72results about How to "Alleviate coking" patented technology

The bearings of a gas turbine are supplied with a lubricant from a reservoir by a main pump, when the turbine is operating. When the turbine is shut down and rotation ceases, the main pump also shuts down. When this occurs, an auxiliary pump is placed into operation to continue to supply the bearings with the lubricant until such time as the bearings have sufficiently cooled, at which point the auxiliary pump is shut down.

A turbocharger including means for preventing or reducing coking, particularly following engine shutdown, without noticeably increasing weight or volume of the turbocharger. The turbocharger bearing housing (14) has defined therein a lubrication flow path for bearing lubricant and a lubricant drain gallery (40) below a shaft (20), and in accordance with the invention at least a portion of a wall (42) of the lubricant drain gallery (40) is coated with an oil repellant and/or heat insulating coating (44).

Gas oil components, coking process recycle, and heavier hydrocarbons are cracked or coked in the coking vessel by injecting an additive into the vapors of traditional coking processes in the coking vessel. The additive contains catalyst(s), seeding agent(s), excess reactant(s), quenching agent(s), carrier(s), or any combination thereof to modify reaction kinetics to preferentially crack or coke these components. The quenching effect of the additive can be effectively used to condense the highest boiling point compounds onto the catalyst(s), thereby focusing the catalyst exposure to these target reactants. With a catalyst to crack these highest boiling point materials, this mechanism can effectively increase the catalyst's selectivity, thereby increasing its efficiency and reducing catalyst requirements and costs. Selective, catalytic conversion of the highest boiling point materials in the coking process product vapors (coker recycle and/or ‘heavy tail’ of the heavy coker gas oil) may be accomplished with an exemplary embodiment of the present invention in varying degrees. Exemplary embodiments of the present invention can also provide methods to control the (1) coke crystalline structure and (2) the quantity and quality of volatile combustible materials (VCMs) in the resulting coke. Pet coke from this process may have unique characteristics with substantial utility.

The benzene content in a gasoline pool is reduced by a process that hydrogenates a benzene-containing isomerization zone feedstream. The additional cyclic hydrocarbons produced by the saturation of benzene can be processed in the isomerization zone for ring opening to increase the available paraffinic feedstock or the isomerization zone can be operated to pass the cyclic hydrocarbons through to a product recovery section. The isomerization zone feedstream is treated to remove contaminants and dried before entering the hydrogenation zone.

The invention relates to coke inhibitor for ethylene cracking, which comprises the following component by weight percentage: 20% to 60% of sulfur-containing compound, 5% to 10% of passivator, 1% to 10% of film-forming agent, 5% to 15% of polymerization inhibitor, 1% to 10% of decoking agent and 25% to 45% of solvent, wherein the sulfur-containing compound is particularly dialkyl disulfide, dialkyl sulfide, di-alkylphenol sulfide, diphenyl sulfide, diphenyl disulfide, thiophene or thioxene; and the passivator is particularly triphenyl phosphate, triethyl phosphate, di-octyl-phenyl-phosphate, tributyl phosphate, thiophosphate trilaurate, diethyl-phosphorodi-thioate or triacyl piperidine phosphate, and the passivator is preferably triphenyl phosphate or di-octyl-phenyl-phosphate. The coke inhibitor of the invention for ethylene cracking is capable of effectively relieving the coking condition of an ethylene cracking tube, ensuring the good coke-inhibiting effect, obviously increasing the operation cycle of cracking and reducing the air-decoking time. Therefore, the coke inhibitor of the invention has wide applicable range in the coke inhibition of gaseous light dydrocarbon and naphtha.

A thermal management and power generation system for a hypersonic vehicle. The thermal management and power generation system comprising a fluid supply having a volatile fluid and a fuel supply having an endothermic fuel. A first heat exchanger, fluidically coupled to the fluid supply, absorbs heat from a first portion of the hypersonic vehicle, which vaporizes the volatile fluid. A mixing apparatus, fluidically coupled to the first heat exchanger and the fuel supply combines the vaporized volatile fuel and endothermic fuel. A second heat exchanger, fluidically coupled to the mixing apparatus, absorbs heat from a second portion of the hypersonic vehicle and decomposes the endothermic fuel by endothermic pyrolysis. A heat engine, fluidically coupled to the first heat exchanger and the mixing apparatus, is configured to generate an electrical power for use by the hypersonic vehicle. The vaporized volatile fluid mixed with the endothermic fuel within the second heat exchanger reduces coking caused by the endothermic pyrolytic decomposition of the endothermic fuel as compared to an endothermic pyrolytic decomposition of an endothermic fuel not having a vaporized volatile fluid mixed therewith.

