A method for extracting compounds from plant material utilizing terpenes as a solvent is described. The invention includes the excitation of the plant material and terpene solvent with microwave, ultrasound, heat input, and physical agitation or combinations thereof. The invention particularly covers the process as it relates to the extraction of THC and CBD and their derivatives from cannabis and hemp for the use in products for medical and recreational use. The combinations of terpene saturant, plant material strain and process variables can be tuned in order to dial in the final resultant product for several variables including but not limited to terpene content, THC or CBD potency, ratios of THC or CBD and their derivatives, or flavor profile.

Devices, systems, and methods for metals production are disclosed. In a first embodiment, a first portion of an ore is reduced, producing metals. A portion of the metals are stripped, complexed, or a combination thereof, into a supercritical carbon dioxide stream.

The invention extends the utility of apparatus used to extract medicinal cannabis compounds into an eluate by separating a portion of medicinal cannabis compounds contained within a portion of eluate at a first extraction target level providing enough clean solvent to continue extraction operations. A high efficiency concentrator such as a rotary evaporator or a wiped film evaporator processes eluate from one or more tanks or extraction vessels creating clean solvent when extraction targets are met or when clean solvent is exhausted. This manages eluate concentration levels and limits the quantity of concentrated medicinal cannabis compounds on site at any moment in time. The invention enables a business model for keeping medicinal cannabis compounds within a legal system, and reduces pollution because law enforcement would no longer have to burn large quantities of cannabis plant matter.

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.

Provided is an extraction method for extracting an extract from a mixture using liquefied gas that can dissolve the extract, the method facilitating extraction operations and enabling low cost operation. An extraction device that extracts a component dissolved in liquefied gas from material to be treated using continuous phase changes in the liquefied gas is characterized by being provided with: a compressor that feeds gas under pressure; a heat exchanger for generating liquefied gas by the gas flowing in a high temperature side flow path; a treatment tank into which the material to be treated is loaded and the liquefied gas flows; and a retention tank provided in series or in parallel to the flow path downstream of the high temperature side flow path in the heat exchanger.

A system machines and methods for extracting select moieties, flavonoids, and essential oils from plant material without co-extracting chlorophyll, lipids and other undesirable constituents from plants. Super-cooled extraction techniques are taught. Likewise, according to embodiments methods provides 100% grain ethyl alcohol extract with a concentration of chlorophyll that is below 1%.

In alternative embodiments, provided are industrial processes and methods for extracting or removing cannabinoids, flavonoids and terpenes from plant materials such as trichomes. In alternative embodiments, the cannabinoids, flavonoids and terpenes are extracted or removed from the plant materials using a non-polar, organic solvent, or a mixture of non-polar, organic solvent and polar, organic solvent.

Disclosed are compositions enriched with thymohydroquinone, further comprising of thymoquinone, hederagenin and/or -hederin formulated by blending the active molecules isolated from the seeds of Nigella sativa. Also disclosed are novel processes for the isolation of bioactive components thymohydroquinone, thymoquinone from the seeds of Nigella sativa. A process for the isolation -hederin and hederagenin from the spent material of Nigella sativa is also disclosed herein.

Systems and methods for selectively recovering a target metal from an ion exchange resin are generally described. In certain embodiments, such methods and systems can be employed for metal purification and enrichment of target metal species from mixtures containing contaminating or non-target metals. In some embodiments, ion exchange is accomplished in the presence of one or more species that facilitate the recovery of a metal from a composition further comprising one or more other metals. The recovered metal-containing composition may contain the recovered metal at relatively high purity and/or in relatively large amounts. In some embodiments, the conditions present during ion exchange are varied in a manner that facilitates the enrichment of a metal from an initial (e.g. sample) composition further comprising one or more other metals to result in a product that contains the enriched metal at relatively high purity and/or in relatively large amounts

In accordance with one or more embodiments of the present disclosure, a computer-controlled programmable logic controller (PLC) extraction system for separating an extract from a biomass includes a PLC, a solvent reservoir comprising a solvent that is a gas when the solvent is at a temperature of 25 C. and atmospheric pressure, a plurality of extraction devices comprising the biomass, an extract collection reservoir for collecting the extract, a solvent recovery system, and a temperature controlled circulation system. The circulation system fluidly connects the solvent reservoir, the plurality of extraction devices, the extract collection reservoir, and the solvent recovery system and comprises at least one apparatus for controlling a flow of the solvent. The solvent comprises no more than 1 weight % CO.sub.2. A method of extracting an extract from a biomass using a PLC extraction system is also described.