EA201650034A1 - CATALYST AND METHOD FOR CONVERSION OF C-C ALIPHATIC HYDROCARBONS, C-ALCOHOLS, THEIR ETHERS OR THEIR MIXES FRIEND WITH A FRIEND INTO A HIGH-OCTANE COMPONENT OF AUTOMOBILE GASOLINE OR IN A DEVELOPMENT OF THE CAR-MOTOR BENZINE OR IN THE WORLD, IN A HIGH-ORGANIZE COMPONENT OF AUTOMOBILE GASOLINE OR IN A HIGH-ORANGE HIGH-OCTANE COMPONENT OF AUTOMOBILE GASOLINE OR IN THEIR HIGH-OCTANE COMPONENT - Google Patents

CATALYST AND METHOD FOR CONVERSION OF C-C ALIPHATIC HYDROCARBONS, C-ALCOHOLS, THEIR ETHERS OR THEIR MIXES FRIEND WITH A FRIEND INTO A HIGH-OCTANE COMPONENT OF AUTOMOBILE GASOLINE OR IN A DEVELOPMENT OF THE CAR-MOTOR BENZINE OR IN THE WORLD, IN A HIGH-ORGANIZE COMPONENT OF AUTOMOBILE GASOLINE OR IN A HIGH-ORANGE HIGH-OCTANE COMPONENT OF AUTOMOBILE GASOLINE OR IN THEIR HIGH-OCTANE COMPONENT

Info

Publication number
EA201650034A1
EA201650034A1 EA201650034A EA201650034A EA201650034A1 EA 201650034 A1 EA201650034 A1 EA 201650034A1 EA 201650034 A EA201650034 A EA 201650034A EA 201650034 A EA201650034 A EA 201650034A EA 201650034 A1 EA201650034 A1 EA 201650034A1
Authority
EA
Eurasian Patent Office
Prior art keywords
gasoline fractions
component
catalyst
octane
olefin
Prior art date
Application number
EA201650034A
Other languages
Russian (ru)
Other versions
EA033290B1 (en
Inventor
Михайло Барильчук
Николай Николаевич Ростанин
Original Assignee
Михайло Барильчук
Николай Николаевич Ростанин
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Михайло Барильчук, Николай Николаевич Ростанин filed Critical Михайло Барильчук
Priority to EA201650034A priority Critical patent/EA033290B1/en
Publication of EA201650034A1 publication Critical patent/EA201650034A1/en
Publication of EA033290B1 publication Critical patent/EA033290B1/en

