A high-efficiency supercritical oil extraction method is provided. According to the method, in an early extraction stage, extraction is performed using an extractant along an extraction kettle from top to bottom; in a middle extraction stage, the extraction kettle is longitudinally flipped by 180 degrees, extraction is still performed using an extractant along the extraction kettle from top to bottom; in a later extraction stage, extraction is performed using a conventional extractant along the extraction kettle from bottom to top. Thus, the pressure effect and the critical extraction effect of the critical extractant are simultaneously exerted, thereby greatly improving the extraction efficiency of supercritical oil extraction, shortening the extraction time, and reducing the dosage of extractant, so as to achieve high-efficiency and low-cost oil extraction.

The present disclosure discloses processes for treating, producing, or producing and treating biodiesel. Products produced with the various processes of the present invention are also disclosed.

A system for purifying cannabis miscella is provided comprising a feed tank enabled to store the miscealla derived from cannabis extraction, a plurality of optical sensor modules, at least one valve, an ultrafiltration membrane module; and at least one pump. Wherein a closed system enabled to maintain a positive or negative pressure created by the at least one pump, enabling moving a flow of the miscealla through the system, one optical sensor is positioned upstream and downstream from the ultrafiltration membrane, the at least one valve is positioned between ultrafiltration membrane and an outlet, and a level of opening the valve creates different levels of back pressure based on readings from the optical sensors.

A lithium-generating system can include a lithium-containing source feed, a hardness reduction unit, and a bipolar electrodialysis or electrolysis unit. The lithium-containing source feed can provide a lithium-containing material. The hardness reduction unit can be configured to receive the lithium-containing material and reduce the hardness thereof yet still be over 10 ppm upon processing by the hardness reduction unit. The bipolar electrodialysis unit can process the lithium-containing material and generate an aqueous LiOH product. The hardness reduction unit is configured to produce a hardness level within a given hardness-reduced lithium-containing material to be within an upper operational limit of at least one bipolar membrane, in addition to being at a given hardness level of over 10 ppm. The lithium-generating system can further include components to facilitate production of Li.sub.2CO.sub.3 and/or LiOH.Math.H.sub.2O.

In various aspects, methods and apparatuses for liquid-liquid extraction are provided. In certain aspects, an emulsion can be formed by combining a feed stream, an extractant, and a surfactant. The feed stream comprises a plurality of distinct components including a first component to be removed therefrom. The feed stream may be selected from a group consisting of: a hydrocarbon feed stream and an azeotrope. Then, a portion of the first component is extracted from the feed stream (or emulsion) by contact with a superoleophobic and hygroscopic membrane filter that facilitates passage of the first component and extractant through the superoleophobic and hygroscopic membrane filter. A purified product is collected having the portion of the first component removed. Such methods are particularly useful for refining fuels and oils and separating azeotropes and other miscible component systems. Energy-efficient, continuous single unit operation apparatuses for conducting such separation techniques are also provided.

A lateral flow device is disclosed. The device comprises a test layer comprising a test region between opposite first and second end regions of the test layer, a first permeable layer having a first contact area in contact with the first end region, and a second permeable layer having a second contact area in contact with the first end region. The device further comprises a first non-permeable layer between the first and second permeable layers and having a third contact area with the first end region. The first contact area and the second contact area are separated by the third contact area. The device further comprises a sample pad in fluid contact with the first and second permeable layers for delivery of a sample fluid to the first and second contact regions. The second contact area is further from the second end region than the first contact area is from the second end region.

An object of the present invention is to provide a chemical liquid purification method by which a chemical liquid capable of inhibiting the occurrence of short in a semiconductor substrate manufactured by a photolithography process is obtained. Another object of the present invention is to provide a chemical liquid manufacturing method and a chemical liquid. The chemical liquid purification method of the present invention includes a purification step of filtering a liquid to be purified by using a filter, in which a filter satisfying a condition 1 or a condition 2 in the following test is used as the filter.

Test: 1,500 ml of a test liquid formed of the organic solvent is brought into contact with the filter for 24 hours under a condition of 23 C., and a content of particles containing at least one kind of metal selected from the group consisting of Fe, Al, Cr, Ni, and Ti in the test liquid after the contact satisfies a predetermined condition.

This disclosure provides systems and methods for direct production of lithium hydroxide by utilizing cation selective, monovalent selective, or preferably lithium selective membranes. Lithium selective membranes possess high lithium selectivity over multivalent and other monovalent ions and thus prevent magnesium precipitation during electrodialysis (ED) and also address the presence of sodium in most naturally occurring brine or mineral based lithium production processes.

A high-efficiency supercritical oil extraction method is provided. According to the method, in an early extraction stage, extraction is performed using an extractant along an extraction kettle from top to bottom; in a middle extraction stage, the extraction kettle is longitudinally flipped by 180 degrees, extraction is still performed using an extractant along the extraction kettle from top to bottom; in a later extraction stage, extraction is performed using a conventional extractant along the extraction kettle from bottom to top. Thus, the pressure effect and the critical extraction effect of the critical extractant are simultaneously exerted, thereby greatly improving the extraction efficiency of supercritical oil extraction, shortening the extraction time, and reducing the dosage of extractant, so as to achieve high-efficiency and low-cost oil extraction.

Disclosed is a process for the alteration of the ratio of the specific gravities of the oil and water phases resulting from the conversion of biomass to liquid products, the reduction of the conductivity and of metals of the product mixture, which each can aid in the removal of solids contained in the oil phase; and a liquid-liquid extraction method for partitioning desirable carbon containing compounds into the oil phase and undesirable carbon containing compounds into the water phase.