Abstract:
A process for the preparation of Group II and Group III lube oil base stocks wherein liquid-continuous aromatics saturation is used to treat lube hydrocrackate. The treated hydrocrackate is then be sent to dewaxing unit and then optionally to a hydrotreating step.
Abstract:
A process is presented for treating crude oil that contains a clathrate hydrate inhibitor. In the process, a crude oil contaminated with the inhibitor is maintained in a vessel at inhibitor removal conditions to produce a treated crude oil having a reduced methanol concentration.
Abstract:
In the present invention, pyrolysis oil is processed in a well mixed or a back mixed reactor to prevent the plugging up of a reactor that otherwise occurs. The pyrolysis oil can then be further upgraded in a hydroprocessing reactor through use of an appropriate catalyst.
Abstract:
L'invention concerne un procédé d'hydroconversion de charges lourdes carbonées comportant une étape (1) d'hydroconversion de la charge dans au moins un réacteur contenant un catalyseur en lit bouillonnant puis une étape (2) d'hydroconversion d'une partie au moins de l'effluent obtenu dans au moins un réacteur contenant un catalyseur en slurry.
Abstract:
Recovering crude oil by separating and removing valuable hydrocarbon, water and solid components from sludge or an emulsion. A sludge or an emulsion with added reagents of predefined ratio is received to form a mixture for treatment. The mixture is processed to break a micelle structure of the sludge or the emulsion. The mixture is agitated to allow homogenization thereof. The processed mixture is centrifuged to separate hydrocarbons, water and solids from the sludge or the emulsion. The separated hydrocarbons are tested to ensure separated solids are disposed as environmentally safe materials. Basis solids and water contents of separated hydrocarbons are tested. The separated hydrocarbons are separated, and the filtered hydrocarbons (i.e., the recovered crude oil) are stored. The crude oil is thereby recovered from sludge or emulsion through a chemical exothermic reaction and centrifugation to resolve the emulsion into free water, solids and hydrocarbons.
Abstract:
According to the invention, there is provided a method for treating heavy crude oil (HCO) which includes the steps of combining the HCO with an alkane containing solvent to form an HCO/solvent mixture, sonicating this mixture at audio frequency to precipitate asphaltenes from the HCO/solvent mixture, and separating the precipitated asphaltenes from the HCO/solvent mixture.
Abstract:
The invention provides a metal alloy fuel catalyst for decontaminating a hydrocarbon fuel, including diesel and bio-diesel fuel, of a bacterial contamination. The metal alloy fuel catalysts preferably includes about 70% Sn, about 22% Sb, about 4% Bi, and about 4% Pb, although other formulations are possible. The fuel catalyst can take the form of an in-line component in a fuel system or be coated within a fuel storage container.
Abstract:
The present invention provides a process for the treatment of crude oil or aged crude oil residue comprising the steps of (a) contacting the oil or residue with a phenol resin and with a diluent, to provide a diluted phenol resin treated oil or residue; and (b) optionally removing solid material from the diluted phenol resin treated oil or residue.
Abstract:
A method of augmenting the separation of immiscible heavier and lighter components of an emulsion including the steps of conducting the emulsion into a treatment vessel (10), providing an AC voltage source (46), employing from the source an AC voltage of at least one selected frequency F1 (42) to establish at least one electric field (28, 30) within the vessel (10) through which the emulsion passes, and cyclically modulating the AC voltage (42) with a method of modulation (44) selected from: (a) amplitude modulation; (b) frequency modulation; and (c) combined amplitude and frequency modulation.
Abstract:
A process for the production of low sulfur, low olefin gasoline wherein a cracked naphtha, such as a full boiling range cracked naphtha, is first separated by fractional distillation into at least two fractions while simultaneously selectively hydrogenating the polyunsaturated compounds contained therein. The mono olefins in the light fraction are then subjected to etherification with alcohol to produce ethers or hydration with water to produce alcohols. The heavy fraction is subjected to sulfur removal by hydrodesulfurization or chemisorption. The two fractions are then combined to produce a low sulfur, low olefin gasoline.