A distillation apparatus has a cooling jacket, in the shape of a halo, surrounding at least a part of a vertical extent of a fraction collector in the disclosed technology. Connecting to and/or extending into an interior space of the fraction collector is an end of a vertically-extending passageway. This passageway is functionally connected at an other end to a lower-end entry portal. An outer cover substantially covers the cooling jacket, fraction collector, and a portion of the vertically-extending passageway, excepting for a top portal, a side exit portal, at least one cooling jacket intake, and at least one cooling jacket outtake.

A method for phytochemical extraction includes providing a distillation vessel, providing a mixture of solvent and plant extract to the distillation vessel, placing the distillation vessel on a heat source, coupling the distillation vessel with a collector configured to collect condensed solvent, selecting an initial distillation temperature and outputting heat from the heat source at a heat source initial target temperature to heat the distillation vessel to a distillation vessel initial target temperature and boil the mixture in the distillation vessel at the initial distillation temperature and at an initial heat flux. With a vacuum pump, a distillation vessel initial target pressure is set within the distillation vessel.

A method for phytochemical extraction includes providing a distillation vessel, providing a mixture of solvent and plant extract to the distillation vessel, placing the distillation vessel on a heat source, coupling the distillation vessel with a collector configured to collect condensed solvent, selecting an initial distillation temperature and outputting heat from the heat source at a heat source initial target temperature to heat the distillation vessel to a distillation vessel initial target temperature and boil the mixture in the distillation vessel at the initial distillation temperature and at an initial heat flux. With a vacuum pump, a distillation vessel initial target pressure is set within the distillation vessel.

A system and method for separating desirable elements from typically undesirable byproducts of a cannabis extraction system is disclosed. The system and method may separate terpenes and/or THC from residue byproducts that may typically be discarded as waste. The system and method includes at least two unique steps of refinement that may result in purity levels of 90% for the terpenes and 90% for the THC.

The invention provides a method and apparatus for purifying water. The apparatus includes a water still for receiving water and a hot air maintained in a heat-exchanging relationship to obtain a hot water and a cold air. The apparatus also includes one or more water purification units configured to receive the hot water from the water still in which the hot water is further heated using thermal energy received from one or more thermal energy sources to obtain steam and waste matter. A water purification unit of the one or more water purification units includes a waste matter remover for removing the waste matter from the water purification unit. The water still includes a heat-exchanging unit configured to receive the steam from the one or more water purification units. The steam received at the heat-exchanging unit is condensed to obtain purified water within the heat-exchanging unit using the cold air.

The invention provides a method and apparatus for purifying water. The apparatus includes a water still for receiving water and a hot air maintained in a heat-exchanging relationship to obtain a hot water and a cold air. The apparatus also includes one or more water purification units configured to receive the hot water from the water still in which the hot water is further heated using thermal energy received from one or more thermal energy sources to obtain steam and waste matter. A water purification unit of the one or more water purification units includes a waste matter remover for removing the waste matter from the water purification unit. The water still includes a heat-exchanging unit configured to receive the steam from the one or more water purification units. The steam received at the heat-exchanging unit is condensed to obtain purified water within the heat-exchanging unit using the cold air.

A liquid separator and concentrator is disclosed. An example liquid separator and concentrator includes a separator column. A spray chamber has a sprayer nozzle to spray an influent within the spray chamber and create a falling film in the separator column. A heating jacket surrounds the separator column, wherein the heating jacket heats the falling film to evaporate at least one portion of the falling film and leaves a concentrate. A concentrate collection vessel receives the concentrate from the separator column.

An automatic tritium extraction device for environmental monitoring comprises a distillation chamber, a temperature control unit, a condensation unit and an auxiliary condensation unit. The distillation chamber is connected to a first pump, a second pump and a third pump. A delivery pipe comprises a first vertical pipe, a second vertical pipe and an oblique pipe which inclines upwards from the distillation chamber to the condensation unit. An automatic tritium extraction method for environmental monitoring comprises the following steps: 1) cleaning of a distillation chamber; 2) distillation rising; 3) distillation; 4) condensation; 5) discharging samples out of the distillation chamber. By the adoption of the automatic tritium extraction device and method for environmental monitoring, fully-automatic distillation and condensation of environmental tritium samples, automatic cleaning of the distillation chamber, and automatic and accurate addition of required agents are realized, and fully-automatic acquisition, preparation, distillation, purification, measurement and analysis of environmental tritium can be completed; and manual intervention is reduced, so that monitoring results are more accurate, and labor costs are saved.

The present invention relates to supercritical water oxidation reactor adapted to contain inside the reactor an aqueous fluid below and above its supercritical state, said fluid comprising organic and/or inorganic material and a method of controlling such a reactor.

The present invention relates to supercritical water oxidation reactor adapted to contain inside the reactor an aqueous fluid below and above its supercritical state, said fluid comprising organic and/or inorganic material and a method of controlling such a reactor.