A method of recovering a sugar by separating a fermentation inhibitor and the sugar from a sugar solution containing the fermentation inhibitor, the method including: bringing the sugar solution containing the fermentation inhibitor into contact with a basic anion exchange resin filled into a column, followed by separation of the fermentation inhibitor and the sugar by a difference in retention time therebetween through use of water as an eluent, and separate recovery of a fraction containing the fermentation inhibitor and a fraction containing the sugar, wherein the basic anion exchange resin is previously treated with a solution containing the fermentation inhibitor.

A sample cartridge for a liquid chromatography device includes a microfluidic chip. A collector in the microfluidic chip includes a collector flow channel and a first window for acquisition of spectral data from a sample in the collector flow channel.

A single-use device for separating or purifying a large volume of a mixture of substances including membrane chromatography modules which are fixedly mounted in a predetermined grid and a line system for linking the membrane chromatography modules and for connecting the membrane chromatography modules to each other. A cover or bottom mechanism holding the membrane chromatography modules in position in a predetermined grid may be attached to the upper or lower side of the membrane chromatography modules. At least part of the line system is formed in the cover or the bottom mechanism, with connecting lines between the membrane chromatography modules. In a method of separating or purifying a large volume of a mixture of substances using such a single-use device having a plurality of automated valves and sensors connected to a control unit, the automated valves are controlled based on an evaluation of the parameters measured by the sensors.

The present disclosure provides a method for extracting and separating flavonoids from Lindera aggregata leaves. The method includes: mixing Lindera aggregata leaves with an adsorbent, conducting elution with a matrix solid-phase dispersion (MSPD) extraction method, followed by concentration to obtain a Lindera aggregata leaf extract; conducting primary separation and secondary separation on the Lindera aggregata leaf extract by high-speed counter-current liquid chromatography (HSCCC), to separate quercetin-3-O-β-D-arabinofuranoside, a mixture of quercetin-3-O-β-D-glucoside and quercetin-5-O-β-D-glucoside, quercetin-3-O-rhamnopyranoside, and kaempferol-7-O-α-L-rhamnopyranoside; where a second solvent system used in the secondary separation includes ethyl acetate, n-butanol, an addictive and water, and the addictive includes cyclodextrin. The method has a short separation period, high separation efficiency, and less impurities during purification and separation of the flavonoids from the Lindera aggregata leaves.

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.

The present invention relates to a method for separating one or more components from a liquid feed mixture in an EBA-SMB operating mode without the need of pumps at the outlets of the EBA columns. The present invention also relates to a simulated moving bed separation device with expanded bed adsorption columns which can be used in the method according to the invention.

Provided herein are, inter alia, biological manufacturing and downstream purification processes.

An optimization method for capturing proteins by multi-column continuous chromatography (MCC), including the following steps: step 1, under the conditions of a set loading protein concentration and an arbitrary load residence time, performing a single time of protein breakthrough experiment to obtain a protein breakthrough curve; step 2, under a set breakthrough percentage for a target protein, integrating the breakthrough curve to obtain a single-column loading capacity and establishing a linear relationship between the interconnected load time and the load residence time; step 3, solving for the optimal number of operating columns for capturing proteins by MCC based on step 2; step 4, solving for the optimal load residence time for capturing proteins by MCC based on step 2, step 3; and step 5, solving for the maximum productivity of capturing proteins by MCC based on step 4.

The present disclosure provides a macroporous noble metal catalyst and processes employing such catalysts for the regeneration of deactivated ionic liquid catalyst containing conjunct polymer.

The invention concerns a purification method comprising: providing a flow comprising a glycol, monovalent ions and multivalent ions; treating this flow with ion exclusion chromatography comprising: injecting the flow into a chromatographic unit comprising an ion exchange stationary phase; injecting an eluent into the chromatographic unit; collecting a fraction at the outlet of the chromatographic unit; the collected fraction being enriched with glycol and depleted of monovalent ions and multivalent ions relative to the flow.

The invention also concerns an installation adapted to implement this method, and its application to the regeneration of an anti-hydrate agent.