C10G75/04

Means and methods for managing ammonia, amine and normal salt fouling in oil production and refining

Methods for use in treating hydrocarbon streams are provided. The methods of the present disclosure include; introducing one or more alcohols into a hydrocarbon stream that includes one or more hydrolyzable chloride compounds; allowing the one or more alcohols to interact with, the one or more hydrolyzable chloride compounds; and increasing: one of a solubility value or a dispersancy value of at least a portion of the hydrolyzable chloride compounds in the hydrocarbon steam.

DRAG REDUCTION OF ASPHALTENIC CRUDE OILS

The process begins by obtaining a first batch of monomers selected from a group of acrylates with a molecular weight equal to or less than butyl acrylate and/or methacrylate with a molecular weight equal to or less than butyl methacrylate. A second batch of monomers is then selected from a group of acrylates with a molecular weight greater than butyl acrylate and/or methacrylate with a molecular weight greater than butyl methacrylate. A mixture is then prepared by mixing the first batch of monomers and the second batch of monomers, wherein the second batch of monomers are greater than 50% by weight of the mixture. Finally, the mixture is polymerized to produce a drag reducing polymer. The drag reducing polymer is capable of imparting drag reducing properties in liquid hydrocarbons.

DRAG REDUCTION OF ASPHALTENIC CRUDE OILS

The process begins by obtaining a first batch of monomers selected from a group of acrylates with a molecular weight equal to or less than butyl acrylate and/or methacrylate with a molecular weight equal to or less than butyl methacrylate. A second batch of monomers is then selected from a group of acrylates with a molecular weight greater than butyl acrylate and/or methacrylate with a molecular weight greater than butyl methacrylate. A mixture is then prepared by mixing the first batch of monomers and the second batch of monomers, wherein the second batch of monomers are greater than 50% by weight of the mixture. Finally, the mixture is polymerized to produce a drag reducing polymer. The drag reducing polymer is capable of imparting drag reducing properties in liquid hydrocarbons.

USE OF A PARAFFINIC HYDROCARBON-BASED FUEL COMPOSITION FOR CLEANING THE INTERNAL PARTS OF DIESEL ENGINES

The present invention relates to the use of a fuel composition comprising at least 85% by weight of one or more hydrocarbon fractions consisting of one or more hydrotreated vegetable oils, said fraction(s) having a distillation range between 100 and 400° C. and having a paraffin content greater than or equal to 90% by weight, for reducing the deposits present in the internal parts of a compression ignition engine (or diesel engine). The present invention also relates to a method for cleaning the deposits present in the internal parts of a compression ignition engine using such a composition.

Solvent and temperature assisted dissolution of solids from steam cracked tar

Processes for preparing a low particulate liquid hydrocarbon product are provided and include blending a tar stream containing particles with a fluid and heating to a temperature of 250° C. or greater to produce a fluid-feed mixture that contains tar, the particles, and the fluid. The fluid-feed mixture contains about 20 wt % or greater of the fluid, based on a combined weight of the tar stream and the fluid. Also, about 25 wt % to about 99 wt % of the particles in the tar stream are dissolved or decomposed when producing the fluid-feed mixture.

Solvent and temperature assisted dissolution of solids from steam cracked tar

Processes for preparing a low particulate liquid hydrocarbon product are provided and include blending a tar stream containing particles with a fluid and heating to a temperature of 250° C. or greater to produce a fluid-feed mixture that contains tar, the particles, and the fluid. The fluid-feed mixture contains about 20 wt % or greater of the fluid, based on a combined weight of the tar stream and the fluid. Also, about 25 wt % to about 99 wt % of the particles in the tar stream are dissolved or decomposed when producing the fluid-feed mixture.

Treatment composition and method for reducing viscosity of hydrocarbons
11279887 · 2022-03-22 · ·

A treatment composition for reducing viscosity, pour point, and precipitate content of a hydrocarbon fluid at temperatures below 90° F., preferably 34° F. to 90° F. The treatment composition includes one or more mixed fatty acid methyl esters, an aromatic mixture consisting essentially of C.sub.9 to C.sub.15 aromatic compounds, and a main solvent consisting essentially of low odor kerosene, low odor diesel, or a mixture of low odor diesel or low odor kerosene. The treatment composition solubilizes hydrocarbon deposits for removal. The treatment composition also solubilizes paraffins and asphaltenes in a hydrocarbon fluid to prevent or mitigate the formation of hydrocarbon deposits.

Treatment composition and method for reducing viscosity of hydrocarbons
11279887 · 2022-03-22 · ·

A treatment composition for reducing viscosity, pour point, and precipitate content of a hydrocarbon fluid at temperatures below 90° F., preferably 34° F. to 90° F. The treatment composition includes one or more mixed fatty acid methyl esters, an aromatic mixture consisting essentially of C.sub.9 to C.sub.15 aromatic compounds, and a main solvent consisting essentially of low odor kerosene, low odor diesel, or a mixture of low odor diesel or low odor kerosene. The treatment composition solubilizes hydrocarbon deposits for removal. The treatment composition also solubilizes paraffins and asphaltenes in a hydrocarbon fluid to prevent or mitigate the formation of hydrocarbon deposits.

Processes for thermal upgrading of heavy oils utilizing disulfide oil

A process for upgrading a heavy oil includes passing heavy oil and disulfide oil to a thermal cracking system that includes a thermal cracking unit and a cracker effluent separation system downstream of the thermal cracking unit and thermally cracking at least a portion of the heavy oil in the presence of the disulfide oil in the thermal cracking unit to produce solid coke and a cracking effluent comprising reaction products. The reaction products include one or more liquid reaction products, one or more gaseous reaction products, or both. The presence of the disulfide oil in the thermal cracking unit promotes conversion of hydrocarbons from the heavy oil to the liquid reaction products, the gaseous reaction products, or both relative to the production of the solid coke.

MEANS AND METHODS FOR MANAGING AMMONIA, AMINE AND NORMAL SALT FOULING IN OIL PRODUCTION AND REFINING

Methods for use in treating hydrocarbon streams are provided. The methods of the present disclosure include; introducing one or more alcohols into a hydrocarbon stream that includes one or more hydrolyzable chloride compounds; allowing the one or more alcohols to interact with, the one or more hydrolyzable chloride compounds; and increasing: one of a solubility value or a dispersancy value of at least a portion of the hydrolyzable chloride compounds in the hydrocarbon steam.