333results about "Hydrocarbon by isomerisation" patented technology

The invention relates to a method for synthesizing mesitylene by gas-phase non-hydroisomerization of unsym-trimethylbenzene, which comprises the following step of: contacting the unsym-trimethylbenzene with a catalyst under a gas-phase non-hydroisomerization reaction condition in the presence of the catalyst, wherein the catalyst is an EWT structure molecular sieve, the total pore volume of the EWT structure molecular sieve is 0.20-0.51 cm < 3 >. G <-1 >, and the mesoporous volume is 0.11-0.37 cm < 3 >. G <-1 >. According to the method disclosed by the invention, the EWT structure molecular sieve with an ultra-large pore channel structure is adopted as the catalyst, and when the catalyst is used for synthesizing mesitylene through unsym-trimethylbenzene gas-phase non-hydroisomerization, the distribution conditions of raw materials and products are improved, the conversion rate of unsym-trimethylbenzene and the selectivity and the mass yield of mesitylene are improved, heavy component carbon deposition is slowed down, and the yield of mesitylene is improved. The service life of the catalyst is prolonged.

The invention discloses a catalytic method for converting alpha-olefin in an alkane-olefin mixture into internal olefin and application, raw materials and a solid acid catalyst are carried out in a fixed bed or a reaction kettle, the reaction temperature is 50-150 DEG C, the reaction pressure is 15-400 psi, and the reaction environment is an inert gas atmosphere; when the reaction is carried out on the fixed bed, the mass space velocity of the solid acid catalyst is 1h <-1 >-20h <-1 >; when the reaction is carried out in the reaction kettle, the conversion frequency of the raw materials is 5000 mol substrate mol acid site density <-1 > h <-1 > to 50000 mol substrate mol acid site density <-1 > h <-1 >; wherein the raw material is an alkane-alkene mixture; the solid acid catalyst comprises an active component and a carrier, wherein the carrier contains at least one inorganic oxide; the active component has a structure as shown in a formula (1) and / or a formula (2), in the formula (1) and the formula (2), R is alkyl or phenyl, and n is greater than or equal to 1. According to the catalysis method provided by the invention, the conversion rate of alpha-olefin can be increased, and the proportion of skeleton isomerization products and oligomers in internal olefin products can be reduced.

The invention provides a nickel metal hydroisomerization catalyst as well as a preparation method and application thereof. The catalyst comprises nickel, an alumina carrier and a molecular sieve, the nickel is loaded on the alumina carrier, and the content of the nickel in the catalyst is 1-10wt%; the molecular sieve is an SAPO molecular sieve. According to the invention, alumina is used as a carrier, non-noble metal nickel is loaded through a wet immersion method and is mixed with the molecular sieve to prepare the alkane isomerization catalyst, so that active metal with smaller particle size and higher dispersity can be provided, metal agglomeration at high temperature is avoided, and the utilization rate of metal is increased; the catalyst with excellent catalytic activity can be obtained only by loading low-content nickel metal, the catalyst has higher catalytic activity and selectivity, the obtained product contains more isomers, and the low-temperature fluidity of the product can be remarkably improved.

According to the method, a heteroatom EWT structure molecular sieve with a framework containing aluminum atoms and heteroatoms is adopted as a catalyst, the molecular sieve has the advantage of improving the utilization rate of an acid center, and when the molecular sieve is used for a gas-phase non-hydroisomerization reaction of the unsym-trimethylbenzene, the utilization rate of the acid center is increased; according to the present invention, the activity, the selectivity and the stability are high, the catalytic performance is significantly improved, the mesitylene selectivity and the mesitylene yield are higher than the heteroatom-free [Si, Al]-EWT structure molecular sieve, and the by-products such as tetratoluene and xylene are significantly reduced.

The invention discloses a preparation method of a bifunctional catalyst, the bifunctional catalyst and application, the preparation method comprises the following steps: (1) soaking an acidic functional component with an organic matter solution to obtain an acidic functional component precursor; (2) carrying out pre-reduction treatment on the dehydrogenation hydrogenation functional component to obtain a pretreated dehydrogenation hydrogenation functional component; and (3) kneading, molding, drying and roasting a mixture containing the acidic functional component precursor, the pretreated dehydrogenation and hydrogenation functional component, an auxiliary agent and a binder to obtain the bifunctional catalyst. The bifunctional catalyst disclosed by the invention has the characteristics of high conversion rate, good selectivity and excellent regeneration performance.

