35results about "Hydrocarbon by polyaryl split-off" patented technology

A catalyst and process is disclosed to selectively upgrade a paraffinic feedstock to obtain an isoparaffin-rich product for blending into gasoline. The catalyst comprises a support of a sulfated oxide or hydroxide of a Group IVB (IUPAC 4) metal, a first component comprising at least one Group III A (IUPAC 13) component, and at least one platinum-group metal component which is preferably platinum.

A catalyst and process is disclosed to selectively upgrade a paraffinic feedstock to obtain an isoparaffin-rich product for blending into gasoline. The catalyst comprises a support of a tungstated oxide or hydroxide of a Group IVB (IUPAC 4) metal, a first component of at least one lanthanide element, yttrium or mixtures thereof, which is preferably ytterbium or holmium, and at least one platinum-group metal component which is preferably platinum.

A process for converting polycyclic aromatic compounds to monocyclic aromatic compounds includes pyrolyzing a coal feed to produce a coke stream and a coal tar stream. The coal tar stream is cracked, and the cracked coal tar stream is fractionated to produce an aromatic fraction comprising the polycyclic aromatic compounds. The process further includes hydrocracking the aromatic fraction to partially hydrogenate at least a first portion of the aromatic fraction, and to open at least one ring of a second portion of the aromatic fraction to form the monocyclic aromatic compounds from the polycyclic compounds, and recycling the first portion of the aromatic fraction.

The invention relates to a method for directionally preparing benzene by utilizing xylogen. The method comprises the following steps of: selecting a cylindrical fixed bed catalytic reactor with a conductive metal wire arranged in a cavity; depolymerizing to converte xylogen to an aromatic monomer, wherein a led raw material is the xylogen, a catalyst is powder zeolite catalyst or modified zeolite catalyst containing transition metal nickel element, the usage amount is characterized in that the weight ratio of the catalyst to the xylogen is 0.3-10 per hour, and a product is a liquid-state aromatic monomer mixer; and directionally converting the aromatic monomer mixer into benzene, wherein a led raw material is the aromatic monomer mixer which is preheat to be 200-250 DEG C, a catalyst is powder zeolite catalyst containing an Re element, the usage amount is characterized in that the weight ratio of the aromatic monomer mixer to the zeolite catalyst containing the Re element is 0.2-15 per hour, and a product is mixed liquid taking the benzene as the main part. According to the method, an external hydrogen source is not needed, the raw material resources are rich, and higher benzene yield and benzene selectivity can be obtained at intermediate temperature and constant pressure as well as under a green and mild reaction environment.

The present invention relates to a selective ring-opening catalyst and a preparation method thereof. A purpose of the present invention is to mainly solve the problems of poor polycyclic aromatic hydrocarbon ring-opening selectivity, low monocyclic aromatic hydrocarbon yield and rapid catalyst deactivation in the prior art. The technical scheme of the present invention comprises that the selective ring-opening catalyst comprises, by weight, 63.5-68.4% of at least one selected from alumina, amorphous silicon aluminum and a zeolite molecular sieve, 20-30% of pseudo boehmite, 0.1-1.5% of a noble metal Ir, and 0.1-5% of at least one selected from Ba, Zn and Mg. With the technical scheme, the problems in the prior art are well solved. The selective ring-opening catalyst of the present invention has characteristics of high polycyclic aromatic hydrocarbon ring-opening selectivity, high monocyclic aromatic hydrocarbon yield and slow catalyst deactivation, and can be used in the aromatic hydrocarbon refining field.

Disclosed herein is a process and catalyst for producing an ethylbenzene feed from a polyethylbenzene feed, comprising the step of contacting a benzene feed with a polyethylbenzene feed under at least partial liquid phase conditions in the presence of a zeolite beta catalyst having a phosphorus content in the range of 0.01 wt. % to 0.5 wt. % of said catalyst, to provide a product which comprises ethylbenzene.

The catalyst for producing aromatic hydrocarbon is for producing monocyclic aromatic hydrocarbon having 6 to 8 carbon number from oil feedstock having a 10 volume % distillation temperature of 140° C. or higher and a 90 volume % distillation temperature of 380° C. or lower and contains crystalline aluminosilicate and phosphorus. A molar ratio (P / Al ratio) between phosphorus contained in the crystalline aluminosilicate and aluminum of the crystalline aluminosilicate is from 0.1 to 1.0. The production method of monocyclic aromatic hydrocarbon is a method of bringing oil feedstock having a 10 volume % distillation temperature of 140° C. or higher and a 90 volume % distillation temperature of 380° C. or lower into contact with the catalyst for producing monocyclic aromatic hydrocarbon.

A catalyst for producing monocyclic aromatic hydrocarbons, used for producing monocyclic aromatic hydrocarbons of 6 to 8 carbon number from a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and an end point temperature of not more than 400° C., wherein the catalyst contains a crystalline aluminosilicate, gallium and / or zinc, and phosphorus, the molar ratio between silicon and aluminum (Si / Al ratio) in the crystalline aluminosilicate is not more than 100, the molar ratio between the phosphorus supported on the crystalline aluminosilicate and the aluminum of the crystalline aluminosilicate (P / Al ratio) is not less than 0.01 and not more than 1.0, and the amount of gallium and / or zinc is not more than 1.2% by mass based on the mass of the crystalline aluminosilicate.

