A method for cell disruption and extraction of a plant, includes placing plant material on a porous container, placing the porous container into a reaction device, and producing water ion steam of an atmospheric pressure by a water ion generator. The water ion steam infiltrates the porous container and permeates the plant material. The water ion steam penetrate cells of the plant material and breaks the cell wall of the cells, to cause a cell disruption. The residual water ion steam is drained outward from the exhaust pipe of the box.

The disclosed embodiments include systems and methods for the solvent extraction of a substance from a material. The disclosed systems include multiple tanks and an extraction chamber in communication with the tanks. Solvent transport is accomplished by heating and/or cooling selected tanks to cause the solvent to be transported between tanks.

An apparatus and method for extraction of oils from botanical material using high-pressure hydrocarbons such as propane, or butane, or mixtures thereof are described. A high-pressure propane or butane saturated liquid/vapor mixture formed by pressure reduction through a valve placed before an extraction column, thereby serving as an expansion port was employed. The apparatus is capable of both continuous liquid extraction or batch-style liquid operation through the use of a manifold valve, which directs the solvent liquid/vapor in the system to either a supply tank or an extraction column.

Generally, an extraction system useful in separating an extract from a matrix using one or more extractants. Specifically, an extractor including one or more of: an extraction vessel having an extractor vessel internal surface which defines an extraction chamber which communicates between open extraction vessel first and second ends, a first piston configured to sealably engage the extractor vessel internal surface of the extraction vessel first end or a second piston adapted to sealably engage the extractor vessel internal surface of the extraction vessel second end.

Disclosed herein is a method for obtaining compounds and compositions from plant and fungus materials by thermal treatment, affinity capture, filtration, and release through multi-phasic transitions between gas, solid, and liquid states. The compounds of interest are obtained by manipulating the temperature and pressure of the heating chamber. The compounds in gas phase are passed through an affinity medium which captures the compounds of interest in either solid or liquid phase by exposing the compound of interest to the localized micro-affinity environment of the medium. The compounds are separated from the medium using direct competition with solvent or buffers optimized for the specific chemical properties of compounds.

The industrial production of an extract by means of solid-liquid extraction improves the exchange of substances during extraction and allows enhanced dehumidification of a raffinate with residual moisture.

The extraction is enhanced during a first dwell time by at least partially flooding a vessel in the form of at least one flow discharged with a secondary solvent or the obtained extract, swirling and keeping in suspension the primary mixture within the vessel by supplying the secondary solvent or the obtained extract via a foot area of the vessel, and/or moving the vessel relative to the extraction container within the obtained extract.

The secondary solvent or the extract circulates in the extraction container by a circulation guide incorporating the extraction container from top to bottom relative to the extraction container, and the extract freed from raffinate with residual moisture obtained by dehumidification is supplied to the separated or to be separated extract.

A system and method for extracting essential oils is provided. One embodiment comprises an extractor assembly with an extractor cover, an extractor container, and an extractor assembly base, wherein the extractor container is secured between the extractor cover and the extractor assembly base during an extraction process; a bowl cover assembly with a collection bowl, and a bowl cover assembly base, wherein the collection bowl is secured between the extractor assembly base and the bowl cover assembly base during the extraction process; and a canister compression holder assembly, wherein a cannister containing a solvent is secured within the canister compression holder assembly during the extraction process. A solvent that is released from the cannister passes into the extractor container that contains matter that is to have essential oils extracted therefrom. The extracted oils exits the extractor assembly base into the collection bowl that collects the solvent with the essential oils.

A method of extracting at least one cannabinoid from a biomass consisting of industrial hemp comprises: (i) contacting the biomass with a solvent formulation which comprises a C1-4 fluorinated hydrocarbon or a C1-4 hydrofluorocarbon ether, thereby to charge the solvent formulation with an extract from the biomass; and (ii) separating charged solvent formulation from the biomass.

A device for automatic extraction, storage and encapsulation of fatty compounds, the device may include: an extraction unit configured to provide a liquid mixture comprising fatty compounds extracted from biological material and a liquid solvent; an evaporation and reaction unit; a storage unit comprising one or more storage outlet ports; and a controller configured to: control delivery of the liquid mixture from the extraction unit to the evaporation and reaction unit; control evaporation of the solvent from the liquid mixture in the evaporation and reaction unit; control delivery of the liquid mixture from the evaporation and reaction unit to the storage unit; detect safe connection of each of at least one of one or more capsules to one of the one or more storage outlet ports of the storage unit; and control filling of at least one of the one or more connected capsules with the liquid mixture.

A recirculating high pressure lipid extractor includes a kettle with a sealed interior configured for pressurizing and heating a fluid mixture. A flow funnel is positioned in a lower portion. A removable material basket is positioned on top of the flow funnel in an upper section. The removable material basket is configured to hold a material inside the removable material basket. A drain and inlet port is at a bottom of the kettle in communication with the sealed interior of the kettle. A recirculation port is approximate a top of the kettle in communication with the sealed interior of the kettle. Wherein, when the fluid mixture is inserted into the kettle, the recirculating high pressure lipid extractor is configured to pressurize and heat the fluid mixture and recirculate the pressurized and heated fluid mixture from the recirculation port into the drain and inlet port.