The application provides a C8 aromatic hydrocarbon isomerization catalyst and a preparation method and application thereof. The catalyst contains an active component and a carrier; wherein, based on the weight of the carrier, the carrier contains 5wt%-25wt% of HZSM-23, 5-30wt% of mordenite, 20-60wt% of macroporous alumina and 10wt%-25wt% of a binder component. The method comprises preparation of the carrier and loading of the active metal, wherein the preparation process of the carrier is as follows: HZSM-23 molecular sieve, mordenite, macroporous alumina and a binder are mixed and formed, and the carrier is prepared after drying and calcination. The catalyst is used for C8 aromatic hydrocarbon isomerization reaction, and has the characteristics of high ethylbenzene conversion rate and high xylene yield when the xylene is at an equilibrium concentration.

The invention relates to a method and device for preparing low-carbon olefins, and the method comprises the following steps: S1, contacting raw oil with a catalytic conversion catalyst in a catalytic conversion reactor for catalytic conversion reaction to obtain a catalytic conversion reaction product; s2, separating the catalytic conversion reaction product to obtain ethylene and propylene as well as a first circulating olefin flow containing butene and / or a second circulating olefin flow containing C5 + olefin; s3, enabling the olefin material to enter an etherification unit, and contacting the olefin material with an alcohol raw material under an etherification condition to obtain a circulating ether material and etherified olefin; and S4, enabling at least one part of etherified olefin to enter an isomerization unit, and carrying out isomerization reaction in the presence of an isomerization catalyst to obtain isomerized olefin. According to the method disclosed by the invention, the conversion of ethers into low-carbon olefins can be realized, the yield and selectivity of ethylene and propylene are improved, the yield of methane is reduced, the content of methanol in the product is reduced to the greatest extent, and the conversion of low-cost methanol into low-carbon olefins is realized.

The invention provides a modified molecular sieve and a preparation method and application thereof, the modified molecular sieve is a Na-type molecular sieve containing Mg element, and preferably, the modified molecular sieve also contains a template agent. When the molecular sieve is used for preparing trans-m-pentadiene, the reaction temperature is low, the product yield is high, the operation is simple, and the recovery is convenient; according to the preparation method provided by the invention, an Mg source is added in the process of synthesizing the molecular sieve, and the modified molecular sieve product can be prepared without roasting after crystallization.

This application discloses a method for preparing n-butene from isobutene, comprising the following steps: contacting a raw material containing isobutene with a catalyst and reacting to obtain a product containing n-butene; the catalyst is composed of MgAl2O4 and a hierarchical porous molecular sieve; and obtaining the catalyst through the following steps: 1) subjecting the molecular sieve to alkali treatment and acid treatment in sequence to obtain the porous molecular sieve; 2) wet mixing of magnesium source and aluminum source and calcining to obtain the MgAl2O4; 3) mixing the porous molecular sieve with the MgAl2O4 and calcining to obtain the catalyst.

The application discloses a method for selectively hydrogen-dealkylating aromatics and coupling xylene isomerization. + The method comprises the following steps: contacting aromatics, PX-lean C8 aromatics and a catalyst to perform selective hydrogen-dealkylation and xylene isomerization; wherein the catalyst comprises catalyst A, catalyst B and catalyst C, catalyst A is arranged upstream of catalyst B, and catalyst C is arranged downstream of catalyst B; wherein the catalyst A is a composite modified alumina; the catalyst B and the catalyst C are independently selected from group VIII metal modified molecular sieves. + The method provided by the application can concentrate a reaction unit to selectively hydrogen-dealkylate C8 10 C2 + The method can realize xylene isomerization in the PX-lean C8 aromatics while selectively hydrogen-dealkylating the side chains, and can cooperate with liquid phase transalkylation technology, so that an isomerization unit in an existing process is omitted, and device energy consumption, material consumption and investment are greatly reduced.

A process for producing branched aldehyde intermediates from alpha olefins, and further reacting said branched aldehyde intermediates via hydrogenation reactions, surfactant forming reactions and other chemical derivative forming reactions to produce branched alcohols, branched surfactants and other branched derivatives. A process for producing isomerized olefins, branched aldehydes, branched alcohols, branched surfactants and other branched derivatives through isomerization, hydroformylation, hydrogenation, surfactant forming reactions and other derivative forming reactions.