Links

Landscapes

  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Изобретение относится к области нефтепереработки, газопереработки и нефтехимии, а именно к составу цеолитсодержащего катализатора и способу превращения на нем алифатических углеводородов C-C, содержащихся в низкооктановых прямогонных нефтяных или газоконденсатных бензиновых фракциях, олефинсодержащих бензиновых фракциях вторичных процессов переработки нефти, широких фракциях легких углеводородов (ШФЛУ), попутных нефтяных или отходящих нефтезаводских парафин- или олефинсодержащих газах, спиртов C-C, их эфиров или их смесей друг с другом в высокооктановый компонент автомобильного бензина с октановым числом не менее 76 пунктов по моторному методу (м.м.) или в дизельную фракцию в стационарном или движущемся слое гранулированного или шарикового катализатора. Катализатор и способ с его использованием превращения алифатических углеводородов C-C,спиртов C-C, их эфиров или их смесей друг с другом в адиабатическом реакторе или изотермическом реакторе с тепловой трубой (трубами) или панелями при температуре 200-580°C, давлении 0,1-10,0 МПа, объемной скорости подачи сырья (по жидкости) 0,1-11,0 чв высокооктановый компонент автомобильного бензина или в дизельную фракцию, содержащий в своем составе цеолит группы пентасилов (ZSM-5 или ZSM-11) с мольным отношением SiO/AlO=20-80 и содержанием оксида натрия NaO не более 0,2 мас.%, содержащий оксид цинка и связующий компонент (гамма - AlO, и/или двуокись кремния, и/или синтетический алюмосиликат, и/или глина, и/или двуокись циркония и другие), отличающийся тем, что он дополнительно содержит оксид стронция, причем его содержание в составе катализатора составляет от 0,01 до 3,0 мас.%, содержание оксида цинка составляет от 0,1 до 6,0 мас.%, содержание цеолита составляет от 20,0 до 90,0 мас.%, содержание связующего - остальное до 100 мас.%. Катализатор также может содержать в своем составе оксид бора, и/или оксид железа(III), и/или оксид магния, и/или оксид кальция, и/или пентоксид фосфора, и/или фтор при общем содержании всех промотирующих элементов (оксидов) (B, Fe, Mg, Ca, P, F) не более 5,0 мас.%.The invention relates to the field of oil refining, gas processing and petrochemistry, in particular to the composition of a zeolite-containing catalyst and a method for converting on it aliphatic hydrocarbons CC contained in low-octane straight-run oil or gas condensate gasoline fractions, olefin-containing gasoline fractions of the secondary processing of petroleum, gasoline fractions, olefin-containing gasoline fractions, and petrochemical gasoline fractions, olefin-containing gasoline fractions, and petrochemical gasoline fractions, olefin-containing gasoline fractions, olefin-containing gasoline fractions, and petrochemical gasoline fractions; associated petroleum or waste refinery paraffin or olefin containing gases, alcohols CC, their esters or their mixtures with each other ohm into the high-octane component of motor gasoline with an octane rating of at least 76 points by the motor method (m. m) or into the diesel fraction in a stationary or moving bed of a granular or ball catalyst. Catalyst and method of using it to convert aliphatic hydrocarbons CC, alcohols CC, their esters or their mixtures with each other in an adiabatic reactor or an isothermal reactor with a heat pipe (s) or panels at a temperature of 200-580 ° C, pressure 0.1-10 , 0 MPa, the volumetric feed rate of the raw material (liquid) 0.1-11.0 chv high-octane component of motor gasoline or diesel fraction containing in its composition a zeolite of the pentasil group (ZSM-5 or ZSM-11) with a molar ratio of SiO / AlO = 20-80 and the content of sodium oxide NaO is not more than 0.2 wt.%, Soda Corrosive zinc oxide and a binder component (gamma - AlO, and / or silicon dioxide, and / or synthetic aluminosilicate, and / or clay, and / or zirconium dioxide, etc.), characterized in that it additionally contains strontium oxide, and its content in the composition of the catalyst is from 0.01 to 3.0 wt.%, the content of zinc oxide is from 0.1 to 6.0 wt.%, the content of zeolite is from 20.0 to 90.0 wt.%, the content of the binder is the rest is up to 100 wt.%. The catalyst may also contain boron oxide, and / or iron (III) oxide, and / or magnesium oxide, and / or calcium oxide, and / or phosphorus pentoxide, and / or fluorine with a total content of all promoting elements (oxides). (B, Fe, Mg, Ca, P, F) not more than 5.0 wt.%.

EA201650034A 2016-10-28 2016-10-28 Catalyst and method to convert c-caliphatic hydrocarbons, c-calcohols, their esters or mixtures into high-octane gasoline component or diesel fraction EA033290B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EA201650034A EA033290B1 (en) 2016-10-28 2016-10-28 Catalyst and method to convert c-caliphatic hydrocarbons, c-calcohols, their esters or mixtures into high-octane gasoline component or diesel fraction

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EA201650034A EA033290B1 (en) 2016-10-28 2016-10-28 Catalyst and method to convert c-caliphatic hydrocarbons, c-calcohols, their esters or mixtures into high-octane gasoline component or diesel fraction

Publications (2)

Publication Number Publication Date
EA201650034A1 true EA201650034A1 (en) 2018-04-30
EA033290B1 EA033290B1 (en) 2019-09-30

Family

ID=62045895

Family Applications (1)

Application Number Title Priority Date Filing Date
EA201650034A EA033290B1 (en) 2016-10-28 2016-10-28 Catalyst and method to convert c-caliphatic hydrocarbons, c-calcohols, their esters or mixtures into high-octane gasoline component or diesel fraction

Country Status (1)

Country Link
EA (1) EA033290B1 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2768115C1 (en) * 2021-04-13 2022-03-23 Общество С Ограниченной Ответственностью "Новые Газовые Технологии-Синтез" (Ооо "Нгт-Синтез") Catalyst and method for production thereof
RU2768118C1 (en) * 2021-04-13 2022-03-23 Общество С Ограниченной Ответственностью "Новые Газовые Технологии-Синтез" (Ооо "Нгт-Синтез") Method of producing catalyst
RU2766555C1 (en) * 2021-05-21 2022-03-15 Акционерное общество "Специальное конструкторско-технологическое бюро "Катализатор" Catalyst for selective oxidation of hydrogen sulfide and method of its use