The invention provides a direct coal liquefaction cycle solvent, a preparation method of the direct coal liquefaction cycle solvent and application of the direct coal liquefaction cycle solvent. The preparation method comprises the steps of S1, carrying out hydrogenation on a mixture of petroleum refining secondary products and direct coal liquefaction oil, and obtaining a hydrogenation product, S2, fractionating the hydrogenation product, and obtaining light distillate oil, medium distillate oil and heavy distillate oil, and S3, mixing the heavy distillate oil with a part of the medium distillate oil, and obtaining the direct coal liquefaction cycle solvent. In the preparation method of the direct coal liquefaction cycle solvent, on one hand, a large amount of arene is contained in the petroleum refining secondary products, the hydrogenation product is rich in components such as tetrahydronaphthalene, therefore, the hydrogen supplying capacity of the direct coal liquefaction cycle solvent can be obviously improved, and the yield of the direct coal liquefaction oil is improved; on the other hand, a part of high-added-value diesel distillate with the boiling range lower than 350 DEG C in the direct coal liquefaction cycle solvent is substituted with the petroleum refining secondary products, the diesel yield is improved, the economical efficiency of the coil liquefaction technology is remarkably improved, and the problem that an existing cycle solvent gets light can be solved.

The present invention relates to a process for converting oxygenates to olefins, comprising

• • (1) providing a gas stream comprising one or more ethers;
  • (2) contacting the gas stream provided in (1) with a catalyst,

the catalyst comprising

• • a support substrate and
  • a layer applied to the substrate,

the layer comprising one or more zeolites of the MFI, MEL and/or MWW structure type.

The invention discloses a system and method of blending combustion of a coal type with a low ash melting point in a coal-fired utility boiler and belongs to the technical field of coal-fired utility boiler operation. The coal-fired utility boiler is equipped with a positive-pressure, direct-firing, double-in and double-out steel ball coal pulverizer; the method of blending combustion of coal type with the low ash melting point in the coal-fired utility boiler comprises the following steps: the coal type with the low ash melting point and a coal type with a high ash melting point are sent into the steel ball coal pulverizer from one end of the positive-pressure, direct-firing, double-in and double-out steel ball coal pulverizer respectively; after thorough mixing and grinding, powder is uniformly output from two ends of the steel ball coal pulverizer; after the blending, compared with the melting point of the coal type with a low ash melting point, the melting point of the blended ash is increased to a relatively large extent; under various boiler loading, through adjusting the belt rotational speeds of coal feeders that correspond to the coal type with the low ash melting point and the coal type with the high ash melting point, the mixing proportion control is realized on the coal type with the low ash melting point. The system and method of blending combustion of coal type with the low ash melting point in the coal-fired utility boiler can improve the combustion and utilization proportion of the coal type with the low ash melting point to the utmost extent, on the basis of effectively relieving the boiler from coking and ensuring the safe operation of the boiler; the cost of fuel is reduced; the economical efficiency in the operation of the coal-fired utility boiler machine set is improved.

Disclosed is a hydrocarbon gas reforming supported catalyst, and methods for its use, that includes a catalytic material capable of catalyzing the production of a gaseous mixture comprising hydrogen and carbon monoxide from a hydrocarbon gas, and a clay support material comprising a clay mineral, wherein the catalytic material is attached to the clay support material.

The invention discloses a condense-dilute type double-cyclone cylinder pulverized coal burner which comprises a pulverized coal entrance channel, a pulverized coal concentrator and two cyclone separation type burners communicated with the pulverized coal entrance channel. The burner is characterized in that the pulverized coal concentrator is arranged in the pulverized coal entrance channel; and a blade in the pulverized coal concentrator inclines towards the side away from a boiler side wall and a wing wall adjacent to the pulverized coal concentrator along the flowing direction of pulverized coal so as to divide a pulverized coal airflow into a condense part and a dilute part. The invention changes a traditional double-cyclone cylinder burner into a condense-dilute type and has more obvious effect on reducing the discharge of NOx. Aiming at the reformation of an original burner, the condense-dilute type double-cyclone cylinder pulverized coal burner is the equipment having smallest changes, lowest cost and easiest implementation, a more effective measure for solving side (wing) wall coking under a current coal condition and can create a good condition for the safe and stable operation of boilers.

The benzene content in a gasoline pool is reduced by a process that hydrogenates a benzene-containing isomerization zone feedstream. The additional cyclic hydrocarbons produced by the saturation of benzene can be processed in the isomerization zone for ring opening to increase the available paraffinic feedstock or the isomerization zone can be operated to pass the cyclic hydrocarbons through to a product recovery section. The isomerization zone feedstream is treated to remove contaminants and dried before entering the hydrogenation zone.