CU24737B1 - METHOD FOR OBTAINING GASOLINE - Google Patents

METHOD FOR OBTAINING GASOLINE

Info

Publication number
CU24737B1
CU24737B1 CU2022000076A CU20220076A CU24737B1 CU 24737 B1 CU24737 B1 CU 24737B1 CU 2022000076 A CU2022000076 A CU 2022000076A CU 20220076 A CU20220076 A CU 20220076A CU 24737 B1 CU24737 B1 CU 24737B1
Authority
CU
Cuba
Prior art keywords
stream
olefin
inlet temperature
relates
containing fraction
Prior art date
Application number
CU2022000076A
Other languages
Spanish (es)
Other versions
CU20220076A7 (en
Inventor
Aleksandr Anatolevich Bessonov
Vladimir Vladislavovich Imshenetskii
Dmitrii Valerevich Ivanov
Losif Lzrailevich LISHCHINER
Elena Nikolaevna Lobichenko
Olga Vasilevna Malova
Denis Vasilevich Pchelintsev
Andrei Leonidovich Tarasov
Original Assignee
Joint Stock Company Gazpromneft Omsk Refinery
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 Joint Stock Company Gazpromneft Omsk Refinery filed Critical Joint Stock Company Gazpromneft Omsk Refinery
Publication of CU20220076A7 publication Critical patent/CU20220076A7/en
Publication of CU24737B1 publication Critical patent/CU24737B1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G35/00Reforming naphtha
    • C10G35/04Catalytic reforming
    • C10G35/06Catalytic reforming characterised by the catalyst used
    • C10G35/095Catalytic reforming characterised by the catalyst used containing crystalline alumino-silicates, e.g. molecular sieves
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00Technologies relating to oil refining and petrochemical industry
    • Y02P30/20Technologies relating to oil refining and petrochemical industry using bio-feedstock

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

<p>Esta invención se refiere a áreas de la industria petroquímica y de refinación de petróleo. Más específicamente, la invención se refiere a un método para aumentar el rendimiento de un producto hidrocarbónico líquido dentro de un método para producir gasolina, en el que se utilizan tres corrientes como materias primas, la primera de las cuales incluye una fracción hidrocarbónica, la segunda incluye el oxigenado y la tercera corriente incluye una fracción que contiene olefinas, donde la fracción que contiene olefinas incluye olefinas <em>C2-C4 </em>en una cantidad total, de 10 a 50 en % del peso. Se utilizan tres zonas de reacción llenas con un catalizador de zeolita. La primera corriente abastece a al menos una zona de reacción, mientras que la segunda corriente y la tercera corriente se distribuyen en tres zonas de reacción, y la temperatura de entrada de cada zona de reacción consecutiva es mayor que la temperatura de entrada de la zona anterior.</p><p>This invention relates to areas of the petrochemical and petroleum refining industries. More specifically, the invention relates to a method for increasing the yield of a liquid hydrocarbon product within a method for producing gasoline, wherein three streams are used as feedstocks, the first of which includes a hydrocarbon fraction, the second includes the oxygenate, and the third stream includes an olefin-containing fraction, where the olefin-containing fraction includes C2-C4 olefins in a total amount of 10 to 50% by weight. Three reaction zones filled with a zeolite catalyst are used. The first stream supplies at least one reaction zone, while the second stream and the third stream are distributed among three reaction zones, and the inlet temperature of each consecutive reaction zone is higher than the inlet temperature of the previous zone.</p>

CU2022000076A 2020-06-29 2021-06-22 METHOD FOR OBTAINING GASOLINE CU24737B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
RU2020121564A RU2747864C1 (en) 2020-06-29 2020-06-29 Method for increasing yield of liquid hydrocarbon product
PCT/RU2021/050180 WO2022005334A1 (en) 2020-06-29 2021-06-22 Method for increasing the yield of a liquid hydrocarbon product

Publications (2)

Publication Number Publication Date
CU20220076A7 CU20220076A7 (en) 2023-09-07
CU24737B1 true CU24737B1 (en) 2025-03-10

Family

ID=75919971

Family Applications (1)