A process for producing ethylene and at least one of butanol and an alkyl tert-butyl ether from field butane includes separating the field butane into an n-butane stream and an isobutane stream; cracking the n-butane stream to obtain a cracked product stream comprising n-butane, 1- butene, 2-butene, butadienes, or a combination comprising at least one of the foregoing; and at least one of the following: (1) separating the cracked product stream to obtain a butane stream and a butene stream, and reacting the butene stream with water to obtain a fuel additive comprising butanol, and (2) dehydrogenating the isobutane stream in a dehydrogenation unit to form an isobutene stream and reacting the isobutene stream with an aliphatic alcohol to produce an alkyl tert-butyl ether.

A hydrocarbon isomerization system for an iC4 feed stream that provides for removal of C3s from an isomerization reactor feed stream by the addition of a depropanizer column to remove C3s from the reactor effluent stream after it has passed through a stabilizer column. This configuration prevents a buildup of C3s in the system and provides significant savings by reducing the size of the chloride treaters that are used to remove chlorides from off gas, increasing chlorides recovered to the hydrocarbon feed stream for use in combination with the isomerization catalyst. Significant utility savings are provided as well as a reduction in the amount of perchloroethane (PERC) and adsorbent that are required.

Systems and methods for processing a C3 and C4 hydrocarbon mixture have been disclosed. The C3 and C4 hydrocarbon mixture is first processed in an isomerization unit to isomerize n-butane to form isobutane. The resulting effluent stream from the isomerization unit comprising primarily isobutane and C3 hydrocarbons, collectively, is flowed into a separation unit configured to separate the effluent stream to form a C3 stream comprising C1 to C3 hydrocarbons and a C4 stream comprising primarily isobutane. The isobutane in the C4 stream is further dehydrogenated to form isobutene, which is further flowed into an MTBE synthesis unit as a feedstock for producing MTBE.

This invention discloses a method for the efficient conversion of isoparaffins, comprising the following steps: contacting a raw material containing isoparaffins and hydrogen with a catalyst in a reactor, reacting to obtain a product containing small molecule alkanes; wherein the isoparaffins are selected from at least one of isobutane, isopentane, neopentane, isohexane, and 3-methylpentane; wherein the small molecule alkanes are selected from at least one of ethane, propane, and n-butane; the catalyst is obtained by the following steps: mixing a metal acidic functional component, a metal basic functional component, a matrix precursor, a phosphorus auxiliary component precursor, a molding aid, and water, kneading, molding, and vacuum drying to obtain the catalyst.

Disclosed are apparatuses and processes for preparation and conversion comprising / using: a fractionation chain (4-6) that produces a xylene fraction (24); a xylene separation unit (10) that treats the xylene fraction to produce a para-xylene extract (39) and a raffinate (40); an isomerization unit (11) treating the raffinate to produce an isomerization product (42) of xylenes fed to the fractionation chain; the synthesis gas production unit (14; 15) that treats the hydrocarbon feedstock (30) to produce a synthesis gas (34) containing CO and CO2; a methanol synthesis reaction section (50) that treats the synthesis gas (34) to produce methanol (51); a toluene alkylation reaction section (13) treating the toluene-containing fraction (23) with methanol (51) to produce an alkylation effluent (32) containing xylene and fed to the fractionation chain.

The application provides a method for preparing isobutylbenzene from benzene and butene, which comprises four reactions in sequence; the first reaction is to synthesize sec-butylbenzene from benzene and butene; the second reaction is to generate 2-phenyl-2-butene by dehydrogenation of sec-butylbenzene; the third reaction is to generate 2-methyl-1-phenylpropene by isomerization of 2-phenyl-2-butene; and the fourth reaction is to generate isobutylbenzene by hydrogenation of 2-methyl-1-phenylpropene; the butene comprises 1-butene and / or 2-butene. The method uses benzene and butene as raw materials, adopts a four-step continuous series fixed-bed reaction process to synthesize isobutylbenzene, is simple to operate, can realize continuous production, does not need to use the metal potassium-sodium catalyst used in the traditional isobutylbenzene synthesis process, has small safety risk, and is suitable for industrialized production of isobutylbenzene.

The invention discloses a HUSY molecular sieve pretreatment method, a HUSY catalyst, a hanging type tetrahydrodicyclopentadiene preparation process and hanging type tetrahydrodicyclopentadiene prepared by the hanging type tetrahydrodicyclopentadiene preparation process. The HUSY molecular sieve pretreatment method comprises the following steps: taking an acidified HUSY molecular sieve, putting into a heating reaction device, calcining, heating to 500 DEG C at a heating rate of 5 DEG C / min, maintaining the constant temperature of 500 DEG C, reacting for 5 hours, naturally cooling to 80 DEG C, and taking out. According to the method, the yield of exo-tetrahydrodicyclopentadiene is increased by improving the pretreatment conditions of the catalyst, the temperature required by the isomerization reaction and the dosage of the catalyst.

