B01D15/00

METHOD FOR SEPARATING DRILL FLUID FROM OILY DRILL CUTTINGS SLURRIES
20230032931 · 2023-02-02 ·

The present invention provides a method for separating oily drill fluid from an oily drill cuttings slurry comprising oily drill fluid and drill cuttings. The method comprises destructively modifying at least a portion of the drill cuttings that are contacted by at least one cuttings-reactive chemical thereby disrupting attraction forces between the portion of the drill cuttings and the oily drill fluid and making it easier for mechanical cuttings treatment equipment to separate oily drill fluid from the oily drill cuttings slurry.

METHOD FOR SEPARATING DRILL FLUID FROM OILY DRILL CUTTINGS SLURRIES
20230032931 · 2023-02-02 ·

The present invention provides a method for separating oily drill fluid from an oily drill cuttings slurry comprising oily drill fluid and drill cuttings. The method comprises destructively modifying at least a portion of the drill cuttings that are contacted by at least one cuttings-reactive chemical thereby disrupting attraction forces between the portion of the drill cuttings and the oily drill fluid and making it easier for mechanical cuttings treatment equipment to separate oily drill fluid from the oily drill cuttings slurry.

METHOD FOR EXTRACTING LOW-MOLECULAR-WEIGHT SUBSTANCE EXISTING IN BIOLOGICAL SAMPLE
20230029620 · 2023-02-02 · ·

A method for extracting a low-molecular-weight substance existing in a biological sample, including: 1) an adsorption step of adsorbing the substance on porous carbon by mixing the biological sample with the porous carbon having mesopores of 3.5 nm to 150 nm and micropores of a larger size as a hierarchical structure, and recovering the porous carbon from the obtained mixture, or by bringing the biological sample into contact with a filtration filter on which the porous carbon is disposed or supported; and 2) a releasing step of releasing the low-molecular-weight substance from the porous carbon by mixing the porous carbon obtained after the adsorption step with an aqueous solution containing 0.1 mass % to 1 mass % of spherical silica having an average particle diameter of 10 nm to 100 nm and containing 10% to 12% of acetonitrile, or by causing the filtration filter to contact and pass through the aqueous solution.

CHEMICAL LIQUID PURIFICATION METHOD AND CHEMICAL LIQUID

An object of the present invention is to provide a chemical liquid purification method which makes it possible to obtain a chemical liquid having excellent defect inhibition performance. Another object of the present invention is to provide a chemical liquid. The chemical liquid purification method according to an embodiment of the present invention is a chemical liquid purification method including obtaining a chemical liquid by purifying a substance to be purified containing an organic solvent, in which a content of the stabilizer in the substance to be purified with respect to the total mass of the substance to be purified is equal to or greater than 0.1 mass ppm and less than 100 mass ppm.

MODIFIED CLAY SORBENTS AND METHODS OF SORBING PFAS USING THE SAME
20220339600 · 2022-10-27 ·

A method of sorbing a PFAS compound from a contaminated environment can include admixing a modified clay sorbent with the environment. The modified clay can include a clay intercalated with a blend of mono-quaternary amine compound and di-quaternary amine compound.

Method of preparing composition containing factor VIII (FVIII) and von Willebrand factor (vWF) with controlled content of von Willebrand factor (vWF)

Disclosed is a method for preparing a composition comprising factor VIII (FVIII) and von Willebrand factor (vWF), wherein the content of the von Willebrand factor (vWF) can be controlled by mixing the factor VIII (FVIII) with the von Willebrand factor (vWF) at an appropriate ratio after separately purifying the factor VIII (FVIII) and the von Willebrand factor (vWF) from plasma in a single process. The method can prepare and purify a composition comprising factor VIII (FVIII) and a varying content of von Willebrand factor (vWF) without increasing the amount of impurities other than the von Willebrand factor (vWF) compared to a method of purifying factor VIII (FVIII) separately, without significantly increasing the processing time (within 3 hours) compared to a method of purifying factor VIII (FVIII), and without changing the yield of factor VIII (FVIII).

METAL-ORGANIC FRAMEWORKS FOR p-Cresyl SULFATE ADSORPTION

Provided herein is a method for removing uremic toxins from blood is provided. The method includes exposing blood to iron-based metal-organic frameworks; and allowing the metal-organic frameworks to bind a least one uremic toxin in the blood.

METAL-ORGANIC FRAMEWORKS FOR p-Cresyl SULFATE ADSORPTION

Provided herein is a method for removing uremic toxins from blood is provided. The method includes exposing blood to iron-based metal-organic frameworks; and allowing the metal-organic frameworks to bind a least one uremic toxin in the blood.

Porous fiber, adsorbent material, and purification column

A solid fiber is described, where the solid fiber is characterized by (a) a modification degree Do/Di, in a cross section of the solid fiber of 1.20 to 8.50 where the inscribed circle diameter is denoted by Di and the circumscribed circle diameter is denoted by Do; and (b) a porous specific surface area of not less than 30 m.sup.2/g.

Porous fiber, adsorbent material, and purification column

A solid fiber is described, where the solid fiber is characterized by (a) a modification degree Do/Di, in a cross section of the solid fiber of 1.20 to 8.50 where the inscribed circle diameter is denoted by Di and the circumscribed circle diameter is denoted by Do; and (b) a porous specific surface area of not less than 30 m.sup.2/g.