RU2012128049A - METHOD OF CATALYTIC DEPARAFFINIZATION - Google Patents

METHOD OF CATALYTIC DEPARAFFINIZATION Download PDF

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RU2012128049A
RU2012128049A RU2012128049/04A RU2012128049A RU2012128049A RU 2012128049 A RU2012128049 A RU 2012128049A RU 2012128049/04 A RU2012128049/04 A RU 2012128049/04A RU 2012128049 A RU2012128049 A RU 2012128049A RU 2012128049 A RU2012128049 A RU 2012128049A
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metal
catalyst
dewaxing
hydrocarbon feed
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RU2012128049/04A
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Russian (ru)
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Кристин Н. ЭЛИА
Тимоти Ли ХИЛБЕРТ
Луис Фрэнсис БЕРНС
Эрик Д. ДЖОСЕК
Джинок Т. КИМ
Сильвэйн С. ХАНЦЕР
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ЭкссонМобил Рисерч энд Энджиниринг Компани
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Publication of RU2012128049A publication Critical patent/RU2012128049A/en

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    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
    • C10G45/60—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used
    • C10G45/64—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used containing crystalline alumino-silicates, e.g. molecular sieves
    • 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
    • C10G73/00—Recovery or refining of mineral waxes, e.g. montan wax
    • C10G73/02—Recovery of petroleum waxes from hydrocarbon oils; Dewaxing of hydrocarbon oils
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
    • C10G45/60—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used
    • C10G45/62—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used containing platinum group metals or compounds thereof
    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
    • C10G47/12—Inorganic carriers
    • 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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
    • C10G65/043—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps at least one step being a change in the structural skeleton
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20—Characteristics of the feedstock or the products
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/201—Impurities
    • C10G2300/202—Heteroatoms content, i.e. S, N, O, P
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4018—Spatial velocity, e.g. LHSV, WHSV

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

Abstract

1. Способ каталитической депарафинизации, включающий:(a) использование в реакционной зоне катализатора, содержащего от 40 до 80 мас.% ZSM-48, имеющего мольное отношение диоксида кремния к оксиду алюминия менее 200:1, и от 0,3 до 1,5 мас.% металла или соединения металла групп 8-10 Периодической системы элементов; и(b) периодическое приведение указанного катализатора в указанной реакционной зоне, в условиях проведения депарафинизации, в контакт с первым углеводородным сырьем, имеющим содержание парафинов менее 50 мас.%, и со вторым углеводородным сырьем, имеющим содержание парафинов 50 мас.% или более.2. Способ по п.1, в котором катализатор включает от 50 до 70 мас.% ZSM-48, имеющего мольное отношение диоксида кремния к оксиду алюминия менее 200:1.3. Способ по п.1 или 2, в котором ZSM-48 имеет мольное отношение диоксида кремния к оксиду алюминия 100:1 или менее.4. Способ по п.1, в котором катализатор включает от 0,3 до 0,8 мас.% металла или соединения металла групп 8-10 Периодической системы элементов.5. Способ по п.1, в котором указанный металл или соединение металла групп 8-10 Периодической системы элементов включает платину.6. Способ по п.1, в котором катализатор дополнительно включает связующее - неорганический оксид.7. Способ по п.1, в котором указанные условия депарафинизации включают температуру 365°С или менее.8. Способ по п.1, в котором указанные условия депарафинизации включают температуру от 290° до 365°С.9. Способ по п.1, в котором указанные условия депарафинизации включают часовую объемную скорость жидкости углеводородного сырья по меньшей мере 0,4 ч.10. Способ по п.1, в котором указанные условия депарафинизации включают часовую объемную скорость жидкости углев�1. The method of catalytic dewaxing, including: (a) the use in the reaction zone of a catalyst containing from 40 to 80 wt.% ZSM-48, having a molar ratio of silicon dioxide to alumina less than 200: 1, and from 0.3 to 1, 5 wt.% Metal or metal compound of groups 8-10 of the Periodic Table of the Elements; and (b) periodically bringing said catalyst in said reaction zone, under dewaxing conditions, into contact with a first hydrocarbon feed having a paraffin content of less than 50 wt% and a second hydrocarbon feed having a paraffin content of 50 wt% or more. 2. The method of claim 1, wherein the catalyst comprises 50 to 70 wt% ZSM-48 having a silica to alumina molar ratio of less than 200: 1.3. The method of claim 1 or 2, wherein the ZSM-48 has a silica to alumina molar ratio of 100: 1 or less. The method according to claim 1, wherein the catalyst comprises 0.3 to 0.8 wt.% Of a metal or metal compound of Groups 8-10 of the Periodic Table of Elements. The method of claim 1, wherein said metal or metal compound of Groups 8-10 of the Periodic Table of Elements comprises platinum. The method of claim 1, wherein the catalyst further comprises an inorganic oxide binder. The method of claim 1, wherein said dewaxing conditions comprise a temperature of 365 ° C or less. The method of claim 1, wherein said dewaxing conditions comprise a temperature of 290 ° to 365 ° C. The method according to claim 1, wherein said dewaxing conditions include a liquid hourly space velocity of the hydrocarbon feed of at least 0.4 h. The method of claim 1, wherein said dewaxing conditions comprise liquid hourly space velocity of the carbohydrate.

