2693 results about "Residual oil" patented technology

An improved concentrated surfactant formulation and process for the recovery of residual oil from subterranean petroleum reservoirs, and more particularly an improved alkali surfactant flooding process which results in ultra-low interfacial tensions between the injected material and the residual oil, wherein the concentrated surfactant formulation is supplied at a concentration above, at, or, below its CMC, also providing in situ formation of surface active material formed from the reaction of naturally occurring organic acidic components with the injected alkali material which serves to increase the efficiency of oil recovery.

The invention discloses a method for cleaning an oil tank. The method for cleaning the oil tank is characterized by adopting the following sequential steps under the totally closed condition: crude oil transporting, inert gas filling, homogenic oil cleaning, warm water cleaning, tank ventilating, tank slag removing and other pure physical and mechanical cleaning methods. After the method is adopted for cleaning, above 95% of residual oil in the tank can be recycled and reused, so the comprehensive benefit is obvious; the tank is cleanly and thoroughly cleaned, and even the metal can be seen; and the flame operation standard can be realized in the tank.

The present invention relates to a pseudothin diaspore composition containing organic pore-expanding agent. Said composition contains 92-99.5 wt% of pseudothin diaspore and 0.5-8 wt% of organic pore-expanding agent, in which the crystallinity of pseudothin diaspore is 10-70%. In the pseudothin diaspore composition provided by said invention the organic pore-expanding agent content is low, after high-temperature calcination the alumina with large pore capacity and large pore diameter can be obtained. Said alumina can be used as carrier material for preparing hydrodemetalization catalyst for heavy oil, residual oil and short residuum specially.

The present invention provides a process and an additive package for removing oil from solid material recovered from a well bore, e.g., drill cuttings and produced sand. In this process, the solid material is passed from the well bore to a separation zone. An aqueous acidic solution containing a polymer substituted with an amino group is introduced to the separation zone containing the solid material along with a halogenating agent and optionally one or more surfactants. The polymer, halogenating agent, and optional surfactant constitute the additive package. The polymer substituted with an amino group is preferably chitosan, and the halogenating agent is preferably a sodium hypochlorite solution. The mixture formed in the separation zone is agitated to cause a product of a reaction between the polymer and the halogenating agent to contact the solid material and remove residual oil therefrom.

The invention discloses a hydrotreating guard catalyst for residual oil and application thereof. The catalyst has the advantages of large pore volume, large aperture, high porosity, rational pore distribution, larger external orifice, high pore canal penetrability and over 36 percent of 1,000nm pore canals, and is particularly applied to a hydrotreating method of a residual oil fixed bed to ensure that precipitated metals are uniformly deposited on the whole catalyst bed and impurities, namely vanadium and calcium, can be deposited inside the pore canals so as to improve the utilization ratio of pores and maintain long-period running.

The invention relates to a boiling bed hydrogenation catalyst and a preparation method. The boiling bed hydrogenation catalyst of the invention is spherical shape which diameter is 0.1mm to 0.8mm, and has appropriate amount of additives and hydrogenation of metal components, and has reasonable hole distribution. The catalyst preparation method of the invention is spherical carrier impregnation, the process of spherical carrier preparation is following: making catalyst carrier raw material which is in appropriate temperature into appropriate size grain, then spheroidizing the grain, heating the conglobation and making them into spherical catalyst carrier. The process for making the catalyst carrier raw material into the appropriate size grain is that wet stock passes screen stencil by mechanical action and generates grain. Between the processes of the making grain and nodularization, granular material primely is placed for a period of time or operates in low-speed in nodularization device for a period of time. The catalyst of the invention appropriately conducts the boiling bed hydrogenation for heavy oil, residual oil.

The invention discloses a hydrogenation method for processing heavy oil. Raw heavy oil is mixed with hydrogen, the mixture enters a hydrogenating protective reaction area, reaction effluent directly enters a hydrotreatment reaction area without separation and is subjected to hydrotreatment reaction, and at least two parallelly connected up-flow hydrogenating protective reactors which can be switched in turn are arranged in the hydrogenating protective area. A method of grading four hydrogenating protective agents is adopted and particularly favorable for removing metals, so that blockage is avoided, the service life of a main catalyst is prolonged and the operating period of a device is prolonged. A switchable operating method is adopted, and all catalysts having activity can be fully utilized; and compared with the prior art, the method has the advantages that: the running period of a residual oil hydrogenation device can be prolonged by 20 to 40 percent, so that the running efficiency of the residual oil hydrogenation device is improved and the economic efficiency is improved.