Application Number Title Priority Date Filing Date
CU2022000076A CU24737B1 (en) 2020-06-29 2021-06-22 METHOD FOR OBTAINING GASOLINE

Country Status (3)

Country Link
CU (1) CU24737B1 (en)
RU (1) RU2747864C1 (en)
WO (1) WO2022005334A1 (en)

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7371915B1 (en) * 2004-06-25 2008-05-13 Uop Llc Conversion of oxygenate to propylene using moving bed technology
AU2007331785B2 (en) * 2006-12-13 2012-04-05 Haldor Topsoe A/S Process for the synthesis of hydrocarbon constituents of gasoline
RU2375344C1 (en) * 2008-04-03 2009-12-10 Общество с ограниченной ответственностью Научно-Производственное Объединение "Синтез" Method of producing completely deuterated c5+ hydrocarbons
RU2443471C2 (en) * 2010-06-02 2012-02-27 Учреждение Российской Академии Наук Ордена Трудового Красного Знамени Институт Нефтехимического Синтеза Им. А.В. Топчиева Ран (Инхс Ран) Catalyst and method of producing aliphatic hydrocarbons from carbon oxide and hydrogen in its presence
WO2017155424A1 (en) * 2016-03-09 2017-09-14 Limited Liability Company "New Gas Technologies-Synthesis" (Llc "Ngt-Synthesis") Method and plant for producing high-octane gasolines
RU2671568C1 (en) * 2016-09-27 2018-11-02 Михайло Барильчук Complex installation for processing mixture of hydrocarbons c1-c10 of various composition and oxygen-containing compounds

Also Published As

Publication number Publication date
RU2747864C1 (en) 2021-05-17
CU20220076A7 (en) 2023-09-07
WO2022005334A1 (en) 2022-01-06

Similar Documents

Publication Publication Date Title
US7834229B2 (en) Olefin oligomerization process
CA2781892C (en) Process and system to convert methanol to light olefin, gasoline and distillate
CA2916767C (en) Olefins reduction of a hydrocarbon feed using olefins-aromatics alkylation
Wulfers et al. Assessment of mass transfer limitations in oligomerization of butene at high pressure on H-beta
US20110147263A1 (en) Process and system to convert olefins to diesel and other distillates
BR112018067640A2 (en) Gasoline production method from crude hydrocarbon fractions, and gasoline production facility
US11267770B2 (en) Process to produce olefins from a catalytically cracked hydrocarbons stream
BR102016016875A2 (en) hydrotreating process of renewable materials with improved gas recycling
ATE486115T1 (en) INTEGRATED CATALYTIC DECISION PROCESS AND STEAM PYROLYSIS PROCESS FOR PRODUCING OLEFINS
EP3167027B1 (en) Process for producing btx and lpg
EP1948578A1 (en) Oligomerization reaction
US20150157998A1 (en) Apparatus for the integration of dehydrogenation and oligomerization
JP2013532145A (en) Process for co-oligomerization of olefins
US20150159099A1 (en) Light olefin oligomerization process for the production of liquid fuels from paraffins
WO2016098909A1 (en) Production method for lower olefin, production device for lower olefin, construction method for lower olefin production equipment, and zeolite catalyst
US7786337B2 (en) Olefin oligomerization process
AU596615B2 (en) Process for the manufacture of high viscosity lubricating oils
US20060194999A1 (en) Gasoline production by olefin polymerization
CU24737B1 (en) METHOD FOR OBTAINING GASOLINE
US9394212B2 (en) Process for the cooligomerization of olefins
AU605877B2 (en) Production of high viscosity index lubricating oils from lower olefins and small amounts of water
JP2018508557A (en) Process for converting an olefin-containing hydrocarbon feed to an oligomerized product or a hydrogenated oligomerized product
He et al. Comparison of ginger oil conversion over MFI, BEA, and FAU
JP6480726B2 (en) Lower olefin production method, lower olefin production apparatus, and lower olefin production facility construction method
CU20220074A7 (en) METHOD TO INCREASE THE YIELD OF A LIQUID HYDROCARBON PRODUCT