thorium. The precipitated thorium can be recovered. Chromatography is carried out on the remaining solution to remove residual thorium and to separate the actinium from the radium.

The invention relates to the field of separating rare earth elements by chromatography. The claimed method for separating lutetium and ytterbium from acidic solutions resulting from the recycling of irradiated ytterbium-176 targets is carried out using ion exchange chromatography. Ion sorption is performed on a sulphonic cation resin in copper or nickel form, and lutetium and ytterbium are eluted using a solution of a chelator at elevated temperature with the aid of a system consisting of at least two series connected columns of decreasing diameter, filled with a sulphonic cation resin. The separation of ytterbium and lutetium is carried out in the presence of a bivalent ion of a stable intercalator element selected from the group consisting of cobalt, lead or zinc, in an amount in mEq that is equal to not less than 80% of the total capacity of the last column in the direction of travel of the solution. A solution of ethylenediaminetetraacetic acid or nitrilotriacetic acid is used as the eluent. The technical result is that of increasing the degree of chromatographic separation of lutetium and ytterbium from acidic solutions resulting from, the recycling of ytterbium-176 targets, including targets having a mass greater than 10 g, as well as expanding the range of methods available for separating the aforesaid components.

Disclosed here are compositions comprising recombinant acid sphingomyelinase (rASM) having desired purity, specific activity, and/or rASM isoforms. Also provided are methods for making and purifying such compositions, comprising chromatography steps. Further provided are methods of modulating rASM specific activity in a composition, and methods of modulating rASM isoforms in a composition. The methods disclosed here can be particularly useful for manufacturing pharmaceutical compositions comprising rASM for treating acid sphingomyelinase deficiency (ASMD).

A waste extraction system that includes a column set positioned between and fluidly coupled to an upstream segment of a main waste pathway and a column effluent tank, the column set having a uranium adsorption column fluidly coupled to a supporting adsorption column along the main waste pathway. The uranium adsorption column is upstream the supporting adsorption column. The waste extraction system also includes a strip waste pathway extending from the uranium adsorption column to the column effluent tank bypassing the supporting adsorption column, an anion exchange resin housed in the uranium adsorption column, and a cation exchange resin housed in the supporting adsorption column.

A simulated moving-bed type chromatographic separation method including separating a weakly adsorptive component, a strongly adsorptive component, and an intermediately adsorptive component that has adsorptive property intermediate between the two components, with respect to an adsorbent, with two or more kinds of eluents by using a circulation system in which a plurality of unit packed columns each packed with an adsorbent are connected in series and in an endless form via pipes, the weakly adsorptive component, the strongly adsorptive component, and the intermediately adsorptive component being contained in a feed solution, wherein a feed solution supply port, eluent suply ports and a plurality of extraction ports are provided on the pipes of the circulation system, and positions of the feed solution supply port and the plurality of extraction ports are set to have a specified relationship; and a chromatographic separation system suitable for implementing the chromatographic separation method.

A cation exchange chromatographic matrix comprising a base material, and a copolymer with one monomer unit having at least a sulfonic acid group, the copolymer being immobilized on the base material, wherein: the copolymer forms substantially no cross-linked structure, and the copolymer comprises neither acrylamide nor an acrylamide derivative as a monomer unit, or comprises acrylamide or an acrylamide derivative as a monomer unit in a range which has no substantial influence; the ratio of the mass of the copolymer to the mass of the base material is 5% or more and 200% or less; and the density of the sulfonic acid group is higher than 30 mmol/L and 200 mmol/L or lower.