Claims (12)

1. Способ каталитической депарафинизации, включающий:1. The method of catalytic dewaxing, including: (a) использование в реакционной зоне катализатора, содержащего от 40 до 80 мас.% ZSM-48, имеющего мольное отношение диоксида кремния к оксиду алюминия менее 200:1, и от 0,3 до 1,5 мас.% металла или соединения металла групп 8-10 Периодической системы элементов; и(a) using in the reaction zone a catalyst containing from 40 to 80 wt.% ZSM-48, having a molar ratio of silica to alumina of less than 200: 1, and from 0.3 to 1.5 wt.% of a metal or metal compound groups 8-10 of the Periodic system of elements; and (b) периодическое приведение указанного катализатора в указанной реакционной зоне, в условиях проведения депарафинизации, в контакт с первым углеводородным сырьем, имеющим содержание парафинов менее 50 мас.%, и со вторым углеводородным сырьем, имеющим содержание парафинов 50 мас.% или более.(b) periodically bringing said catalyst in said reaction zone, under conditions of dewaxing, into contact with a first hydrocarbon feed having a paraffin content of less than 50 wt.% and a second hydrocarbon feed having a paraffin content of 50 wt.% or more. 2. Способ по п.1, в котором катализатор включает от 50 до 70 мас.% ZSM-48, имеющего мольное отношение диоксида кремния к оксиду алюминия менее 200:1.2. The method according to claim 1, in which the catalyst comprises from 50 to 70 wt.% ZSM-48, having a molar ratio of silicon dioxide to alumina of less than 200: 1. 3. Способ по п.1 или 2, в котором ZSM-48 имеет мольное отношение диоксида кремния к оксиду алюминия 100:1 или менее.3. The method according to claim 1 or 2, in which ZSM-48 has a molar ratio of silicon dioxide to alumina of 100: 1 or less. 4. Способ по п.1, в котором катализатор включает от 0,3 до 0,8 мас.% металла или соединения металла групп 8-10 Периодической системы элементов.4. The method according to claim 1, in which the catalyst comprises from 0.3 to 0.8 wt.% Metal or metal compounds of groups 8-10 of the Periodic system of elements. 5. Способ по п.1, в котором указанный металл или соединение металла групп 8-10 Периодической системы элементов включает платину.5. The method according to claim 1, wherein said metal or metal compound of groups 8-10 of the Periodic system of elements includes platinum. 6. Способ по п.1, в котором катализатор дополнительно включает связующее - неорганический оксид.6. The method according to claim 1, in which the catalyst further comprises a binder - inorganic oxide. 7. Способ по п.1, в котором указанные условия депарафинизации включают температуру 365°С или менее.7. The method according to claim 1, wherein said dewaxing conditions include a temperature of 365 ° C. or less. 8. Способ по п.1, в котором указанные условия депарафинизации включают температуру от 290° до 365°С.8. The method according to claim 1, wherein said dewaxing conditions include a temperature of 290 ° to 365 ° C. 9. Способ по п.1, в котором указанные условия депарафинизации включают часовую объемную скорость жидкости углеводородного сырья по меньшей мере 0,4 ч-1.9. The method according to claim 1, wherein said dewaxing conditions include an hourly space velocity of a liquid hydrocarbon feed of at least 0.4 h −1 . 10. Способ по п.1, в котором указанные условия депарафинизации включают часовую объемную скорость жидкости углеводородного сырья от 0,95 до 2 ч-1.10. The method according to claim 1, wherein said dewaxing conditions include hourly space velocity of a liquid hydrocarbon feed from 0.95 to 2 h -1 . 11. Способ по п.1, в котором один или оба из указанных первого и второго углеводородного сырья имеет содержание азота до 150 млн ч.11. The method according to claim 1, in which one or both of these first and second hydrocarbon feeds has a nitrogen content of up to 150 million hours 12. Способ по п.1, в котором один или оба из указанных первого и второго углеводородного сырья имеет содержание серы до 1000 млн ч. 12. The method according to claim 1, in which one or both of these first and second hydrocarbon feeds has a sulfur content of up to 1000 million hours
RU2012128049/04A 2009-12-24 2010-12-21 METHOD OF CATALYTIC DEPARAFFINIZATION RU2012128049A (en)

