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RU2001124309A - The method of hydrodesulfurization of the gasoline fraction of catalytic cracking - Google Patents

The method of hydrodesulfurization of the gasoline fraction of catalytic cracking

Info

Publication number
RU2001124309A
RU2001124309A RU2001124309/04A RU2001124309A RU2001124309A RU 2001124309 A RU2001124309 A RU 2001124309A RU 2001124309/04 A RU2001124309/04 A RU 2001124309/04A RU 2001124309 A RU2001124309 A RU 2001124309A RU 2001124309 A RU2001124309 A RU 2001124309A
Authority
RU
Russia
Prior art keywords
hydrodesulfurization
gasoline fraction
catalytic cracking
gasoline
boiling
Prior art date
Application number
RU2001124309/04A
Other languages
Russian (ru)
Other versions
RU2206601C2 (en
Inventor
Николай Михайлович Дюрик
Сергей Анатольевич Котов
Евгений Николаевич Заяшников
Виктор Андреевич Зоткин
Александр Львович Князьков
Николай Макарович Лагутенко
Александр Анатольевич Никитин
Евгений Алексеевич Есипко
Дмитрий Владимирович Кириллов
Original Assignee
Открытое акционерное общество "Славнефть-Ярославнефтеоргсинтез"
Filing date
Publication date
Application filed by Открытое акционерное общество "Славнефть-Ярославнефтеоргсинтез" filed Critical Открытое акционерное общество "Славнефть-Ярославнефтеоргсинтез"
Priority to RU2001124309A priority Critical patent/RU2206601C2/en
Priority claimed from RU2001124309A external-priority patent/RU2206601C2/en
Application granted granted Critical
Publication of RU2206601C2 publication Critical patent/RU2206601C2/en
Publication of RU2001124309A publication Critical patent/RU2001124309A/en

Links

Claims (1)

Способ гидрообессеривания бензиновой фракции каталитического крекинга в присутствии окисно-сульфидного катализатора при повышенных температуре и давлении водородсодержащего газа, отличающийся тем, что бензиновую фракцию ректификацией разделяют на 3 фракции: легкокипящую н.к. - 60-70°С, среднекипящую от 60-70 до 150-160°С и тяжелую 150-160°С - к.к., тяжелую бензиновую фракцию подвергают гидрообессериванию с последующим смешением ее с негидроочищенными легкокипящей и среднекипящей бензиновыми фракциями.The method of hydrodesulfurization of the gasoline fraction of catalytic cracking in the presence of an oxide-sulfide catalyst at elevated temperature and pressure of a hydrogen-containing gas, characterized in that the gasoline fraction by distillation is divided into 3 fractions: low boiling N. - 60-70 ° С, medium boiling point from 60-70 to 150-160 ° С and heavy 150-160 ° С - к.к., The heavy gasoline fraction is subjected to hydrodesulfurization, followed by mixing it with non-purified light boiling and medium boiling gasoline fractions.
RU2001124309A 2001-08-30 2001-08-30 Hydrodesulfurization method for catalytic cracking gasoline fraction RU2206601C2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
RU2001124309A RU2206601C2 (en) 2001-08-30 2001-08-30 Hydrodesulfurization method for catalytic cracking gasoline fraction

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
RU2001124309A RU2206601C2 (en) 2001-08-30 2001-08-30 Hydrodesulfurization method for catalytic cracking gasoline fraction

Publications (2)

Publication Number Publication Date
RU2206601C2 RU2206601C2 (en) 2003-06-20
RU2001124309A true RU2001124309A (en) 2003-06-27

Family

ID=29210354

Family Applications (1)

Application Number Title Priority Date Filing Date
RU2001124309A RU2206601C2 (en) 2001-08-30 2001-08-30 Hydrodesulfurization method for catalytic cracking gasoline fraction

Country Status (1)

Country Link
RU (1) RU2206601C2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7238273B2 (en) * 2004-09-10 2007-07-03 Chevron U.S.A. Inc Process for upgrading heavy oil using a highly active slurry catalyst composition
US7431827B2 (en) * 2004-10-27 2008-10-07 Catalytic Distillation Technologies Process for the production of low sulfur, low olefin gasoline
RU2361902C1 (en) * 2008-02-11 2009-07-20 Открытое акционерное общество "ТАИФ-НК" (ОАО "ТАИФ-НК") Method of refining of light fractions of secondary origin
RU2372380C1 (en) * 2008-07-29 2009-11-10 ООО "Компания Катахим" Method of selective treatment of gasoline fractions of catalytic cracking (versions)
RU2699132C1 (en) * 2015-12-18 2019-09-03 Юоп Ллк Method and apparatus for extracting hydrogen from a hydrotreatment effluent gas of a stripping column

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU1746702A1 (en) * 1990-01-10 1994-04-15 Всесоюзный научно-исследовательский институт по переработке нефти Method of recovery of hydrocarbon fuel
US5318690A (en) * 1991-08-15 1994-06-07 Mobil Oil Corporation Gasoline upgrading process
RU2134287C1 (en) * 1997-05-28 1999-08-10 Открытое акционерное общество "Славнефть-Ярославнефтеоргсинтез" Catalytic cracking gasoline purification process
RU2126437C1 (en) * 1998-02-20 1999-02-20 Открытое акционерное общество "Сызранский нефтеперерабатывающий завод" Method of producing winter diesel fuel
RU2131909C1 (en) * 1998-07-01 1999-06-20 Открытое акционерное общество "Ново-Уфимский нефтеперерабатывающий завод" Method of producing environmentally safe high-octane gasoline

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