The present invention describes novel Cashew Nut Shell Liquid derived cycloaliphatic functional compounds and methods for making the same. The invention also provide methods to use these derivatives in antimicrobials, antioxidants, adhesives, coatings, corrosion retardants composites, cosmetics, detergents, soaps, de-icing products, elastomers, food, flavors, inks, lubricants, oil field chemicals, tackifiers, prepolymer chain-extenders, rheology modifiers, electrical and electronic components (potting, castings, encapsulants), personal care products, polymers, structural polymers, engineered plastics, 3D printable polymers, 3D printable polymers, UV/E-beam/cationic curable polymers, techno-polymers, rubbers, sealants, solvents, surfactants and varnishes, transformer oil, lubricants.

A synthetic chiral composition comprising (i) pinene isomers; (ii) linalool isomers; and (iii) a terpene or terpenoid, and formulations comprising the synthetic chiral composition, in addition to methods for preparing, creating, populating, and querying databases pertaining to, and kits comprising, the synthetic chiral composition are disclosed herein. The composition further includes one or more modifiers. The composition includes organoleptic properties (e.g. aroma) of a plant cultivar (e.g. Cannabis).

A synthetic chiral composition comprising (i) pinene isomers; (ii) linalool isomers; and (iii) a terpene or terpenoid, and formulations comprising the synthetic chiral composition, in addition to methods for preparing, creating, populating, and querying databases pertaining to, and kits comprising, the synthetic chiral composition are disclosed herein. The composition further includes one or more modifiers. The composition includes organoleptic properties (e.g. aroma) of a plant cultivar (e.g. Cannabis).

A benzene selective hydrogenation reaction system and a method are provided. The system includes a benzene refiner, a first hydrogenation reactor, a second hydrogenation reactor and a separator which are connected in sequence. The first hydrogenation reactor is provided with a first inlet and a first outlet, and the second hydrogenation reactor is provided with a second inlet and a second outlet. The first inlet is connected to the discharge port of the benzene refiner; the first outlet is connected to the second inlet; the second outlet is connected to the separator. The catalyst outlet is connected to the first hydrogenation reactor for recycling the catalyst into the first hydrogenation reactor. Two micro-interface units are respectively disposed within the first hydrogenation reactor and the second hydrogenation reactor, and the micro-interface units are used for dispersing and breaking hydrogen into micro-bubbles with a micron-scale diameter.

A benzene selective hydrogenation reaction system and a method are provided. The system includes a benzene refiner, a first hydrogenation reactor, a second hydrogenation reactor and a separator which are connected in sequence. The first hydrogenation reactor is provided with a first inlet and a first outlet, and the second hydrogenation reactor is provided with a second inlet and a second outlet. The first inlet is connected to the discharge port of the benzene refiner; the first outlet is connected to the second inlet; the second outlet is connected to the separator. The catalyst outlet is connected to the first hydrogenation reactor for recycling the catalyst into the first hydrogenation reactor. Two micro-interface units are respectively disposed within the first hydrogenation reactor and the second hydrogenation reactor, and the micro-interface units are used for dispersing and breaking hydrogen into micro-bubbles with a micron-scale diameter.

Compositions and methods for repelling arthropods. The compositions include a carrier and an arthropod repelling compound, which can be a compound discovered by a novel and complex cheminformatic process to demonstrate repellency behavior across a broad spectrum of arthropods. The compound can be a thiane compound, a pyrrolidone compound, a cyclohexadiene compound, a cyclohexenone compound, a cyclohexene compound, a furanone compound, a pyran compound, a tetrahydropyran compound, a thiazolidine compound, a thiazoline compound, a dihydrothiophene compound, a dithiolane compound, a dithiane compound, an epoxide compound, an oxathiane compound, a cyclopentene compound, a cyclohexane compound, a quinoline compound, an oxazoline compound, a tetrahydropyridine compound, and an imidazolidinone compound, or a combination thereof.

Compositions and methods for repelling arthropods. The compositions include a carrier and an arthropod repelling compound, which can be a compound discovered by a novel and complex cheminformatic process to demonstrate repellency behavior across a broad spectrum of arthropods. The compound can be a thiane compound, a pyrrolidone compound, a cyclohexadiene compound, a cyclohexenone compound, a cyclohexene compound, a furanone compound, a pyran compound, a tetrahydropyran compound, a thiazolidine compound, a thiazoline compound, a dihydrothiophene compound, a dithiolane compound, a dithiane compound, an epoxide compound, an oxathiane compound, a cyclopentene compound, a cyclohexane compound, a quinoline compound, an oxazoline compound, a tetrahydropyridine compound, and an imidazolidinone compound, or a combination thereof.

Disclosed is a liquid production method and device for producing a liquid containing water-soluble components. The liquid production method includes extracting water-soluble components from a biological tissue, using a liquefied gas, to yield an extraction liquid, and vaporizing the liquefied gas from the extraction liquid obtained in the extracting to concentrate the extraction liquid.

Disclosed is a liquid production method and device for producing a liquid containing water-soluble components. The liquid production method includes extracting water-soluble components from a biological tissue, using a liquefied gas, to yield an extraction liquid, and vaporizing the liquefied gas from the extraction liquid obtained in the extracting to concentrate the extraction liquid.

The present disclosure provides processes to convert paraffins to corresponding olefins and or heavier hydrocarbons. In at least one embodiment, a process includes introducing, at a temperature of from about 50° C. to about 500° C., a hydrocarbon feed comprising paraffins to a first metal oxide comprising one or more group 1 to group 17 metal and one or more oxygen. The process includes obtaining a product mixture comprising one or more C3-C50 cyclic olefins, one or more C2-C50 acyclic olefins, one or more C5-C200 hydrocarbons, such as one or more C5-C100 hydrocarbons, or a mixture thereof. In at least one embodiment, the product mixture is substantially free of H2 (e.g., <500 ppm). The introducing can reduce the first metal oxide to form a second metal oxide. Processes may include introducing the second metal oxide to an oxidizing agent to form the first metal oxide.