A process derived hydrogen donor solvent is used to increase the maximum resid conversion and conversion rate in an ebullated bed resid hydrocracker. The hydrogen donor solvent precursor is produced by hydroreforming reactions within the resid hydrocracker, recovered as the resin fraction from a solvent deasphalting unit, regenerated in a separate hydrotreater reactor, and recycled to the ebullated bed resid hydrocracker. The major advantage of this invention relative to earlier processes is that hydrogen is more efficiently transferred to the resin residual oil in the separate hydrotreater and the hydrogen donor solvent effectively retards the formation of coke precursors at higher ebullated bed resid hydrocracker operating temperatures and resid cracking rates.

A hdyrocatalyst for removing metals from residual oil is composed of a macroreticular aluminium carrier and the Mo and/or W and Co and/or Ni, which are carried by said carrier. It features that said carrier contains aluminium oxide (95-99 wt%) and halogen (1-5) and has lower acidity, resulting in high demetallizing activity and low carbon deposit.

A catalyst for residual oil hydrodemetalling, which is composed of a carrier containing two types of pores and metal components such as Mo and/or W and Co and/or Ni, fixes on the carrier. The distribution of the pores in the said carrier is: the volume percentage of 10-20nm diameter pores in the total pore volume is 35-80%, the volume percentage of 500-1200nm diameter pores in the total pore volume is 15-60%, and the volume percentage of the pores with diameters ú“10nm, ú¥20-ú“500nm and ú¥1200nm in the total pore volume is 5-40%. The process for preparing the carrier comprises the steps of: mixing an alumina precursor with a nonacid nitrogenous compound, molding and sintering. The catalyst in this invention can be used as the catalyst for crude oil and normal atmosphere residual oil hydrodemetalling.

A catalytic and cracking process of inferior oil is characterized by catalytic cracking the inferior oil to obtain light diesel fuel cut fraction, returning it to catalytic cracker to recycle, extracting the obtained heavy diesel fuel cut fraction from solvent, extracting residual oil and returning to catalytic cracker to recycle. It has higher recovery rate, better quality and more yield of product. It can be used for various inferior fuel heavy oils, catalytic raw materials, shale oil and coal tar.

The invention relates to a method for controlling the oil supply device of an automatic planetary transmission, comprising a main oil pump (HP), which is mechanically drivably connected to the drive shaft of an internal combustion engine (VM), and an auxiliary oil pump (ZP) that may be driven via a controllable electric motor, the automatic transmission (ATG) being part of a parallel hybrid powertrain of a motor vehicle having an input shaft (5), which may be connected via a separating clutch (K) to the drive shaft (2) of the internal combustion engine (VM) and is permanently drivably connected to the rotor (4) of an electric machine (EM).

In order to achieve an oil supply to the automatic transmission (ATG) as and when needed, it is provided that the current oil requirement (P_{HD<sub2>—</sub2>soll}) of the automatic transmission is determined as a function of at least one currently captured operating parameter, and that the delivery rate (P_ZP) of the auxiliary oil pump (ZP) is set, by a correspondingly actuation of the associated electric motor, in the combustion and combined driving mode below a minimum input speed of the main oil pump (HP) and in the electric driving mode to at least the total oil requirement, and at least in the combined driving mode above the minimum input speed of the main oil pump (HP) is set to at least the residual oil requirement exceeding the delivery rate (P_HP) of the main oil pump.

The invention provides an analog measurement method and a device of oil saturation in strata, which belong to a geophysical exploration testing method and an analog device. The analog measurement method of the oil saturation in the strata comprises the steps of simulating an actual stratum (manufacturing an artificial cemented rock core model), arranging an analog well, arranging an oil-water saturation monitoring system in the artificial cemented rock core model, constructing an electric field at the periphery of the wall of the well, obtaining the oil saturation illustrative charts of different pervious courses by measuring the change of the resistivity of the rock core model and the like. The method not only can well simulate and measure the underground geological condition but also can further learn the position of the residual oil of a reservoir and the change rule of the saturation, thereby learning and determining the oil accumulation reserves and the grade in the simulated stratum.

