The present disclosure describes an apparatus of managing solvent associated with a field flow fractionator. In an exemplary embodiment, the apparatus includes (1) a union assembly coupled to a detector flow output from at least one detector coupled to a field flow fractionator, and (2) a recycle and waste assembly coupled to an output of the union assembly and a channel cross flow output of the field flow fractionator.

The liquid feeding device includes a discharge speed calculation part configured to calculate a discharge speed v of the plunger pump so that a converted value L.sub.ATM under an atmospheric pressure of a flow rate L.sub.PRE of the mobile phase discharged to the discharge channel from the pump part becomes a set flow rate L.sub.SET using a volume V of the mobile phase in the pump chamber of the closing pump immediately before the precompression process is started, a volume ΔV reduced due to the precompression process of the mobile phase in the pump chamber of the closing pump, and a feeding pressure P; and a discharge operation controller configured to control a discharge speed of the plunger pump to a discharge speed v calculated by the discharge speed calculation part.

The disclosure relates to a recycling chromatography method that includes injecting a sample into a mobile phase flow stream of a chromatography system to create a combined flow stream. The sample includes an API and at least one impurity. The chromatography system includes a first column and a column in series, a first valve in fluid communication with the first and second chromatographic columns, a heater in communication with the first and second chromatographic columns, a fraction collector in fluid communication with the first and second chromatographic columns, and a second valve positioned before the fraction collector. The combined flow stream is recycled from the first chromatographic column to the second chromatographic column and vice versa by switching the first valve until a baseline resolution is achieved to separate the at least one impurity from the API. The at least one impurity is collected in the fraction collector.

In one embodiment, a system of PFAS (Per-Poly-fluorinated alkyl substances) effluent liquid treatment includes: a pump to pump a liquid received via an intake; a sediment filter to filter sediment from the liquid; a granular activated carbon (GAC) device, disposed downstream of the sediment filter, to remove organic contaminants from the liquid; one (preferably two) or more ion exchange resin columns, disposed downstream of the GAC device, to remove PFAS constituents from the liquid; and a plurality of control valves being controlled to direct the liquid to flow along one or more liquid flow paths through the ion exchange resin columns so as to adjust a rate of processing the liquid by the one or more ion exchange resin columns. The system is disposed in a shipping container to be transported to a destination and is set up in the container onsite at the destination.

The present disclosure is directed at the selection and design of columns for liquid chromatography including liquid chromatography devices and systems and corresponding methods of operation, particularly in the field of high pressure liquid chromatography (HPLC).

The present disclosure relates to methodologies, systems, apparatus, and kits for introducing a sample within a chromatography system. A makeup pump is configured to pump a makeup fluid through a first restrictor into the chromatography system upstream of the column and downstream of a mobile phase pump. The first restrictor is located upstream of a column and downstream of makeup pump and a sample fluid pump. Decreasing an output volume of the makeup pump can direct a sample fluid from the sample fluid pump through the first restrictor to the column. Increasing an output volume of the makeup pump can direct the sample fluid to a second restrictor located downstream of the makeup pump and in parallel with the column and the detector.

Methodologies, systems, and computer-readable media are provided for controlling the mass flow rate within a CO.sub.2 based chromatography system. The pressure within a CO.sub.2 pump is measured and received at a computing system, and the computing system retrieves a target temperature value corresponding to the new pressure measurement within the CO.sub.2 pump. The computing system then generates a temperature control command that controls a CO.sub.2 pump heater or cooler in order to achieve the target temperature value at the CO.sub.2 pump. Thus, a target mass flow rate of CO.sub.2 from the CO.sub.2 pump is achieved by adjusting the temperature of the CO.sub.2 pump in response to changes in pressure.

Provided are apparatus and systems for performing a swing adsorption process. This swing adsorption process may involve passing an input feed stream through two swing adsorption systems as a purge stream to remove contaminants, such as water, from the respective adsorbent bed units. The wet purge product stream is passed to a solvent based gas treating system, which forms a wet hydrocarbon rich stream and a wet acid gas stream. Then, the wet hydrocarbon rich stream and the wet acid gas stream are passed through one of the respective swing adsorption systems to remove some of the moisture from the respective wet streams.

This disclosure provides a method for converting CBD to a tetrahydrocannabinol featuring the use of cheap and non-toxic aluminum isopropoxide as a catalyst. The method comprises (a) providing a reaction mixture comprising a catalyst in an organic solvent, wherein the catalyst comprises aluminum isopropoxide; (b) adding a reagent comprising CBD to the reaction mixture; (c) mixing the reaction mixture and allowing a reaction for converting CBD to a tetrahydrocannabinol to occur for a predetermine period of time; (d) removing the catalyst by filtration upon the completion of the reaction; (e) removing the organic solvent; and (f) eluting the tetrahydrocannabinol from the organic phase.

Liquid chromatography techniques are disclosed. Specifically, the liquid chromatography technique includes providing a liquid chromatography system having a coated metallic fluid-contacting element, and transporting a fluid to contact the coated metallic fluid-contacting element. Conditions for the transporting of the fluid are selected from the group consisting of the temperature of the fluid being greater than 150° C., pressure urging the fluid being greater than 60 MPa, the fluid having a protein-containing analyte incompatible with one or both of titanium and polyether ether ketone, the fluid having a chelating agent incompatible with the one or both of the titanium or the polyether ether ketone, and combinations thereof