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2100075C1 (en) * 1996-02-16 1997-12-27 Николай Николаевич Ростанин Zeolite-containing catalyst and method of converting $$$-hydrocarbons into high-antiknock gasoline component or aromatic hydrocarbon concentrate
EA002139B1 (en) * 2000-03-09 2001-12-24 Генрих Семенович Фалькевич Catalst and method for converting alyphatic hydrocarbons c2-c12 into high-octane gasoline or aromatic hydrocarbon concentrate
RU2183656C1 (en) * 2000-12-25 2002-06-20 Мельников Вячеслав Борисович Method for production of motor fuels and catalyst for implementation thereof
RU2236289C1 (en) * 2002-12-30 2004-09-20 Общество с ограниченной ответственностью "Томскнефтехим" Aliphatic c2-c12-hydrocarbon conversion catalyst, method of preparation thereof and a method for converting aliphatic c2-c12-hydrocarbons into high-octane gasoline and/or aromatic hydrocarbons

Also Published As

Publication number Publication date
EA033290B1 (en) 2019-09-30

Similar Documents

Publication Publication Date Title
Occelli Catalytic cracking with an interlayered clay. A two-dimensional molecular sieve
CA2662082C (en) A process for the catalytic conversion of hydrocarbons
WO2007064019A1 (en) Liquefied fuel gas composition
EA201650034A1 (en) CATALYST AND METHOD FOR CONVERSION OF C-C ALIPHATIC HYDROCARBONS, C-ALCOHOLS, THEIR ETHERS OR THEIR MIXES FRIEND WITH A FRIEND INTO A HIGH-OCTANE COMPONENT OF AUTOMOBILE GASOLINE OR IN A DEVELOPMENT OF THE CAR-MOTOR BENZINE OR IN THE WORLD, IN A HIGH-ORGANIZE COMPONENT OF AUTOMOBILE GASOLINE OR IN A HIGH-ORANGE HIGH-OCTANE COMPONENT OF AUTOMOBILE GASOLINE OR IN THEIR HIGH-OCTANE COMPONENT
JP5142588B2 (en) Method for producing gasoline composition
CN102746877B (en) Method for preparing gasoline from methanol
CN101755036A (en) Be used to have the high diesel yield of low aromatic content and/or the catalytic cracking process of high propylene yield
TWI627269B (en) Hydrocarbon oil catalytic cracking catalyst and hydrocarbon oil catalytic cracking method
Doronin et al. Advanced developments: Cracking catalysts and additives to them
Safaev et al. EFFECT OF CHEMICAL COMPOSITION OF FUEL IS USED IN THE INTERNAL COMBUSTION ENGINE ON CHEMICAL COMPOSITION
Sousa-Aguiar Y Zeolites as a major component of FCC catalysts: Main challenges in the modification thereof
JP5137335B2 (en) Method for producing gasoline composition
Khande et al. Recent developments in FCC process and catalysts
KR20090025241A (en) Hydrotreating process, low environmental load gasoline base material and lead-free gasoline compositions
JP2012061409A (en) Method for manufacturing catalytic cracking catalyst
CN101362964A (en) Catalytic conversion method for reducing benzene content in gasoline
JP6327709B2 (en) Hydrocarbon oil catalytic cracking catalyst and hydrocarbon oil catalytic cracking method
RU2554884C1 (en) Method of preparing catalyst for cracking vacuum gas oil with controlled output of c3 and c4 olefins
JP2019512574A (en) Method and catalyst for producing high-octane component
Naman et al. Evaluation and improvement of diesel cut from tawke crude oil wells, Zakho
JP4847116B2 (en) A method for producing a liquefied fuel gas composition.
Potapenko et al. Features of catalysts for the hydrogenless refining of low-grade gasoline fractions
Esgair The Catalytic Activity of Modified Zeolite Lanthanum on the Catalytic Cracking of Al-Duara Atmospheric Distillation Residue.
Terentyev et al. Investigation of catalytic properties of new industrial KN-4 catalyst made from doped aluminosilicate of ZSM-5 zeolite structure
JP2012061410A (en) Method for manufacturing catalytic cracking catalyst

Legal Events

Date Code Title Description
MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

Designated state(s): AM BY KG TJ TM