CU24738B1 - Método para producir gasolinas o concentrados de compuestos aromáticos - Google Patents

Método para producir gasolinas o concentrados de compuestos aromáticos

Info

Publication number
CU24738B1
CU24738B1 CU2022000077A CU20220077A CU24738B1 CU 24738 B1 CU24738 B1 CU 24738B1 CU 2022000077 A CU2022000077 A CU 2022000077A CU 20220077 A CU20220077 A CU 20220077A CU 24738 B1 CU24738 B1 CU 24738B1
Authority
CU
Cuba
Prior art keywords
stream
mass
supplied
reaction zone
olefin
Prior art date
Application number
CU2022000077A
Other languages
English (en)
Other versions
CU20220077A7 (es
Inventor
Aleksandr Anatolevich Bessonov
Vladimir Vladislavovich Imshenetskii
Dmitrii Valerevich Ivanov
Iosif Izrailevich 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 CU20220077A7 publication Critical patent/CU20220077A7/es
Publication of CU24738B1 publication Critical patent/CU24738B1/es

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
    • C10G3/00Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
    • 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
    • C10G3/00Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
    • C10G3/42Catalytic treatment
    • C10G3/44Catalytic treatment characterised by the catalyst used
    • C10G3/48Catalytic treatment characterised by the catalyst used further characterised by the catalyst support
    • C10G3/49Catalytic treatment characterised by the catalyst used further characterised by the catalyst support containing crystalline aluminosilicates, e.g. molecular sieves
    • 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
    • C10G3/00Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
    • C10G3/60Controlling or regulating the processes
    • 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)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

<p>La invención se refiere a un método para obtener gasolinas o concentrados de compuestos aromáticos, en el que se usan como materias primas tres corrientes, Ia primera de las cuales incluye una fracción de hidrocarburo, Ia segunda corriente incluye un oxigenado, Ia tercera corriente incluye una fracción que contiene olefina, se usan tres zonas de reacción rellenas con un catalizador zeolítico, además: Ia fracción que contiene olefina incluye de 10 a 50% en masa de olefinas C2-C4, y de 0.5 a 8 % en masa de hidrógeno, Ia primera corriente se suministra al menos a una zona de reacción, Ia segunda corriente se suministra a Ia primera zona de reacción, o a Ia tercera zona de reacción, y cuando Ia segunda corriente se suministra a la primera zona, la distribución de Ia tercera corriente entre las dos zonas de reacción es 35-65 % en masa / 65-35 % en masa, y cuando Ia segunda corriente se suministra a Ia tercera zona de reacción, Ia distribución de Ia tercera corriente entre las dos zonas de reacción es 25-45 % en masa / 75-55 % en masa. El método permite procesar corrientes de olefinas diluidas que contienen hidrógeno sin separación de hidrógeno, sin reciclaje de productos gaseosos y sin el uso de intercambiadores internos de calor, al tiempo que aumenta el rendimiento y el número de octano (NO) del producto.</p>
CU2022000077A 2020-06-29 2021-06-22 Método para producir gasolinas o concentrados de compuestos aromáticos CU24738B1 (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
RU2020121538A RU2747870C1 (ru) 2020-06-29 2020-06-29 Способ получения бензинов или концентратов ароматических соединений
PCT/RU2021/050176 WO2022005330A1 (ru) 2020-06-29 2021-06-22 Способ получения бензинов или концентратов ароматических соединений

Publications (2)

Publication Number Publication Date
CU20220077A7 CU20220077A7 (es) 2023-08-08
CU24738B1 true CU24738B1 (es) 2025-04-04

Family

ID=75920004

Family Applications (1)

Application Number Title Priority Date Filing Date
CU2022000077A CU24738B1 (es) 2020-06-29 2021-06-22 Método para producir gasolinas o concentrados de compuestos aromáticos

Country Status (3)

Country Link
CU (1) CU24738B1 (es)
RU (1) RU2747870C1 (es)
WO (1) WO2022005330A1 (es)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023229485A1 (ru) * 2022-05-23 2023-11-30 Публичное акционерное общество "Газпром нефть" Способ получения бензиновых фракций и ароматических углеводородов

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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 (ru) * 2016-09-27 2018-11-02 Михайло Барильчук Комплексная установка для переработки смеси углеводородов с1-с10 различного состава и кислородсодержащих соединений
CN206751740U (zh) * 2017-05-10 2017-12-15 山东大齐化工科技有限公司 甲醇、石脑油芳构化生产高辛烷值汽油的系统

Also Published As

Publication number Publication date
CU20220077A7 (es) 2023-08-08
RU2747870C1 (ru) 2021-05-17
WO2022005330A1 (ru) 2022-01-06

Similar Documents

Publication Publication Date Title
BR112018067640A2 (pt) método de produção de gasolina a partir de frações de hidrocarboneto bruto, e instalação de produção de gasolina
EP1858830A4 (en) LIQUID PHASE PROCESS FOR ALKYLATING AROMATIC COMPOUNDS
AR053423A1 (es) Proceso de elaboracion de 1,2-dicloretano
BRPI0513338A (pt) métodos de produção de etileno e propileno
CN101448767A (zh) 制备烯烃的方法
BRPI0508591A (pt) processo para produzir olefinas leves e aromáticas
WO2010021910A3 (en) Process for the conversion of lower alkanes to aromatic hydrocarbons and ethylene
EP3558908B1 (en) Process to produce olefins from a catalytically cracked hydrocarbons stream
CN102666800A (zh) 将烯烃转化为柴油和其它馏分油的方法和系统
RU2015105406A (ru) Способ получения олефинов посредством термического парового крекинга в крекинг-печах
CU24738B1 (es) Método para producir gasolinas o concentrados de compuestos aromáticos
US9834493B2 (en) Process for reducing the benzene content of gasoline by alkylating benzene using a lower olefin in the presence of a paraffinic diluent
BRPI0510496A (pt) componente de gasolina alifática, composição de combustìvel de gasolina, e, processo para preparar um componente de gasolina alifática
US9580525B2 (en) Olefin olegomerization process
CU20220073A7 (es) Método de obtención de gasolinas o concentrados de compuestos aromáticos
BR0301025A (pt) Processo e aparelhagem para preparação de olefinas
ES183411A1 (es) UN PROCEDIMIENTO PARA POLIMERIZAR HIDROCARBUROS OLEFiNICOS
AU2015387361A1 (en) Process for converting an olefin containing hydrocarbon feed into an oligomerization product or a hydrogenated oligomerization product
ES3056910T3 (en) Isomerization zone in alkylate complex
RU2007134102A (ru) Производство бензина полимеризацией олефина с алкилированием ароматики
CU20220074A7 (es) Método para aumentar el rendimiento de un producto de hidrocarburo líquido
US10065904B2 (en) Process for producing alkylated aromatic hydrocarbons from a mixed hydrocarbon feedstream
CU20220075A7 (es) Método para aumentar el rendimiento de un producto de hidrocarburo líquido
CU20220076A7 (es) Método para aumentar el rendimiento de un producto de hidrocarburo líquido
US10414700B2 (en) Process for producing cumene and/or sec-butylbenzene using a mixed olefins stream as alkylation agent