The present invention relates to a valve unit for a chromatography apparatus, the valve unit comprising a fluid inlet configured to receive an input fluid, a fluid outlet configured to provide an output fluid, a first pair of fluid ports configured to be coupled to a first column, a second pair of fluid ports configured to be coupled to a second column, a coupling valve assembly configured to direct fluid between a selection of the fluid inlet, the fluid outlet, the first pair of fluid ports and the second pair of fluid ports in response to one or more control signals, wherein the coupling valve assembly is configured to direct fluid using a selection of membrane valves coupled by fluid channels comprised in a body of the coupling valve assembly. The invention further relates to a chromatography apparatus comprising the valve unit and a membrane valve comprised in the valve unit.

A valve switching system for selectively interconnecting components of a bioprocess installation, comprising a valve switching cassette and an actuator block. It is proposed, that the valve switching cassette comprises a perforated sandwich plate with perforation holes, which sandwich plate is placed between the cassette manifold and the actuator block body.

An apparatus for a selective fractionation of ultrafine particles includes at least three separating columns fluidically connected in series by connecting lines. An infeed is arranged to feed into a connecting line which is arranged upstream of each separating column. Each connecting line comprises an inlet for a suspension of ultrafine particles to be separated and an inlet for at least one additional mobile phase. The inlets are alternately operated. A discharge branches off from a connecting line which is arranged downstream of each separating column. Each connecting line comprises an outlet for a first and a second discharge suspension of the ultrafine particles. The outlets are alternately operated. A control means provides a simultaneous switching of the through-flow switching position of the shutoff valves at the inlets and outlets. At least one magnetic field source for a magnetic field is arranged in each separating column.

A method for purification and separation of cannabinoids, such as cannabidiol and tetrahydrocannabinol, e.g., from dried hemp and cannabis leaves can use a continuous simulated moving bed process, a batch column chromatography method, or a single column, and a combination of one or more of a sequence of purification steps including: filtration, decolorization, activation or decarboxylation, dewaxing, polishing, and crystallization to separate a cannabinoid from the cannabis plant and to provide various cannabinoid products. The cannabinoid products can be used in various pharmaceutical and nutraceutical applications.

A method for operating a chromatography setup of a bioprocess installation with a plurality of chromatography columns, each with a column inlet and a column outlet, and a valve switching cassette with a group of inlet ports, a group of outlet ports, a group of column-in ports and a group of column-out ports . It is prosed, that a first liquid stream of concentrated buffer is introduced into a first internal liquid line via a first inlet port and that a second liquid stream of diluent is introduced into a second internal liquid line via a second inlet port, that in a dilution process, the array of valve units is switched as to create a third liquid stream by merging the first liquid stream and the second liquid stream at a merging location within the valve switching cassette.

A method for purification and separation of cannabinoids, such as cannabidiol and tetrahydrocannabinol, e.g., from dried hemp and cannabis leaves can use a continuous simulated moving bed process, a batch column chromatography method, or a single column, and a combination of one or more of a sequence of purification steps including: filtration, decolorization, activation or decarboxylation, dewaxing, polishing, and crystallization to separate a cannabinoid from the cannabis plant and to provide various cannabinoid products. The cannabinoid products can be used in various pharmaceutical and nutraceutical applications.

Compositions and methods for isolating L-glufosinate from a composition comprising L-glufosinate and glutamate are provided. The method comprises converting the glutamate to pyroglutamate followed by the isolation of L-glufosinate from the pyroglutamate and other components of the composition to obtain substantially purified L-glufosinate. The composition comprising L-glufosinate and glutamate is subjected to an elevated temperature for a sufficient time to allow for the conversion of glutamate to pyroglutamate, followed by the isolation of L-glufosinate from the pyroglutamate and other components of the composition to obtain substantially purified L-glufosinate. The glutamate alternatively may be converted to pyroglutamate by enzymatic conversion. The purified L-glufosinate is present in a final composition at a concentration of 90% or greater of the sum of L-glufosinate, glutamate, and pyroglutamate. In some embodiments, a portion of the glutamate in the starting composition may be separated from the L-glufosinate using a crystallization step. Solid forms of L-glufosinate materials, including crystalline L-glufosinate ammonium, are also described.

The present invention relates to zeolite adsorbents based on agglomerated crystals of zeolite X comprising barium, potassium, sodium and strontium. These adsorbents have applications in the separation of fractions of aromatic C8 isomers and in particular xylenes.

The invention is a method for liquid, gaseous or supercritical phase chromatography which involves circulating, on a chromatograph (6) containing a stationary phase, a load (1) comprising components to be separated entrained by a carrier fluid (2), said method being characterized in that it involves: (a) obtaining, at the outlet of the chromatograph, a plurality of chromatographic fractions (3, 4) comprising at least one component of the load and the carrier fluid in a first fluid phase, (b) imposing a change of state on at least one of said chromatographic fractions (3, 4) so as to obtain at least one fraction of purified carrier fluid in a second fluid phase different from the first fluid phase by separating said carrier fluid from the component of the load, (c) imposing a change of state in a reverse direction to that of step (b) on at least one fraction of purified carrier fluid obtained in step (b) so as to obtain at least one fraction of purified carrier fluid in a third fluid phase different to the second fluid phase, and in that it involves coupling the change-of-state energies from the first fluid phase to the second fluid phase and from the second fluid phase to the third fluid phase of the same or of another fraction of purified carrier fluid, said coupling comprising a transfer of heat using a heat pump.

The invention relates to a method for the chromatographic purification of at least one cannabinoid compound, wherein the method comprises a main purification stage comprising the steps of: injecting an initial mixture comprising the at least one cannabinoid compound and one or more additional compounds onto a main stationary phase comprising silica particles, the silica particles comprising amino and/or diol groups; performing an elution with an elution solution, and collecting one or more elution fractions; and optionally, washing the main stationary phase with a washing solution and collecting one or more washing fractions; at least one of the elution fractions or washing fractions containing the at least one cannabinoid compound purified from the one or more additional compounds.