An initial introduction control part introduces an aqueous solution containing molybdenum 99 and technetium 99m, and an organic solvent being capable of dissolving the technetium 99m into an extraction tank. A micro-mixing control part micro-mixes the aqueous solution and the organic solvent by heating and stirring a mixed solution of the aqueous solution and the organic solvent introduced into the extraction tank with a heater, while applying ultrasonic to the mixed solution. A separation control part separates the mixed solution micro-mixed into two phases of aqueous solution and an organic solvent. A taking-out introduction control part passes the organic solvent separated into two phases through an adsorption column be capable of adsorbing molybdenum 99 and introduces the organic solvent into an evaporation elution tank. An evaporation control part evaporates the organic solvent and leaves residue by reducing pressure inside the evaporation elution tank and heating the organic solvent introduced into the evaporation elution tank with a heater, while applying ultrasonic to the organic solvent. An elution control part introduces physiological saline solution into the residue and elutes technetium 99m into the physiological saline solution from the residue.

A method for chemical separation of cannabinoids includes: (i) providing a starting organic solvent solution that contains a mixture of cannabinoid acids, (ii) using an aqueous basic solution to remove a portion of the cannabinoid acids from the mixture of cannabinoid acids in the starting organic solvent solution by converting the portion of the cannabinoid acids to cannabinoid carboxylate salts that solubilize in the an aqueous basic solution, (iii) separating the aqueous basic solution in (ii) from the starting organic solvent, (iv) combining the aqueous solution from (iii) with new organic solvent to produce a combined solution, (v) acidifying the combined solution to extract the cannabinoid acids from the aqueous solution to the organic solvent, (vi) separating the organic solvent of (v) from the aqueous solution, and (vii) evaporating the organic solvent of (vi) to leave product cannabinoid acids.

An object of the present invention is to preserve the total content of chlorophyll in an extract while increasing the extraction yield of a Spirulina extract. Another object of the present invention is to provide a pharmaceutical composition and health functional food for prevention or treatment of degenerative cranial nerve diseases containing a Spirulina extract as an active ingredient, and to provide a method for treating degenerative cranial nerve diseases using a Spirulina extract. The present invention provides a method for producing a Spirulina extract including the steps of (a) preparing a Spirulina powder; (b) adding 50% to 80% of ethanol to the Spirulina powder and performing an ultrasonic pretreatment at 15° C. to 35° C.; (c) extracting a Spirulina extract at 50° C. to 80° C.; (d) vacuum-concentrating the Spirulina extract; and (e) freeze-drying the vacuum-concentrated Spirulina extract.

A method for purifying a boron nitride nanotube feedstock is disclosed, including an initial step of mixing a boron nitride nanotube (BNNT) feedstock with a solvent to form an initial mixture. This BNNT feedstock is made up of hexagonal boron nitride (h-BN) particles and less than about 50 weight percent BNNTs on a dry basis. This initial mixture is then sonicated within a treatment vessel using an ultrasonic probe. At least a portion of the initial mixture is filtered out of the treatment vessel and across a nanoporous membrane at the same as the sonication. In this manner, the method provides a filtrate which is enriched in h-BN particles relative to the initial mixture and a retentate which is enriched in BNNTs relative to the initial mixture.

A cavitation mixing apparatus is provided for performing separations from solid material using subcritical liquid CO.sub.2. A cavitation inducing device inside a cavitation mixing vessel is held in place with a cavitation mixer mount comprising at least one fluid channel for equalizing gaseous pressure of CO.sub.2 around the cavitation inducing device. Also described is method of separating oils from a crude plant oil mixture by injecting crude plant oil into a pressurized mixing vessel comprising liquid carbon dioxide and mixing the crude oil with the liquid carbon dioxide under pressure using powered induced cavitation, the cavitation mixing vessel comprising an encapsulated cavitation inducing device.

A sample purification system includes a container assembly bounding a sample purification compartment and having an upper end and an opposing lower end, the sample purification compartment comprising mixing zones and settling zones. A plurality of shielding elements are positioned within the sample purification compartment so as to at least partially separate adjacent mixing zones and settling zones or separate adjacent mixing zones, the mixing zones being in fluid communication with the settling zones. A mixing element is disposed within each mixing zone. An acoustic wave settler is aligned with a portion of the container assembly, the acoustic wave settler being configured to emit an acoustic wave through the portion of the container assembly and a mixture disposed therein, the acoustic wave coalescing fluid phase droplets disposed in the mixture to increase the buoyancy or density of the fluid phase droplets.

In accordance with embodiments of the present invention, a terpene-rich sample is prepared for terpene analysis using liquid chromatography via an extraction method that takes little time, uses minimal external equipment, and permits direct injection of extracted terpenes into a liquid chromatography instrument for analysis. An embodiment of the invention involves preparing a terpene-containing sample for analysis by liquid chromatography by liquid extraction; heating the liquid extract in a vial that contains a filter medium or solvent; collecting the terpenes in the medium by the vapor pressure forced through the filter from heating; and eluting the collected terpenes into a vial or directly into a chromatography injector.

In accordance with embodiments of the present invention, a terpene-rich sample is prepared for terpene analysis using liquid chromatography via an extraction method that takes little time, uses minimal external equipment, and permits direct injection of extracted terpenes into a liquid chromatography instrument for analysis. An embodiment of the invention involves preparing a terpene-containing sample for analysis by liquid chromatography by liquid extraction; heating the liquid extract in a vial that contains a filter medium or solvent; collecting the terpenes in the medium by the vapor pressure forced through the filter from heating; and eluting the collected terpenes into a vial or directly into a chromatography injector.

The present disclosure relates, according to disclosed embodiments, to a system for extracting an organic compound from a natural source, the system comprising a computer processor operational to control the system; a storage vessel configured to store an extraction gas, the storage vessel comprising a storage vessel outlet in electrical communication with the computer processor; a valve in electrical communication with the computer processor, the valve comprising a valve inlet and a valve outlet, wherein the valve inlet connects to the storage vessel outlet; a dynamic extraction vessel; and a spray evaporation loop system configured to receive a solute from the dynamic extraction vessel, the spray evaporation loop system comprising an injection nozzle in electrical communication with the computer processor, the injection nozzle comprising an injection nozzle inlet connected to the first dynamic extraction vessel outlet; and a cyclonic separator in electrical communication with the computer processor.

A semi-aqueous method for extracting a substance. The method involves combining a first liquid or solid substance containing an extract with a semi-aqueous solution containing a water-soluble or water-emulsifiable (WSWE) compound. Said WSWE compound selectively dissolves extract during a dense phase CO.sub.2 expansion and salting-out process, which is simultaneously co-extracted using said dense phase CO.sub.2, and desolvated to produce a CO.sub.2 salted-out solvent mixture containing extract. Said CO.sub.2 salted-out solvent mixture is treated using various secondary processes. The present invention is useful for producing extracts for use as additives in pharmaceuticals, nutraceuticals, cosmetics, beverages, or foods, and for quantitative analysis.