Patent classifications
B01D15/40
Dynamic interface system and its application in supercritical fluid extraction and chromatography
The present invention provides a dynamic interface system between an extraction device and a chromatographic purification device for separating and purifying substance(s) from a mixture or matrix. One embodiment is the Supercritical Fluid Interface (“SFI”) between Supercritical Fluid Extraction (“SFE”), and Supercritical Fluid Chromatography (“SFC”). The SFI is capable of interfacing; gas, subcritical and supercritical fluid extraction methods and pair with gas, subcritical and supercritical fluid chromatography technologies that operate within the pressure and temperature parameters of the SFI. The SFI can operate up to 200 degrees celsius and 5000 psi. This interface technology allows for an inline oil extraction and chromatographic separation, the SFI can pair extraction and chromatography with the same solvent in different mobile phases, whereas the extraction can be performed using CO.sub.2 as a solvent in sub-critical phase and the SFI can receive the subcritical solution and then increase pressure and/or temperature to achieve supercritical state as required for injection into supercritical fluid chromatography technologies. The SFI coupling between SFE and SFC can to extract and refine cannabinoids from the cannabis industrious, hemp, plant and can also be applied to improve efficiency in an industry that extracts and refines oils, through chromatography, from organic materials using a gas, or sub/supercritical fluid as a solvent and mobile phase.
Device storage structure for fluid chromatograph
A storage container includes a casing and a bi-parting door. The casing has an opening and stores a device to be used in a fluid chromatograph. A door of the bi-parting door includes a frame member and a cover member. The frame member includes an upper frame and a lower frame. The upper frame and the lower frame are provided at the casing to be turnable around a turning axis and be spaced apart from each other on the turning axis. The cover member is configured to be attachable to and detachable from the frame member and partially cover the opening when the door is closed. A space is formed between the upper frame and the lower frame.
Process for Producing an Aroma-Laden Gas, Aroma-Laden Gas, and Use of the Aroma-Laden Gas
A process for producing an aroma-laden gas (10) comprises the following steps: a) providing a liquid phase (5), which contains a solvent and one or several aromatic substances (1, 2, 3); b) guiding through a solid phase extraction column (3) of the liquid phase provided in step (a) by obtaining the solid phase (35) laden with one or several aromatic substances; separating one or several aromatic substances from the laden solid phase by means of at least one gas (2) in a liquid and/or supercritical state; and optionally d) collecting the gas (10), which is laden with one or several aromatic substances (1, 2, 3).
Gas-Liquid Separator for a Chromatography System
The present invention relates to a gas-liquid separator for a chromatography system, comprising: (a) a separating region having an inlet nozzle, a baffle unit and a gas distribution unit; (b) a dividing region having a liquid outlet; and (c) a gas discharge region having a gas outlet; wherein the separating region is connected to the dividing region by a separating opening and the distance of the inlet nozzle from the baffle unit is greater than the smallest longitudinal extension of the separating opening and the inlet nozzle is configured such that a gas-liquid stream directed through the inlet nozzle can act on the baffle unit.
The present invention further relates to a chromatography system comprising a separator according to the invention and to a chromatography method wherein the separator is used.
Gas-Liquid Separator for a Chromatography System
The present invention relates to a gas-liquid separator for a chromatography system, comprising: (a) a separating region having an inlet nozzle, a baffle unit and a gas distribution unit; (b) a dividing region having a liquid outlet; and (c) a gas discharge region having a gas outlet; wherein the separating region is connected to the dividing region by a separating opening and the distance of the inlet nozzle from the baffle unit is greater than the smallest longitudinal extension of the separating opening and the inlet nozzle is configured such that a gas-liquid stream directed through the inlet nozzle can act on the baffle unit.
The present invention further relates to a chromatography system comprising a separator according to the invention and to a chromatography method wherein the separator is used.
Supercritical fluid chromatography system
Provided is a chiller and system that may be utilized in a supercritical fluid chromatography method, wherein a non-polar solvent may replace a portion or all of a polar solvent for the purpose of separating or extracting desired sample molecules from a combined sample/solvent stream. The system may reduce the amount of polar solvent necessary for chromatographic separation and/or extraction of desired samples. The system may incorporate a supercritical fluid chiller, a supercritical fluid pressure-equalizing vessel and a supercritical fluid cyclonic separator. The supercritical fluid chiller allows for efficient and consistent pumping of liquid-phase gases employing off-the-shelf HPLC pumps. The pressure equalizing vessel allows the use of off-the-shelf HPLC column cartridges. The system may further incorporate the use of one or more disposable cartridges containing silica gel or other suitable medium. The system may also utilize an open loop cooling circuit using fluids with a positive Joule-Thompson coefficient.
Supercritical fluid chromatography system
Provided is a chiller and system that may be utilized in a supercritical fluid chromatography method, wherein a non-polar solvent may replace a portion or all of a polar solvent for the purpose of separating or extracting desired sample molecules from a combined sample/solvent stream. The system may reduce the amount of polar solvent necessary for chromatographic separation and/or extraction of desired samples. The system may incorporate a supercritical fluid chiller, a supercritical fluid pressure-equalizing vessel and a supercritical fluid cyclonic separator. The supercritical fluid chiller allows for efficient and consistent pumping of liquid-phase gases employing off-the-shelf HPLC pumps. The pressure equalizing vessel allows the use of off-the-shelf HPLC column cartridges. The system may further incorporate the use of one or more disposable cartridges containing silica gel or other suitable medium. The system may also utilize an open loop cooling circuit using fluids with a positive Joule-Thompson coefficient.
Differentiation of natural vitamin E from synthetic vitamin E and quantification of tocopherols by supercritical fluid chromatography
The present disclosure provides methods for the separation and quantitation of enantiomers of vitamin E using supercritical fluid chromatography (SFC) or carbon dioxide-based chromatography on chiral columns. The disclosed methods may be used to quantitatively determine the concentration of RRR-α-tocopherol in foods, food ingredients, dietary supplements, vitamin premixes, nutritional formulas, and medicines. Further provided is a method of differentiating the source of α-tocopherol as natural or synthetic.
Differentiation of natural vitamin E from synthetic vitamin E and quantification of tocopherols by supercritical fluid chromatography
The present disclosure provides methods for the separation and quantitation of enantiomers of vitamin E using supercritical fluid chromatography (SFC) or carbon dioxide-based chromatography on chiral columns. The disclosed methods may be used to quantitatively determine the concentration of RRR-α-tocopherol in foods, food ingredients, dietary supplements, vitamin premixes, nutritional formulas, and medicines. Further provided is a method of differentiating the source of α-tocopherol as natural or synthetic.
Device capable of pressurization and associated systems and methods
Exemplary embodiments are directed to devices, methods and systems capable of pressurization, generally involving a flow system that includes a pressurized reservoir, at least one pump including a pump control valve, an outlet port, a shut-off valve and a vent valve. The flow system is configured to be pressurized. The shut-off valve is disposed between the pressurized reservoir and the at least one pump. The vent valve is disposed between the at least one pump and the outlet port. The shut-off valve, the vent valve and the pump control valve of the at least one pump are configured to actuate in a coordinated manner to control a pressurization of the flow system. Exemplary embodiments are further directed to devices, methods and systems for column switching, generally including at least a first column, a second column and a column switching valve.