Applications Claiming Priority (3)

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US28483509P 2009-12-24 2009-12-24
US61/284,835 2009-12-24
PCT/US2010/061542 WO2011079116A1 (en) 2009-12-24 2010-12-21 Catalytic dewaxing process

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US (1) US20110180453A1 (en)
EP (1) EP2516597A1 (en)
JP (1) JP2013515821A (en)
KR (1) KR20120114321A (en)
CN (1) CN102686709A (en)
CA (1) CA2784146A1 (en)
IN (1) IN2012DN05208A (en)
RU (1) RU2012128049A (en)
SG (1) SG181451A1 (en)
WO (1) WO2011079116A1 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9944865B2 (en) 2015-12-28 2018-04-17 Exxonmobil Research And Engineering Company Dewaxing catalyst with improved aromatic saturation activity
CA3009745C (en) 2015-12-28 2024-04-16 Exxonmobil Research And Engineering Company Sequential impregnation of a porous support for noble metal alloy formation
EP4381029A1 (en) 2021-08-06 2024-06-12 ExxonMobil Technology and Engineering Company Hydro-dealkylation process to generate high quality fuels, base stocks and waxes

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4397827A (en) * 1979-07-12 1983-08-09 Mobil Oil Corporation Silico-crystal method of preparing same and catalytic conversion therewith
US4375573A (en) * 1979-08-03 1983-03-01 Mobil Oil Corporation Selective production and reaction of p-Disubstituted aromatics over zeolite ZSM-48
US4423021A (en) * 1979-08-08 1983-12-27 Mobil Oil Corporation Method of preparing silico-crystal ZSM-48
US4448675A (en) * 1981-09-17 1984-05-15 Mobil Oil Corporation Silico-crystal ZSM-48 method of preparing same and catalytic conversion therewith
US20040108250A1 (en) * 2002-10-08 2004-06-10 Murphy William J. Integrated process for catalytic dewaxing
US7125818B2 (en) * 2002-10-08 2006-10-24 Exxonmobil Research & Engineering Co. Catalyst for wax isomerate yield enhancement by oxygenate pretreatment
US7132042B2 (en) * 2002-10-08 2006-11-07 Exxonmobil Research And Engineering Company Production of fuels and lube oils from fischer-tropsch wax
TWI450762B (en) * 2005-12-13 2014-09-01 Exxonmobil Res & Eng Co High activity zsm-48 and methods for dewaxing
US7482300B2 (en) * 2005-12-13 2009-01-27 Exxonmobil Research And Engineering Company High activity ZSM-48 and methods for dewaxing

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KR20120114321A (en) 2012-10-16
JP2013515821A (en) 2013-05-09
CA2784146A1 (en) 2011-06-30
WO2011079116A1 (en) 2011-06-30
CN102686709A (en) 2012-09-19
US20110180453A1 (en) 2011-07-28
SG181451A1 (en) 2012-07-30
EP2516597A1 (en) 2012-10-31

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