The invention relates to the oil-refining industry, in particular, to methods for purifying a fuel from sulfur-containing compounds. The method for purifying liquid hydrocarbon motor fuels from sulfur and for further reducing the sulfur dioxide content in exhaust gases up to zero during combustion of the fuels by modifying the sulfur-containing fuel molecules in a fully-developed cavitation mode, by separating the sulfur-containing modified molecules from the remainder of the fuel molecules on polymer membranes and by activating the fuel purified up to 20 ppm in the fully-developed cavitation mode prior to the combustion. What is novel is that the reduction of the sulfur content in the fuel is achieved by means of treating the fuel or a fuel fraction in the fully-developed cavitation mode with addition of a hydrogen peroxide aqueous solution and/or a strong aqueous solution of iron oxides to the fuels, followed by separating the obtained emulsion into a fuel fraction and a water-paraffin emulsion, followed by separating the fuel fraction on the membranes under the temperature of from 90 C. to 180 C. under the atmospheric pressure into a fuel fraction having a low sulfur content and a fuel fraction having an increased sulfur content. Reduction of the sulfur dioxide in the exhaust gases during combustion of the purified fuels up to zero by means of activation of the fuels having the low sulfur content in the fully-developed cavitation mode is performed without addition of other chemical substances. Production of a reduced oil-water emulsion from the water-paraffin emulsion and the fuel fraction having the increased sulfur content that increases the efficiency of reduced oils combustion is performed in boiler units. Reduction of the sulfur content in the fuel or fuel fractions is performed up to the required level of 20 ppm or less. Treatment of the initial fuel or fuel fraction by the cavitation is performed under the pressure of 1.0-0.5.0 atm and the temperature of 20 C.-70 C.

Oxidized disulfide oil (ODSO) solvent compositions are derived from by-product disulfide oil (DSO) compounds produced as by-products from the generalized mercaptan oxidation (MEROX) processing of a refinery feedstock. The oxidized disulfide oil (ODSO) solvent compositions comprise at least a primary oxidized disulfide oil (ODSO) compound selected from either water soluble or water insoluble oxidized disulfide oil (ODSO) compounds and in some embodiments at least 0.1 ppmw of a secondary oxidized disulfide oil (ODSO) compound that is a water soluble oxidized disulfide oil (ODSO) compound.

Oxidized disulfide oil (ODSO) solvent compositions are derived from by-product disulfide oil (DSO) compounds produced as by-products from the generalized mercaptan oxidation (MEROX) processing of a refinery feedstock. The oxidized disulfide oil (ODSO) solvent compositions comprise at least a primary oxidized disulfide oil (ODSO) compound selected from either water soluble or water insoluble oxidized disulfide oil (ODSO) compounds and in some embodiments at least 0.1 ppmw of a secondary oxidized disulfide oil (ODSO) compound that is a water soluble oxidized disulfide oil (ODSO) compound.

Systems and methods for reducing olefin concentration in a hydrocarbon stream comprising aromatic compounds and olefins, the method including supplying an aromatic-rich olefinic hydrocarbon stream; combining the aromatic-rich olefinic hydrocarbon stream with a catalyst; heating the aromatic-rich olefinic hydrocarbon stream and the catalyst to effect a reaction selected from the group consisting of: oxidation of olefins; hydration of olefins; and combinations of the same; separating an aqueous phase from a produced hydrocarbon phase; and separating C.sub.7 compounds from C.sub.8+ compounds in the produced hydrocarbon phase.

Systems and methods for reducing olefin concentration in a hydrocarbon stream comprising aromatic compounds and olefins, the method including supplying an aromatic-rich olefinic hydrocarbon stream; combining the aromatic-rich olefinic hydrocarbon stream with a catalyst; heating the aromatic-rich olefinic hydrocarbon stream and the catalyst to effect a reaction selected from the group consisting of: oxidation of olefins; hydration of olefins; and combinations of the same; separating an aqueous phase from a produced hydrocarbon phase; and separating C.sub.7 compounds from C.sub.8+ compounds in the produced hydrocarbon phase.

A system for processing fuel to remove sulfur species through the oxidation of the sulfur species is disclosed which includes one or more (and preferably two or more processing units). Additionally, a method of removing sulfur species through the oxidation of the sulfur species is also disclosed. The system and the method rely on the use of aqueous and does not require the removal (through sorption or the like) at each or between each processing unit. Such a configuration for numerous reasons is economically advantageous.

A system for processing fuel to remove sulfur species through the oxidation of the sulfur species is disclosed which includes one or more (and preferably two or more processing units). Additionally, a method of removing sulfur species through the oxidation of the sulfur species is also disclosed. The system and the method rely on the use of aqueous and does not require the removal (through sorption or the like) at each or between each processing unit. Such a configuration for numerous reasons is economically advantageous.

An integrated controlled catalytic oxidation process converts low value disulfide oil (DSO) compounds produced as a by-product of a generalized mercaptan oxidation (MEROX) process into oxidized DSO (ODSO) compounds including sulfoxides, sulfones, sulfonates and sulfinates that are completely or partially water soluble and which have utility, e.g., as lubricity additives in diesel fuel and as a solvent in aromatic solvent separation processes.

Oxidized disulfide oil (ODSO) solvent compositions are derived from by-product disulfide oil (DSO) compounds produced as by-products from the generalized mercaptan oxidation (MEROX) processing of a refinery feedstock. The oxidized disulfide oil (ODSO) solvent compositions comprise at least a primary oxidized disulfide oil (ODSO) compound selected from either water soluble or water insoluble oxidized disulfide oil (ODSO) compounds and in some embodiments at least 0.1 ppmw of a secondary oxidized disulfide oil (ODSO) compound that is a water soluble oxidized disulfide oil (ODSO) compound.

Oxidized disulfide oil (ODSO) solvent compositions are derived from by-product disulfide oil (DSO) compounds produced as by-products from the generalized mercaptan oxidation (MEROX) processing of a refinery feedstock. The oxidized disulfide oil (ODSO) solvent compositions comprise at least a primary oxidized disulfide oil (ODSO) compound selected from either water soluble or water insoluble oxidized disulfide oil (ODSO) compounds and in some embodiments at least 0.1 ppmw of a secondary oxidized disulfide oil (ODSO) compound that is a water soluble oxidized disulfide oil (ODSO) compound.