An improved oxidative process that employ a robust, non-aqueous, and oil-soluble organic peroxide oxidant for effective desulfurization and denitrogenation of hydrocarbons including petroleum fuels, hydrotreated vacuum gas oil (VGO), non-hydrotreated VGO, petroleum crude oil, synthetic crude oil from oil sand, and residual oil. Even at low concentrations and without the assistance of catalysts, the non-aqueous organic peroxide oxidant is extremely active and fast in oxidizing the sulfur and nitrogen compounds in the hydrocarbon feedstocks. Furthermore, the process generates a valuable organic acid by-product that is also used internally as the extractive solvent for effective removal of the oxidized sulfur and nitrogen from the hydrocarbons without the need of a final adsorption step. Novel process steps are also disclosed to substantially prevent yield loss in the oxidative process.

The invention provides a hydrotreating device which comprises a hydrotreating protection unit and a main hydrotreating unit, which are connected with each other in series, wherein the hydrotreating protection unit comprises a main hydrotreating protection reactor and a spare hydrotreating protection reactor, which are connected with each other in parallel, and the volume of the main hydrotreating protection reactor is larger than that of the spare hydrotreating protection reactor. The invention further provides the application of the hydrotreating device and a residual oil hydrotreating method. The method comprises the following steps of: introducing the residual oil and the hydrogen into the hydrotreating device, and alternately using the main hydrotreating protection reactor and the spare hydrotreating protection reactor in the process of hydrotreating, wherein the online time of the main hydrotreating protection reactor is longer than that of the spare hydrotreating protection reactor. The method provided by the invention is particularly suitable for machining the high-carbon content residual oil and the high-metal content residual oil. Furthermore, the bigger hydrotreating protection reactor is longer in online time, so that the invention is higher in reactor use ratio.

The invention relates to a catalysis conversion method for producing aromatic compounds. According to the method, poor quality heavy cycle oil and residual oil are subjected to a hydrotreating reaction in the presence of hydrogen gas and a hydrogenation catalyst, and the reaction products are separated to obtain gas, naphtha, hydrogenated diesel oil and hydrogenated residue oil, wherein the hydrogenated diesel oil enters a catalysis cracking device and is subjected to a cracking reaction in the presence of a catalysis cracking catalyst, the reaction products are separated to obtain dry gas, liquefied gas, catalytic gasoline containing rich benzene, toluene and xylene, catalytic light diesel oil, distillates with a distillation range of 250-450 DEG C, and an oil slurry, and the distillates with the distillation range of 250-450 DEG C are conveyed to a residue oil hydrotreating device so as to be recycled. According to the present invention, the residue oil hydrogenation condition is completely utilized to achieve saturation of the aromatic ring in the poor quality heavy cycle oil to the maximal degree, such that the hydrogenated diesel oil maximally produce benzene, toluene and xylene during catalysis cracking.

A recycling system has a pyrolysis apparatus (40) having a combustion section (42) for selectively combusting a carbon component in materials, and a gasification section (41) for pyrolyzing and gasifying the materials by using heat of combustion in the combustion section (42). The materials include residual oil from an atmospheric distillation unit (10), a vacuum distillation unit (20), and a decomposition unit (28), various wastes including waste plastics (181), wastes (182), and shredder dust (183), and organic matter such as biomass (184). The recycling system has a passage for supplying pyrolysates (120) produced in the gasification section (41) to an oil refinery system or a petrochemical system.

The invention provides a method for preparing needle coke. The method is as follows: after delayed coking treatment of fraction or residual oil which are rich in arene through a certain temperature rise formula, green coke obtained is calcined, and the needle coke with high intermediate phase content and developed needle structure are prepared. The petroleum raw materials used comprise mixture of one type or a plurality of types among virgin wax oil, coked wax oil, catalytic cracking clarified oil, ethylene tar, coal tar, dense oil, residual oil and other hydrocarbon-enriched substances. The delayed coking temperature rise formula is characterized in that: intermediate phases generated can be driven to grow fully and are flushed by air flow with enough flow rate before solidification, thereby the granularity of the needle coke prepared is large (the content of coke breeze is not more than 25 weight percent) and the needle coke can be used for large-scale steel-making electric furnaces. When the method is used for an industrial device, people only need to adjust the prior temperature rise formula according to the characteristics of the raw materials and the technological flow.

The invention provides a hydrogenation method for residual oil. The method includes the following steps: under the condition of hydrogenation reaction, residual oil raw materials and hydrogen gas are sequentially guided into two hydrogenation reaction zones connected in series to carry out contact reaction with a plurality of catalyst beds in the hydrogenation reaction zones; according to the flowing directions of a reactant and the hydrogen gas, the first and second hydrogenation reaction zones respectively comprise a hydrogenation protecting catalyst, a hydrogenation de-metallization catalyst and a hydrogenation desulfurization catalyst which are sequentially filled in the catalyst beds; when the pressure drop of at least one catalyst bed in the first hydrogenation reaction zone reaches the upper limit or hot spots appear in the reaction zone, at least one part of the residual oil raw materials and the hydrogen gas is directly guided into the second hydrogenation reaction zone. Compared with the prior art, the method in the invention can prolong the running period of a residual oil hydrogenation device, thereby increasing the running efficiency of the device and improving the economical property of the device as well.

