An apparatus and a method for plant extraction are disclosed. The apparatus of the present invention comprises an extraction module, a separating module and a reservoir. The method essentially includes plant material preparing, decarboxylating, active components extracting and separating. By using liquid tetrafluoroethane as the solvent in the apparatus of the present invention, the active components of the plant material are efficiently extracted under low pressure extraction and high pressure extraction conditions.

An apparatus and a method for plant extraction are disclosed. The apparatus of the present invention comprises an extraction module, a separating module and a reservoir. The method essentially includes plant material preparing, decarboxylating, active components extracting and separating. By using liquid tetrafluoroethane as the solvent in the apparatus of the present invention, the active components of the plant material are efficiently extracted under low pressure extraction and high pressure extraction conditions.

Various aspects of this patent document relate to a method to extract an oil from a plant material using an apparatus by first exposing the plant material to a heated gas stream at a temperature sufficient to volatilize the oil from the plant material, and then rapidly cooling the gas stream to liquefy the oil.

A method of extracting an essential oil from plant matter, starting with providing plant matter to an interior of an extraction vessel, wherein the plant matter includes at least one essential oil. Next, at least one vacuum pump is used to reduce the pressure within the interior of the extraction vessel with the plant matter therein to an absolute pressure of less than 1.0 mm Hg absolute pressure. Microwave energy is applied to the plant matter while the interior of the extraction vessel is under the reduced pressure, thereby forming a vapor including at least a portion of the essential oil. The vapor is directed from the extraction vessel to at least one condenser vessel. Finally, the vapor is condensed to a liquid state such that the vapor includes at least a portion of the essential oil, by utilizing the at least one condenser vessel.

A method of extracting an essential oil from plant matter, starting with providing plant matter to an interior of an extraction vessel, wherein the plant matter includes at least one essential oil. Next, at least one vacuum pump is used to reduce the pressure within the interior of the extraction vessel with the plant matter therein to an absolute pressure of less than 1.0 mm Hg absolute pressure. Microwave energy is applied to the plant matter while the interior of the extraction vessel is under the reduced pressure, thereby forming a vapor including at least a portion of the essential oil. The vapor is directed from the extraction vessel to at least one condenser vessel. Finally, the vapor is condensed to a liquid state such that the vapor includes at least a portion of the essential oil, by utilizing the at least one condenser vessel.

Disclosed is a pharmaceutical composition or food composition for the treatment or prevention of hypertension, containing a peptide isolated from a fraction of a flounder surimi hydrolysate as an active ingredient and is based on the finding that the flounder surimi has an effect of reducing blood pressure, and the hydrolysate of the flounder surimi, the fraction of the hydrolysate of the flounder surimi and peptides isolated from the fraction of the hydrolysate of the flounder surimi have an inhibition activity against an angiotensin I converting enzyme (ACE). Thus, peptides isolated from the fraction of the hydrolysate of the flounder surimi can be used for pharmaceutical compositions or food compositions for treating or preventing hypertension. Also, the present invention is based on the finding that the hydrolysate of the flounder surimi and peptides isolated therefrom have radical scavenging effect and a protective effect against oxidative stress and are thus capable of inhibiting ROS production, lipid peroxidation and apoptosis. Accordingly, peptides isolated from fractions of the hydrolysate of the flounder surimi can be used for food compositions for antioxidation.

Herb oil pressing devices and methods are provided. The devices include a pair of closable opposed jaws that can apply pressure to a herb placed between the jaws; a motor connected to the jaws for controlling the closing of the jaws, and, when closed, controlling the pressure produced between the jaws; a heater connected to the jaws for heating the jaws and herb; a housing in which the jaws, the motor, and the heater are housed; and a user interface connected to the jaws and the heater, the user interface for inputting a selection of temperature, pressure, and amount of time the temperature and pressure is applied to a herb positioned between the jaws to extract oil therefrom. Related computer-implemented methods of pressing a herb are also provided.

An apparatus and method of use employs a multiple displacement evacuation tank and a cavitation apparatus. Heated fluid from the cavitation apparatus is used to treat a plant material to obtain a purified oil product therefrom. The cavitation apparatus output is used to both heat the multiple displacement evacuation tank contents and supply a feed to the multiple displacement evacuation tank for oil product manufacture. The fluid is preferably a lipid emulsion and the plant material is preferably a hemp material that allows for recovering of the cannabinoids therefrom.

Systems and methods for extracting solute from a source material in multiple canister systems are shown and described.

A system for the extraction of essential oils from botanical matter housed within an extraction vessel, the system comprising: a transfer tank storing liquid and gaseous extraction fluid; a charge tank configured for storing liquid and gaseous extraction fluid, the charge tank being in fluid communication with the transfer tank; a transfer tank engagement valve selectively permitting fluid flow between the transfer tank and the charge tank; means for pressurizing the transfer tank; means for cooling the charge tank; wherein pressurizing the transfer tank transfers liquid phase extraction fluid to the charge tank, and cooling the charge tank increases a density of the liquid extraction fluid in the charge tank; wherein a transfer of extraction fluid from the charge tank to the extraction vessel occurs due to a pressure differential between the charge tank and the extraction vessel and without raising the temperature of the charge tank and without using a pump to transfer extraction fluid from the charge tank to the extraction vessel.