78 results about "Isohexanes" patented technology

The present invention relates, in part, to ternary azeotropic compositions and mixtures including chlorotrifluoropropene, methanol, and a third component selected from isohexane, trans-1,2-dichloroethylene, and petroleum ether. The present invention further relates to ternary azeotropic compositions and mixtures including chlorotrifluoropropene, cyclopentane, and a alcohol selected from methanol, ethanol, and isopropanol.

The invention relates to a light hydrocarbon isomerization method comprising the following steps: light hydrocarbon materials are firstly separated by a de-isopentane tower, tower top streams are extracted as isomerization products, and tower bottom streams enter a front isomerization reactor to generate isomerization reaction; liquid phase streams obtained by the gas-liquid separation of outlet streams of the front reactor are separated in a de-isohexane tower, and tower top streams and tower bottom streams of the de-isohexane tower are extracted and then mixed with the tower top streams of the de-isopentane tower and are together taken as a gasoline-stripping stabilization system of the isomerization products; siding streams of the de-isohexane tower are extracted into a rear isomerization reactor; and liquid phase streams obtained by the gas-liquid separation of reaction streams of the rear isomerization reactor completely return and are mixed with the liquid phase streams of a gas-liquid separator of the front isomerization reaction system and together taken as feeding materials of the de-isohexane tower. The method has higher normal paraffin isomerization ratio, wherein the C6 normal paraffin realizes the complete isomerization basically, thereby greatly improving the octane number of the light hydrocarbon materials.

The invention relates to a method and a device for separating n-hexane, isohexane and benzene. The device comprises a light component removal unit, an isohexane separation unit, an n-hexane extractive distillation unit, a first solvent recovery unit, a benzene extractive distillation unit, a second solvent recovery unit and a solvent regeneration unit. The method comprises the following steps: removing impurities with a boiling point less than the boiling point of 2-methylpentane in mixed hydrocarbon raw materials such as raffinate oil, pyrolysis gasoline or straight-run gasoline and the like from an aromatics extraction device firstly, and then separating an isohexane product; separating a n-hexane product from other materials by using an extractive distillation method; and removing n-hexane materials, and carrying out separation on the obtained product so as to obtain a benzene product. The main components of the isohexane product produced by using the technique disclosed by the invention are 2-methylpentane and 3-methylpentane, and the total mass fraction of 2-methylpentane and 3-methylpentane is not less than 95%; n-hexane meets the national standard GB16629-2008, and the mass fraction is not less than 99%; and the benzene product meets the national standard GB3405-89.