An isomerization feature-based method for purifying and preparing punicalagin is provided, wherein pomegranate peel extract is used as a raw material. The isomerization feature-based method avoids impurities contained in the punicalagin based on structural characteristics, for example, the punicalagin in the pomegranate peel extract has two mutually convertible isomers. In the isomerization feature-based method, a pilot-scale preparative liquid chromatography is used to obtain a large amount of the punicalagin having a purity higher than 98% from a complex pomegranate peel extract. The isomerization feature-based method is simple, an obtained punicalagin has high purities and a preparation is in a massive scale. The isomerization feature-based has a strong reference value for purification and preparation of compounds with isomerization features.

Disclosed is a method for preparing a composition comprising factor VIII (FVIII) and von Willebrand factor (vWF), wherein the content of the von Willebrand factor (vWF) can be controlled by mixing the factor VIII (FVIII) with the von Willebrand factor (vWF) at an appropriate ratio after separately purifying the factor VIII (FVIII) and the von Willebrand factor (vWF) from plasma in a single process. The method can prepare and purify a composition comprising factor VIII (FVIII) and a varying content of von Willebrand factor (vWF) without increasing the amount of impurities other than the von Willebrand factor (vWF) compared to a method of purifying factor VIII (FVIII) separately, without significantly increasing the processing time (within 3 hours) compared to a method of purifying factor VIII (FVIII), and without changing the yield of factor VIII (FVIII).

The present disclosure relates to methods of modifying complex extracts such that components or mixtures of components are selectively removed or added, thus providing a complex mixture that does not naturally occur with a refined or a tuned therapeutic or nutraceutical effect. In various aspects, the complex extract can be an extract obtained from one or more plants, e.g., an extract obtained from green tea leaves. The present disclosure pertains to compositions obtained by the disclosed methods, nutraceutical compositions comprising same, pharmaceutical compositions comprising same, and methods of treating various conditions, including physiological dysfunctions associated with elevated reactive oxygen species and/or inflammatory molecule, e.g., TNFα, expression using same. This abstract is intended as a scanning tool for purposes of searching in the particular art and is not intended to be limiting of the present disclosure.

A sample separation network includes a server node, a plurality of client nodes coupled with the server node, a plurality of sample separation devices coupled with the server node, wherein each of the sample separation devices includes device-specific control software configured for controlling specifically the respectively assigned sample separation device, wherein at least one of the server node and the client nodes includes generic control software configured for generically controlling sample separation devices in a non-device-specific way, and wherein at least one of the server node and the client nodes and the sample separation devices is configured for loading device-specific control software from a sample separation device to at least one of the server node and the client nodes upon connection of said sample separation device to the sample separation network.

A method for producing full spectrum hemp extract comprising extracting substances from cannabis-based green material that are soluble in an extraction solvent and collecting an extract that includes the extraction solvent distilling at least a portion of the extraction solvent which results in a concentrate that is not distilled off, removing at least a portion of water soluble substances from the concentrate by partitioning the at least a portion of water soluble substances into an aqueous phase and a remainder of substances from the concentrate into a partitioned concentrate, heating the partitioned concentrate to evaporate the nonpolar solvent and to yield a crude oil, degassing the crude oil by heating it which results in a degassed crude oil, performing a first pass distillation at about 150° C. and collecting a first residue, performing a second and third pass distillation at about 170° C. and about 185° C., and collecting a distillate from same.

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.

An analytical system comprises a chromatography column configured to separate a sample into one or more analytes; an ion removal device configured to remove at least ions of one charge from the mobile phase, the ion removal device fluidly coupled to an output of the chromatography column; an ion selective sensor configured to measure a signal corresponding to an activity of the ions of one charge in the mobile phase, the ion selective sensor fluidly coupled to an output of the ion removal device; an optional diverter valve that can interrupt the flow of the mobile phase; and a microprocessor configured to monitor the signal of the ion selective sensor and to either switch the optional diverter valve to interrupt the flow of the mobile phase or turn off the pump when the signal is greater than a predetermined threshold.

The present invention relates to a preparative chromatography system (200, 500, 800) and a chromatography process (400, 700) adapted to repetitive cycling of chromatography volumes. The system (200, 500, 800) comprises at least two upstream pumps (203a, 803a, 203b, 803b) and separate flow paths (220) from process liquid sources to the chromatography device (200, 500, 800). The system (200, 500, 800) is arranged to prime one flow path (220) with one process liquid while providing another process liquid to the chromatography device and thereby minimizing the hold-up volume of the system (200, 500, 800).

A method for obtaining a liquid from a porous solid phase is described. The method comprises forming a liquid seal at a first end of a porous solid phase to which a liquid is bound, wherein liquid of the liquid seal is immiscible with the liquid bound to the solid phase, and applying a pressure differential across the porous solid phase to cause the immiscible liquid to move through the porous solid phase towards a second end of the porous solid phase, thereby displacing the liquid bound to the porous solid phase towards the second end and releasing this liquid from the second end. Recovery of liquid from the solid phase using such methods is increased compared with corresponding methods in which no liquid seal is formed. In preferred embodiments, the liquid used to form the liquid seal is a mineral oil. The methods have particular application in nucleic acid extractions which utilize capture of nucleic acid to a solid phase. Kits and apparatus for performing the methods are also described.

A method for obtaining a liquid from a porous solid phase is described. The method comprises forming a liquid seal at a first end of a porous solid phase to which a liquid is bound, wherein liquid of the liquid seal is immiscible with the liquid bound to the solid phase, and applying a pressure differential across the porous solid phase to cause the immiscible liquid to move through the porous solid phase towards a second end of the porous solid phase, thereby displacing the liquid bound to the porous solid phase towards the second end and releasing this liquid from the second end. Recovery of liquid from the solid phase using such methods is increased compared with corresponding methods in which no liquid seal is formed. In preferred embodiments, the liquid used to form the liquid seal is a mineral oil. The methods have particular application in nucleic acid extractions which utilize capture of nucleic acid to a solid phase. Kits and apparatus for performing the methods are also described.