Methods for extracting and recovering bioactive components from a biomass feedstock with pressurized aqueous solvent solutions comprising one or more organic solutes and/or one or more inorganic solutes. The methods comprise the steps of: (i) preparing a selected aqueous solvent solution for pressurizing; (ii) providing a flow of the prepared aqueous solvent solution to a plant biomass feedstock contained within a pressure-resistant temperature-controllable reactor vessel (iii) warming the flow of aqueous solvent solution and the contents of the reactor vessel to a selected temperature; (iv) pressurizing the flow of the aqueous solvent solution and the contents of the reactor vessel to a selected pressure; (v) controllably flowing the pressurized aqueous solvent solution through the reactor vessel while maintaining the contents of the reactor vessel at the selected pressure; and (vi) collecting a flow of the pressurized aqueous solvent solution egressing from the reactor vessel for a selected period of time.

The invention relates to methods of separating or isolating a component from a plant using freeze separation. The invention includes products produced by said methods.

A method of recovering fluoropolymer from a three-dimensional printed object can include dissolving a fluoropolymer of a three-dimensional printed object in a fluoropolymer-dissolving solvent to generate dissolved fluoropolymer from the three-dimensional object, wherein the three-dimensional printed object includes from about 0.1 wt % to about 10 wt % particulate fusing compound and from about 90 wt % to about 99.9 wt % fluoropolymer. The method can further include separating the particulate fusing compound from the fluoropolymer-dissolving solvent and the dissolved fluoropolymer, and evaporating the fluoropolymer-dissolving solvent from the dissolved fluoropolymer.

A waste treatment system for separating contaminants including per-fluoroalkyl and poly-fluoroalkyl substances (PFAS) from bulk solid waste (12). A preparation module (9) having a bulk material separator separates oversize material (14) from bulk solid waste (12). A physical separation module (13), located down-stream of the preparation module (9), separates the bulk solid waste (12) based on particle size using physical and/or hydrodynamic and/or density separation techniques. An extraction/chemical separation module (19), located downstream of the physical separation module (13), adds leachate and/or extractant to separate the contaminants from a slurry output from the physical separation module (13), into a fines output and a contaminated water solution. A water circulation system (21) supplies water to the physical separation module (13) and the extraction/chemical separation module (19), the water circulation system including at least one water treatment process, the treated water being recycled and recirculated within the waste treatment system.

The specification provides methods for extracting juice, anthocyanin, pectin, proanthocyanidin, and/or other phenolic compounds, from fruit material such as cranberry fruit, presscake, and/or pomace, through a sequential extraction procedure.

An apparatus for extraction and recovery of components from biomass feedstocks with pressurized low polarity water. The apparatus is configured with four or more reaction columns, wherein each column is in separate communication with a supply of hot water, a first supply of pressurized heated water, a second supply of pressurized heated water, and a supply of pressurized cooling water. Components may be extracted concurrently from two or more batches of the biomass by, first placing the two batches of biomass into two selected columns, separately flooding the two columns with pressurized water, heating the columns and their contents to the point where the water becomes pressurized low polarity (PLP) water, recovering the PLP water comprising the extracted components from the two selected columns, cooling the columns with PLP water, and removing the spent biomass material from the columns.

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.

This invention relates to the extraction of psychoactive compounds from organisms for use in medicine. Extraction is carried out with a strong acid or strong base to either promote or inhibit dephosphorylation. The extract in the slurry form is standardized with added excipient so that when it is dried the powdered composition has a specified total psychoactive alkaloid concentration, with a known ratio of phosphorylated to dephosphorylated psychoactive alkaloids.

A method of making CBD concentrate or CBD Isolate comprises (a) milling a raw material; (b) contacting the milled raw material with an extraction solvent and separating a solid waste material to form a filtered extract; (c) concentrating the filtered extract; (d) washing the concentrated extract to form an organic phase and an aqueous phase; (e) separating the aqueous phase from the organic phase to form a washed extract; (f) removing an organic solvent from the washed extract to form a concentrated washed extract; (g) decarboxylating the concentrated washed extract; (h) vacuum distilling the decarboxylated extract to form a distillate; (i) dewaxing the distillate to form a post-dewax filtrate; (j) applying a vacuum to the post-dewax filtrate to form a post-dewax concentrate; (k) degassing the post-dewax concentrate; and (l) vacuum distilling the degassed concentrate to form a CBD concentrate.

This invention relates to the extraction of psychoactive compounds from psilocybin fungus for use in medicine. Raw psilocybin fungus is dried and ground. The solvent used for extraction is a lower aliphatic alcohol, water, a hydro-alcohol mixture, an acidic hydro-alcohol mixture, or an alkaline hydro-alcohol mixture. The extraction slurry is filtered and pH-adjusted if necessary. The solvent is then partially evaporated, or completely evaporated with water added back, to form a concentrated slurry. The concentrated slurry is then standardized to provide a known concentration of the psychoactive alkaloids that have been extracted. The standardized slurry may then be dried to result in a powdered psilocybin mushroom extract with a precisely defined purity.