RU2014142902A - METHOD FOR MANAGING THE TECHNOLOGICAL PROCESS AND NOMENCLATURE OF PRODUCED OIL PRODUCTS DURING OIL PROCESSING (OPTIONS) - Google Patents

METHOD FOR MANAGING THE TECHNOLOGICAL PROCESS AND NOMENCLATURE OF PRODUCED OIL PRODUCTS DURING OIL PROCESSING (OPTIONS) Download PDF

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Publication number
RU2014142902A
RU2014142902A RU2014142902A RU2014142902A RU2014142902A RU 2014142902 A RU2014142902 A RU 2014142902A RU 2014142902 A RU2014142902 A RU 2014142902A RU 2014142902 A RU2014142902 A RU 2014142902A RU 2014142902 A RU2014142902 A RU 2014142902A
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Russia
Prior art keywords
oil
instead
vacuum distillation
nomenclature
technological process
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RU2014142902A
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Russian (ru)
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RU2607089C2 (en
Inventor
Надежда Васильевна Копыл
Абдужамил Абдуллаевич Курбонов
Александр Кузьмич Жучков
Василий Васильевич Копыл
Любовь Николаевна Кошелева
Дилшод Тахирович Файзиев
Original Assignee
Надежда Васильевна Копыл
Абдужамил Абдуллаевич Курбонов
Александр Кузьмич Жучков
Василий Васильевич Копыл
Любовь Николаевна Кошелева
Дилшод Тахирович Файзиев
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Application filed by Надежда Васильевна Копыл, Абдужамил Абдуллаевич Курбонов, Александр Кузьмич Жучков, Василий Васильевич Копыл, Любовь Николаевна Кошелева, Дилшод Тахирович Файзиев filed Critical Надежда Васильевна Копыл
Publication of RU2014142902A publication Critical patent/RU2014142902A/en
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Publication of RU2607089C2 publication Critical patent/RU2607089C2/en

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G99/00—Subject matter not provided for in other groups of this subclass
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
    • C10G31/06—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by heating, cooling, or pressure treatment
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G33/00—Dewatering or demulsification of hydrocarbon oils

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

Abstract

Способ управления технологическим процессом и номенклатурой выпускаемых нефтепродуктов при переработке нефти, заключающийся в ее физическом разделении на фракции, отличающийся тем, что для увеличения выхода наиболее ценных светлых топливных фракций нефть подвергают криолизу при температуре не выше -15°С в течение не менее 20 ч с предварительным введением в нее донорной присадки (воды) в количестве не менее 1% на различных этапах ее переработки:- перед фракционированием вместо вакуумной перегонки на нефтепромыслах, где одновременно с повышением содержания топливных фракций в нефти происходит ее обезвоживание и обессоливание (частичное или полное), а также в различных сочетаниях этапов переработки, например перед фракционированием и вместо вакуумной перегонки, или на нефтепромыслах и вместо вакуумной перегонки и т.д.A method of controlling the technological process and the nomenclature of oil products produced during oil refining, which consists in its physical separation into fractions, characterized in that to increase the yield of the most valuable light fuel fractions, the oil is subjected to cryolysis at a temperature of no higher than -15 ° C for at least 20 hours by preliminary introducing into it a donor additive (water) in an amount of at least 1% at various stages of its processing: - before fractionation instead of vacuum distillation in oil fields, where at the same time Decreasing the content of fuel fractions in oil, it is dehydrated and desalted (partial or complete), as well as in various combinations of processing stages, for example, before fractionation and instead of vacuum distillation, or in oil fields and instead of vacuum distillation, etc.

Claims (1)

Способ управления технологическим процессом и номенклатурой выпускаемых нефтепродуктов при переработке нефти, заключающийся в ее физическом разделении на фракции, отличающийся тем, что для увеличения выхода наиболее ценных светлых топливных фракций нефть подвергают криолизу при температуре не выше -15°С в течение не менее 20 ч с предварительным введением в нее донорной присадки (воды) в количестве не менее 1% на различных этапах ее переработки:- перед фракционированием вместо вакуумной перегонки на нефтепромыслах, где одновременно с повышением содержания топливных фракций в нефти происходит ее обезвоживание и обессоливание (частичное или полное), а также в различных сочетаниях этапов переработки, например перед фракционированием и вместо вакуумной перегонки, или на нефтепромыслах и вместо вакуумной перегонки и т.д. A method of controlling the technological process and the nomenclature of oil products produced during oil refining, which consists in its physical separation into fractions, characterized in that to increase the yield of the most valuable light fuel fractions, the oil is subjected to cryolysis at a temperature of no higher than -15 ° C for at least 20 hours by preliminary introducing into it a donor additive (water) in an amount of at least 1% at various stages of its processing: - before fractionation instead of vacuum distillation in oil fields, where at the same time Decreasing the content of fuel fractions in oil, it is dehydrated and desalted (partial or complete), as well as in various combinations of processing stages, for example, before fractionation and instead of vacuum distillation, or in oil fields and instead of vacuum distillation, etc.
RU2014142902A 2013-12-18 2014-10-24 Method of controlling process control and list of produced oil products during oil refining (versions) RU2607089C2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
UZJAP20130528 2013-12-18
UZ1300528 2013-12-18

Publications (2)

Publication Number Publication Date
RU2014142902A true RU2014142902A (en) 2016-05-20
RU2607089C2 RU2607089C2 (en) 2017-01-10

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Application Number Title Priority Date Filing Date
RU2014142902A RU2607089C2 (en) 2013-12-18 2014-10-24 Method of controlling process control and list of produced oil products during oil refining (versions)

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RU (1) RU2607089C2 (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU694530A1 (en) * 1978-06-18 1979-10-30 Научно-Исследовательский И Проектный Институт По Комплексной Автоматизации Нефтяной И Химической Промышленности Method of oil dehydration control at settling stage
RU2301250C1 (en) * 2006-01-24 2007-06-20 Юрий Владимирович Фещенко Hydrocarbon feedstock distillation process and plant

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Effective date: 20201025