The present disclosure provides an automatic separation apparatus for four fractions of heavy oil and a separation method thereof, wherein the apparatus includes a solvent reservoir tank (1), a separation unit for four fractions of heavy oil (100) and a receiving apparatus (9). The separation unit for four fractions of heavy oil (100) includes: a filter disc (4) having one end in communication with the solvent reservoir tank (1), and the other end in communication with an inlet of a pre-column flow path switching valve (5); a chromatographic column (6) having an inlet in communication with an outlet of the pre-column flow path switching valve (5), and an outlet in communication with an inlet of a post-column flow path switching valve (8). The receiving apparatus is in communication with an outlet of the post-column flow path switching valve (8).

A method for making a caffeoylquinic composition from a botanical source is disclosed. The method may include chromatographing an extract of biomass on an ion exchange stationary phase and obtaining an eluent comprising a caffeoylquinic composition. The biomass may be stevia or yerba mate, for example. The caffeoylquinic composition includes one or more of monocaffeoylquinic acid, dicaffeoylquinic acid, and salts of the foregoing.

The invention relates to a method for the separation of two hydrophilic neutral oligosaccharides from each other with a chromatography on a bromine functionalized polystyrene cross-linked with divinylbenzene (BPS-DVB) stationary medium.

A chromatography system is provided. The chromatography system is configured to process a feed fluid containing a plurality of components, wherein at least one component of the plurality of components of the feed fluid is a target component. The chromatography system comprises: a flow path comprising a plurality of fluid control components configured to control a fluid flow; a stationary phase, wherein the stationary phase is at least one membrane adsorber connected to the flow path and the stationary phase is configured to isolate the target component. The flow path is configured such that harvesting of the target component is optimized.

In some examples, a filter assembly may include a filter including a first gasket having a first channel adjacent to a first side of the filter and a second gasket having a second channel adjacent to a second side of the filter. The first gasket and the second gasket may include a beveled surface adjacent to the filter. The first channel and the second channel may include a diameter of from about 0.01 mm to about 0.5 mm. A finger tightening system may securely hold the filter without any leaks.

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 invention relates to a method for purifying a feed comprising at least one target product in a chromatography system having a plurality of purifying units, each having an inlet and an outlet, and a valve assembly having an outlet port and an inlet port. The inlet and the outlet of each purifying unit being connected to a respective port of the valve assembly. The method comprising loading (S10) the plurality of purifying units with feed provided through the inlet port of the valve assembly by sequentially connecting each purifying unit to the inlet port of the valve assembly: eluting (S12) the plurality of purifying units using an elution provided through the inlet port of the valve assembly by sequentially connecting each purifying unit to the inlet port of the valve assembly: and collecting (S14) the at least one target product from the outlet port of the valve.

This invention relates generally to a process for selective adsorption and recovery of lithium from natural and synthetic brines, and more particular to a process for recovering lithium from a natural or synthetic brine solution by passing the brine solution through a lithium selective adsorbent in a continuous countercurrent adsorption and desorption circuit.

This invention relates generally to a process for selective adsorption and recovery of lithium from natural and synthetic brines, and more particular to a process for recovering lithium from a natural or synthetic brine solution by passing the brine solution through a lithium selective adsorbent in a continuous countercurrent adsorption and desorption circuit.

This invention relates generally to a process for selective adsorption and recovery of lithium from natural and synthetic brines, and more particular to a process for recovering lithium from a natural or synthetic brine solution by passing the brine solution through a lithium selective adsorbent in a continuous countercurrent adsorption and desorption circuit.