A component extraction apparatus includes a rack placement part, a heater, an extraction medium supply part, a needle assembly, and a temperature sensor. When the container rack is mounted on the rack placement part, a heater is configured to heat the sample containers in direct or indirect contact with sample containers held by the container rack. The needle assembly holds a needle with a tip thereof pointing downward, and the needle being configured to connect a flow channel by inserting the tip thereof into a needle port provided on an upper surface of each of the sample containers. The temperature sensor is included in the needle assembly and is configured to detect a temperature of the upper surface of any one of the sample containers when the tip of the needle is inserted into the needle port of the one of the sample containers.

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.

A process for the microfluidic extraction of molecules of interest from a vegetable oil, which utilizes a microfluidic chip with a double-Y-channel circuit, two inlets, two outlets, and a main channel, a first vessel including vegetable oil and a second vessel including ethanol for extraction, a pressure controller for pressurizing the vegetable oil and the ethanol, a first collector for the triglycerides-enriched vegetable oil and a second collector for molecules of interest-enriched ethanol. The extraction process includes: controlling the pressures to subject each of the vegetable oil and the ethanol to a pressure, so the interface between the two fluids is positioned at the junction point of inlets, bringing the vegetable oil and ethanol into contact with each other in the main channel for a time to enable extraction of the molecules of interest, collecting the molecules of interest-enriched ethanol, optionally, evaporating the ethanol, collecting the triglycerides-enriched vegetable oil.

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.

A liquid-liquid extraction system includes extraction stages, a pumping system, and a controller. Each extraction stage has a chamber, a primary input, a raffinate output, and an extract output. An input liquid (e.g., either a source liquid or raffinate from a preceding extraction stage, mixed with an extraction liquid) is presented to the chamber via the primary input. The chamber enables phase separation of liquid therein, into a raffinate and a extract, where the raffinate exits the separation vessel at the raffinate output, and the extract exits the separation vessel at the extract output. A level sensor is coupled to the chamber and the controller is operatively programmed to read an output of the level sensor, compare the output of the level sensor to a target, and cause the associated chamber to receive additional liquid if the output is lower than the target.

The present invention relates to a method of purifying waste hydrochloric acid, and more particularly, to a method of purifying waste hydrochloric acid which includes preparing an extraction solution by dissolving an extractant in an organic solvent (S1), extracting metallic components with the organic solvent by adding the extraction solution to the waste hydrochloric acid (S2), separating a waste hydrochloric acid layer and the organic solvent containing the metallic components (S3), and obtaining purified hydrochloric acid by recovering the separated (fractionated) waste hydrochloric acid layer (S4), wherein the extractant is used in an amount of 40 moles or more based on 1 mole of iron (Fe) included in the waste hydrochloric acid, and the waste hydrochloric acid and the extraction solution are mixed in a volume ratio of 1:0.1 to 1:1.

A purification processing apparatus for supplying purified isopropyl alcohol to a substrate processing apparatus. The purification processing apparatus includes: a processing chamber in which unpurified isopropyl alcohol and ionic liquid are mixed, and the isopropyl alcohol and the ionic liquid are separated to purify the isopropyl alcohol; an unpurified solvent supply port configured to supply the unpurified isopropyl alcohol to the processing chamber; an ionic liquid supply port configured to supply the ionic liquid to the processing chamber; and a purified solvent outlet configured to supply the purified isopropyl alcohol from the processing chamber to the substrate processing apparatus.

The interaction system that causes an interaction between a first fluid and a second fluid includes a plurality of processing units configured so as to cause the second fluid separated in the separation container of each of the plurality of processing units to flow into the processing channel of the interaction unit of a processing unit that is next in flow order to the each of the plurality of processing units, the separation container of the each of the plurality of processing units is connected to the processing channel of the interaction unit of the processing unit that is next in the flow order, a first fluid feeding path that leads the first fluid separated in the separation container of a succeeding stage processing unit among the plurality of processing units from the separation container to the processing channel of the interaction unit of a preceding stage processing unit, a storage container that stores the first fluid led out from the separation container of the succeeding stage processing unit to the first fluid feeding path, and a delivery fluid supply unit that supplies a delivery fluid to the storage container so that the first fluid in the storage container is pushed out by the delivery fluid to flow through the first fluid feeding path into the processing channel of the preceding stage processing unit.

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.

Centrifugal contactors that can be used for mixing or separating materials are described. The contactors include a sensing system including a communications fiber within the shaft of the contactors and access ports providing access from the communications fiber to the mixing/separating zone of the contactor. The sensing system can be utilized during operation of the contactor and can provide for detailed and accurate on-line characterization of a protocol, as well as process control and system modification as necessary during operation.