The invention relates to a grading composition of a hydrogenation catalyst. From top to bottom, a reactor is filled with hydrodemetallization and a hydrodesulfurization catalyst; raw materials flow from top to bottom, and along with the flowing direction of raw materials, the activity of the catalyst gradually increases, the pore size gradually decreases, the grain size gradually decreases and the porosity gradually decreases; the hydrodemetallization catalyst and the hydrodesulfurization catalyst are both formed by one or more demetallization catalysts; concentrations of active metal components and acid auxiliary agents are in nonuniform distribution, and from the surface to the center of catalyst grains, the concentrations of the active metal components and acid auxiliary agents of the hydrodemetallization catalyst are of gradient increase, and the concentrations of the active metal components and acid auxiliary agents of the hydrodesulfurization catalyst are of gradient decrease; and based on weight content, the demetallization catalyst accounts for 15 to 80 percent, and the desulfurization catalyst accounts for 20 to 85 percent. The grading composition of the invention is applied to hydrogenation catalysis of oil and residual oil of heavy ends and has the advantages of possessing better activity and stability of demetallization, residual carbon removal and desulfurization, controlling temperature rise of a catalyst bed and degreasing the deactivation speed of the catalyst.

The invention relates to an activated carbon/aluminum oxide composite type catalyst carrier and a preparation method and application of the activated carbon/aluminium oxide composite type catalyst carrier. The preparation method comprises the steps of washing circularly with 20-35% hydrochloric acid in a boiling state, wherein the mass ratio of hydrochloric acid to activated carbon is (5-20):1, performing oxidation with 10-50% nitric acid, wherein the mass ratio of an oxidizing agent to activated carbon is (20-40):1, kneading the activated carbon, aluminium oxide and an assistant into cakes in a kneading machine, extruding the kneaded cakes through an extruding machine, drying the extruded carrier, and roasting in nitrogen protection atmosphere to prepare the activated carbon/aluminum oxide composite type catalyst carrier. The activated carbon/aluminum oxide composite type catalyst carrier is suitably used as a residual oil hydrogenation catalyst carrier of a fixed bed, and is particularly used as the residual oil hydrodemetallization catalyst carrier. The activated carbon/aluminum oxide composite type catalyst carrier has high desulfurization rate up to 86.4-88.3%, high denitrification rate up to 58.3-60.5% and high demetalization rate up to 87.2-90.4%.

The present invention is macroporous alumina carrier and its preparation process. The carrier has pore volume of 0.9-1.3 ml/g, pore volume rate of pores smaller than 20 nm in 55-85 %, pore volume rate of 20-100 nm diameter pores in 7-25 %, and pore volume rate of pores greater than 100 nm in 7-25 %. The preparation process of the carrier includes forming and roasting pseudo-thin diasphore composition containing organic pore expanding agent. The preparation process of the present invention has relatively low organic pore expanding agent consumption and high pore expanding effect. The prepared macroporous alumina carrier is used in catalyst for hydrogenating and demetallating heavy and residual oil, especially decompression residual oil with high metal content.

The invention relates to a physical method for preparing vegetable oil. The method comprises the following process steps of: cleaning, remote infrared vacuum pre-tempering, microwave puffing, tempering, pressing, puffing, high-pressure fluid extraction, fixed bed adsorption refining, continuous vacuum dehydration and finally micro-filtering. The remote infrared vacuum pre-tempering and microwave puffing pre-processing method is fast and high-efficient and is suitable for industrial production. Press cake puffing and high-pressure fluid extraction are combined so that the problem of oil extraction of cold-pressing cakes is effectively solved, and meanwhile residual oil of the cold-pressing cakes is effectively reduced. The fixed bed adsorption refining method is simply and conveniently operated and has the advantages of short cycle, low energy consumption, low oil refining loss, high grease quality and the like. The whole process has the advantages of simplicity and convenience in operation, no solvent residue, low energy consumption, small neutral oil loss, high product quality and the like, an environment-friendly effect is achieved, and the method can be widely suitable for different kinds of oil.