The invention relates to a method for directionally preparing benzene by utilizing xylogen. The method comprises the following steps of: selecting a cylindrical fixed bed catalytic reactor with a conductive metal wire arranged in a cavity; depolymerizing to converte xylogen to an aromatic monomer, wherein a led raw material is the xylogen, a catalyst is powder zeolite catalyst or modified zeolite catalyst containing transition metal nickel element, the usage amount is characterized in that the weight ratio of the catalyst to the xylogen is 0.3-10 per hour, and a product is a liquid-state aromatic monomer mixer; and directionally converting the aromatic monomer mixer into benzene, wherein a led raw material is the aromatic monomer mixer which is preheat to be 200-250 DEG C, a catalyst is powder zeolite catalyst containing an Re element, the usage amount is characterized in that the weight ratio of the aromatic monomer mixer to the zeolite catalyst containing the Re element is 0.2-15 per hour, and a product is mixed liquid taking the benzene as the main part. According to the method, an external hydrogen source is not needed, the raw material resources are rich, and higher benzene yield and benzene selectivity can be obtained at intermediate temperature and constant pressure as well as under a green and mild reaction environment.

An aromatics / naphthalene rich stream obtained by processing heavy gas oil derived from tar sands and cycle oils derived from cracking heavy gas oil may optionally be blended and subjected to a hydrogenation process and a ring opening reaction typically in the presence of a zeolite, alumina, or silica alumina based catalyst which may contain noble metals and or copper or molybdenum to produce paraffinic feedstocks for further chemical processing.

Systems and methods for hydrodearylation of a hydrocarbon feed stream comprising non-condensed alkyl-bridged multi-aromatic hydrocarbons, the method including supplying a hydrogen feed to the hydrocarbon feed stream comprising non-condensed alkyl-bridged multi-aromatic hydrocarbons; mixing the hydrogen feed with the hydrocarbon feed stream to saturate the hydrocarbon feed stream with hydrogen gas to create a hydrogen-enriched liquid hydrocarbon stream; passing the hydrogen-enriched liquid hydrocarbon stream to a hydrodearylation reactor without a separate gaseous phase of hydrogen; allowing the hydrogen-enriched liquid hydrocarbon stream to react in presence of a catalyst under specific reaction conditions to produce a product stream comprising a reduced concentration of di-aromatic compounds and an increased concentration of mono-aromatic compounds compared to the hydrocarbon feed stream comprising non-condensed alkyl-bridged multi-aromatic hydrocarbons; and recovering, from the hydrodearylation reactor, a product stream for a downstream process, wherein the non-condensed alkyl-bridged multi-aromatic hydrocarbons include at least two benzene rings connected by an alkyl bridge group having at least two carbons, wherein the benzene rings are connected to different carbons of the alkyl bridge group.

The invention relates to a catalyst for converting sulfur-containing polycyclic aromatic hydrocarbons into monocyclic aromatic hydrocarbons and a preparation method thereof. The method mainly solves the problems of low conversion depth of sulfur-containing polycyclic aromatic hydrocarbons, low yield and low selectivity of single-ring aromatic hydrocarbons, and fast catalyst deactivation rate existing in the prior art. The present invention comprises the mixture of 30~65% FAU type zeolite and ZSM-12 molecular sieve by adopting catalyst by weight percentage, 33.5~69.8% is selected from at least one in γ-alumina, η-alumina or pseudo-boehmite One is the technical scheme of binder and 0.1-0.5% of at least one metal selected from Pt, Pd or Ir and 0.1-1% of at least one metal selected from La, Ce or Sn, which better solves the problem To solve the above problems, the catalyst can be used in the industrial production of converting sulfur-containing polycyclic aromatic hydrocarbons into single-ring aromatic hydrocarbons.

The invention relates to a reproducible catalyst for converting polycyclic aromatic hydrocarbons into monocyclic aromatic hydrocarbons and a preparation method thereof. The method mainly solves the problems of low conversion depth of polycyclic aromatic hydrocarbons, low yield and selectivity of single-ring aromatic hydrocarbons, and poor catalyst regeneration performance existing in the prior art. The present invention comprises a mixture of 30-65% MOR-type zeolite and ZSM-12 molecular sieve in terms of weight percentage by using a catalyst, and 34.5-69.9% is selected from at least one of γ-alumina, η-alumina or pseudo-boehmite A kind of technical scheme that is binding agent and 0.1~0.5% at least one kind of metal selected from Pt, Pd or Ir solves the above-mentioned problems well, and the regeneration performance of the catalyst is better, and the catalyst can be used for heavy polycyclic In the industrial production of aromatics converted into single-ring aromatics.

A process for the selective ring opening of ring-containing hydrocarbons in a feed stream having at least 10% ring-containing hydrocarbons includes contacting the feed stream with a ring opening catalyst containing a metal or a mixture of metals active for the selective ring opening of the ring-containing hydrocarbons on a support material, wherein the support material is a non-crystalline, porous inorganic oxide or mixture of inorganic oxides having at least 97 volume percent interconnected mesopores based on micropores and mesopores, and wherein the ring-containing hydrocarbons have at least one C6 ring and at least one substituent selected from the group consisting of fused 5- or 6-membered rings, alkyl, cycloalkyl and aryl groups.

A catalyst for producing monocyclic aromatic hydrocarbons of 6 to 8 carbon number from a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and an end point temperature of not more than 400° C., or a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and a 90 volume % distillation temperature of not more than 360° C., wherein the catalyst contains a crystalline aluminosilicate, gallium and / or zinc, and phosphorus, and the amount of phosphorus supported on the crystalline aluminosilicate is within a range from 0.1 to 1.9% by mass based on the mass of the crystalline aluminosilicate; and a method for producing monocyclic aromatic hydrocarbons, the method involving bringing a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and an end point temperature of not more than 400° C., or a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and a 90 volume % distillation temperature of not more than 360° C., into contact with the above-mentioned catalyst for producing monocyclic aromatic hydrocarbons.