An extraction system includes an extractor that carries out an extraction treatment of bringing a raw material liquid into contact with an extraction liquid so that metal ions are extracted from the raw material liquid to migrate to the extraction liquid, a raw material liquid return path that leads the raw material liquid from a separator to a raw material liquid tank; and a raw material liquid pH regulator addition apparatus connected to a raw material liquid pH adjustment place that is one of the raw material liquid tank and the raw material liquid return path, the raw material liquid pH regulator addition apparatus configured to add a raw material liquid pH regulator to the raw material liquid, the raw material liquid pH regulator being a pH regulator that increases pH of the raw material liquid that have been decreased by the extraction treatment.

A semi-aqueous method for extracting a substance. The method involves combining a first liquid or solid substance containing an extract with a semi-aqueous solution containing a water-soluble or water-emulsifiable (WSWE) compound. Said WSWE compound selectively dissolves extract during a dense phase CO.sub.2 expansion and salting-out process, which is simultaneously co-extracted using said dense phase CO.sub.2, and desolvated to produce a CO.sub.2 salted-out solvent mixture containing extract. Said CO.sub.2 salted-out solvent mixture is treated using various secondary processes. The present invention is useful for producing extracts for use as additives in pharmaceuticals, nutraceuticals, cosmetics, beverages, or foods, and for quantitative analysis.

Improvements in extraction techniques are described. The improved extraction is provided by an outlet flow controller nut which enhances the efficiency of the collection of compounds as they are extracted from supercritical CO.sub.2. An improved extraction apparatus which includes precise computer controls based on the properties of supercritical CO.sub.2 is also described. The extraction apparatus enables a human operator to extract compounds from organic material with a minimum of intervention and with greater precision that conventional extraction apparatus, which often requires frequent adjustment and yields imprecise results.

The present invention provides a portable extraction device for extracting at least one constituent from a substance by an extraction fluid. The extraction device comprises at least one pump, an extractor, an evaporator, and a condenser. The substance and the extraction fluid are placed and mixed in the extractor. The extraction fluid is a subcritical fluid. The constituent in the substance will be dissolved in the extraction fluid under a predetermined pressure and temperature. The evaporator receives the extraction fluid including the constituent from the extractor, and heats the extraction fluid including the constituent to gasify the extraction fluid and separate the constituent from the gasified extraction fluid. The condenser receives the gasified extraction fluid via a first pipe, liquefies the gasified extraction fluid, and transmits the liquefied extraction fluid to the extractor via a second pipe. The extractor, the evaporator, and the condenser are operated under constant pressure.

Systems and techniques for demulsifier automation of the wet crude handling facilities can include a computer-implemented method. Demulsifier automation parameters for automating demulsifier injection points of a wet crude handling facility are determined. The determining includes performing a data convolution and a smoothening of inlet demulsifier automation parameters. Performing the demulsifier automation of the wet crude handling facility, includes, for each demulsifier, the following: A current state of the demulsifier is identified based on the demulsifier automation parameters. Demulsifier calculation input parameters are determined, including performing a convolution and a smoothening of the demulsifier calculation input parameters. A demulsifier dosage rate is calculated using the determined demulsifier calculation input parameters. A state dependent dosage multiplication factor is applied to the demulsifier based on the current state based on the calculated demulsifier dosage rate.

The invention relates to a device and to a method for separating two immiscible fluids (2, 3), wherein a three-phase system is formed with a Winsor III type bicontinuous phase (4) so as to phagocytize the dispersed droplets and to produce a droplet-free liquid (2).

The present invention relates to the field of upgrading biomass, in particular algal biomass, and more specifically the present invention relates to a method for extracting water-soluble compounds from microalgae and/or cyanobacteria, as well as the product obtained by this method and the uses of same, in particular in the food industry or as food supplements.

A method for extracting resins and oils from a plant includes: 1) tumbling, inside a container at a temperature of at most 50 degrees Fahrenheit with a tumbler, plant fibers having one or more portions that contain resins and/or oils; 2) colliding the tumbler with the plant fibers to release the one or more portions that contain resins and/or oils from the remainder of the plant fibers; and 3) segregating the one or more portions that contain resins and/or oils from the remainder of the plant fibers.

Methods of removing target impurities from a crude lithium bis(fluorosulfonyl)imide (LiFSI) to make a purified LiFSI product. In some embodiments, a purification method includes contacting crude LiFSI with a first anhydrous organic solvent to create a solution containing LiFSI and the target impurity(ies), wherein the LiFSI is soluble and the impurity(ies) is/are substantially insoluble. In some embodiments, a second anhydrous organic solvent is added to the solution to precipitate the target impurity(ies), which is then filtered to obtain a filtrate. In some embodiments, solvent is removed from the filtrate to obtain a solid mass containing LiFSI, which may then be contacted with a third anhydrous organic solvent in which the LiFSI is insoluble. The LiFSI may then be isolated from the third anhydrous organic solvent to obtain the purified LiFSI product. Also disclosed are purified LiFSI products and electrochemical devices utilizing purified LiFSI products, among other things.

A method of inhibiting degradation of an extractant by utilizing several auxiliary means in the DSX process: includes (a) preparing adjustment of the concentration of an extractant of a DSX solvent to a certain range; (b) extracting a metal contained in a pregnant leached solution by adjusting the ratio of the extractant and the diluent in the DSX solvent to a certain range; (c) measuring the pH of the aqueous phase solution by separating mixture into the aqueous phase solution and the organic phase solvent using a settler after step of extracting; (d) controlling the pH by adding soda ash (Na.sub.2CO.sub.3) so as to maintain the pH of the aqueous phase solution to be 3 to 7; and (e) scrubbing with scrubbing solution having a zinc concentration of 2 to 20 g/L by zinc sulfate (ZnSO.sub.4) to remove the manganese from the organic phase solvent containing the extracted metal.