The present application relates to the technical field of catalyst preparation, and is a catalyst for producing mesitylene from C9 mixed aromatic hydrocarbons and a preparation method thereof.The former is a non-noble metal supported molecular sieve catalyst, the catalyst carrier comprises a molecular sieve and a binder, the molecular sieve accounts for 70% to 90% of the weight percentage of the catalyst carrier, the loading of each element accounts for 1wt% to 10wt% of the weight percentage of the catalyst carrier, and the total loading of elements accounts for 5wt% to 15wt% of the weight percentage of the catalyst carrier.The catalyst for producing mesitylene from C9 mixed aromatic hydrocarbons has good catalytic performance, is applied to the process of producing mesitylene from C9 mixed aromatic hydrocarbons as a catalyst for alkylation reaction and isomerization reaction, finally eliminates the interference of methyl ethyl benzene, maximizes the production of mesitylene, the content of methyl ethyl benzene is less than 0.5%, and the yield of mesitylene is greater than 25%.

The present invention relates to a process for preparing an acrylate, preferably an R-CH2-CH2-(CHR-CH2)x-acrylate, more preferably N-butyl acrylate, and in particular to an alcohol conversion process of ethanol employing a homogeneous catalyst and a base, wherein 1-butanol as a product of said alcohol conversion process is formed, and wherein said 1-butanol is converted into N-butyl acrylate by an esterification process.

The invention relates to a process for producing high-purity 1-butene and high-purity isobutene from two C4 hydrocarbon streams, in which the two streams are partially processed together. Furthermore, the present invention also relates to an apparatus for carrying out the process according to the invention.

Provided is a method for upgrading a bio-based material, the method including the steps of pre-treating bio-renewable oil(s) and / or fat(s) to provide a bio-based fresh feed material, hydrotreating the bio-based fresh feed material, followed by separation, to provide a bio-propane composition.

The application provides a preparation method of a C8 aromatic hydrocarbon isomerization catalyst, which comprises the following steps: 1) mixing and forming EUO zeolite and a binder precursor into a carrier, and preparing a hydrogen type carrier after roasting and ammonium exchange; 2) performing composite modification treatment, which comprises hydrothermal treatment, acid treatment, and co-impregnation treatment using one or more compounds containing group IIIA-VIA elements or lanthanide series elements and a compound containing group VIII metal; 3) drying, roasting and reducing the solid to prepare the C8 aromatic hydrocarbon isomerization catalyst; and the application also provides the C8 aromatic hydrocarbon isomerization catalyst prepared by the above method, which comprises a carrier containing 5-35 mass% of EUO zeolite and 65-95 mass% of a binder, 0.02-0.15 mass% of one or more than two of group IIIA-VIA elements or lanthanide series elements, and 0.1-0.5 mass% of group VIII metal, which are calculated based on the carrier. When the catalyst prepared by the method is used in the C8 aromatic hydrocarbon isomerization reaction, the isomerization activity and the ethylbenzene conversion rate are obviously improved, and the aromatic hydrocarbon loss rate is low.

A process for the purification of isobutene from a C4 stream with at least 1-butene, 2-butene, isobutane and isobutene includes isomerizing 1-butene from a stream of material which is concentrated in isobutane and isobutene obtained from the C4 stream into 2-butene, using a catalyst in an isomerization reactor; supplying a product stream from the isomerization reactor to a rectification column; and providing a stream of material which is concentrated in isobutene. A processing facility is utilized for the purification of isobutene from the C4 stream.

Described herein are methods for converting butene. In some embodiments, butene is converted to an ethylene-containing products. In additional embodiments, butene is converted to an propylene-containing products. In additional embodiments, butene is selectively converted to an ethylene-containing product and a propylene-containing product. These methods generally include metathesis and cracking reactions, as described.

A process for the manufacture of a chemical of interest comprises subjecting a feedstock comprising a renewably-sourced ethanol to dehydration to produce a renewably-sourced ethylene stream, which is subjected to an olefin-interconversion to obtain one or more renewably-sourced C3-4-olefins, selected from propylene, n-butenes and isobutene. Further, the renewably-sourced C3-4-olefin is subjected to a chemical conversion or sequence of chemical conversions to obtain the chemical of interest, the chemical conversion or sequence of chemical conversions producing one or more crude product streams and, optionally, one or more crude intermediate product streams. Subsequently, at least one of the crude product stream(s) and optional intermediate crude product stream(s) is subjected to purification producing one or more purified product streams, one or more waste streams and, optionally, one or more purified intermediate product streams. Then, at least one of the waste streams is incinerated to produce thermal energy. The process provides a reaction scheme that provides renewably-sourced ethylene-derived chemical of interest, while minimizing both fossil carbon dioxide emissions and consumption of renewably-sourced feedstock.

The invention relates to the technical field of diene hydrogenation preparation, in particular to a preparation method of exo-tetrahydrodicyclopentadiene, which comprises the following steps of: performing catalytic hydrogenation on a dicyclopentadiene solution by using a circulating continuous flow bubbling hydrogenation reactor at the normal pressure and the temperature of 70-90 DEG C at the volume space velocity of 5h <-1 > and the hydrogen-oil volume ratio of 750-850 to obtain exo-tetrahydrodicyclopentadiene, automatically separating the hydrogenation catalyst at the tail end of the reactor to obtain a hydrogenation product, stirring and mixing an isomerization catalyst and the hydrogenation product at 90-110 DEG C, and carrying out catalytic isomerization to prepare exo-tetrahydrodicyclopentadiene; and rectifying and separating to obtain hanging tetrahydrodicyclopentadiene. According to the invention, the circulating continuous flow bubbling hydrogenation reactor is adopted for liquid phase hydrogenation, continuous production of exo-tetrahydrodicyclopentadiene is realized by a two-step method, the problem that catalytic hydrogenation and isomerization reaction are not matched is avoided, the conversion rate of exo-tetrahydrodicyclopentadiene is increased, and coking and impurity pollution of non-target products are reduced.

A method for processing a hydrocarbon-containing mixture includes the steps of: I) separating the hydrocarbon-containing mixture into a light fraction and a heavy fraction; II) reacting the light fraction from step I) in an aromatization unit and separating the resulting reaction product into a C5− component and a C6+ component; III) reacting the heavy fraction from step I) and optionally the C6+ component from step II) in an aromatics conversion unit and separating the resulting reaction product into a C5− component, a C6-C7 component, a C8 component, and a C9+ component; and IV) optionally, steam cracking or catalytic cracking one or both of the C5− component from step II) and the C5− component from step III). The method can convert low-value hydrocarbon mixtures into C8 aromatic hydrocarbons and cracking raw materials, and improve the product value. A system for practicing this method is also provided.

The invention relates to the technical field of sizing agent preparation, in particular to a method for preparing an ASA sizing agent based on enhanced olefin isomerization. Comprising the following steps: step 1, deep pretreatment of alpha-olefin; 2, preparing a composite catalyst; step 3, field-enhanced isomerization reaction; step 4, precisely purifying internal olefin; 5, solvent-free ASA closed-loop synthesis is carried out; and 6, ASA targeted post-treatment: cooling the product in the step 5, adding amino modified graphene to adsorb residual maleic anhydride, filtering, carrying out gradient cooling crystallization on the filtrate according to a set rate, and filtering to obtain a high-purity ASA sizing agent crystal. Through deep pretreatment of the alpha-olefin, the content of heavy metal ions in the straight-chain alpha-olefin can be controlled to be less than or equal to 0.05 ppm, and the content of mercaptan impurities can be controlled to be less than or equal to 0.05 ppm; by combining the design of recycling unreacted alpha-olefin through supercritical CO2 extraction and circulating the unreacted alpha-olefin to the step 1, the consumption of the alpha-olefin raw material can be reduced, and the utilization rate of the raw material is high.

The invention discloses a heterogeneous metal-silicon-aluminum molecular sieve composite catalyst and a preparation method and application thereof, the preparation method comprises the following steps: S1, selecting a silicon-aluminum molecular sieve as a carrier, washing, drying and roasting to obtain a first molecular sieve catalyst; step S2, dropwise adding a metal precursor solution into the first molecular sieve catalyst, and introducing the metal precursor into orifices and the surface of the first molecular sieve catalyst to obtain a second molecular sieve catalyst; and S3, drying the second molecular sieve catalyst at a first temperature, and roasting at a second temperature to obtain the multi-phase metal-silicon-aluminum molecular sieve composite catalyst. According to the heterogeneous metal-silicon-aluminum molecular sieve composite catalyst provided by the invention, the metal components are introduced into the orifices and the surfaces of the silicon-aluminum molecular sieves, so that a synergistic effect is formed between the metal components and Bronsted acid sites on the silicon-aluminum molecular sieves, and the side reaction rate is remarkably reduced while efficient double-bond isomerization of alpha-olefin is ensured.