RU2009148675A - Комплексная гидропереработка с высокопроизводительными катализаторами - Google Patents
Комплексная гидропереработка с высокопроизводительными катализаторами Download PDFInfo
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- RU2009148675A RU2009148675A RU2009148675/04A RU2009148675A RU2009148675A RU 2009148675 A RU2009148675 A RU 2009148675A RU 2009148675/04 A RU2009148675/04 A RU 2009148675/04A RU 2009148675 A RU2009148675 A RU 2009148675A RU 2009148675 A RU2009148675 A RU 2009148675A
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- 239000003054 catalyst Substances 0.000 title claims abstract 35
- 238000000034 method Methods 0.000 claims abstract 26
- 239000002184 metal Substances 0.000 claims abstract 10
- 229910052751 metal Inorganic materials 0.000 claims abstract 10
- 239000002994 raw material Substances 0.000 claims abstract 10
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract 5
- 239000002199 base oil Substances 0.000 claims abstract 5
- 150000001491 aromatic compounds Chemical class 0.000 claims abstract 4
- 238000005984 hydrogenation reaction Methods 0.000 claims abstract 3
- 102220500397 Neutral and basic amino acid transport protein rBAT_M41T_mutation Human genes 0.000 claims abstract 2
- 238000009835 boiling Methods 0.000 claims abstract 2
- 229930195733 hydrocarbon Natural products 0.000 claims abstract 2
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract 2
- 230000007935 neutral effect Effects 0.000 claims abstract 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 claims 2
- 229910004298 SiO 2 Inorganic materials 0.000 claims 2
- 239000000203 mixture Substances 0.000 claims 2
- 229910052763 palladium Inorganic materials 0.000 claims 2
- 229910052697 platinum Inorganic materials 0.000 claims 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract 1
- 229910052681 coesite Inorganic materials 0.000 abstract 1
- 229910052593 corundum Inorganic materials 0.000 abstract 1
- 229910052906 cristobalite Inorganic materials 0.000 abstract 1
- 239000000377 silicon dioxide Substances 0.000 abstract 1
- 235000012239 silicon dioxide Nutrition 0.000 abstract 1
- 229910052682 stishovite Inorganic materials 0.000 abstract 1
- 229910052905 tridymite Inorganic materials 0.000 abstract 1
- 229910001845 yogo sapphire Inorganic materials 0.000 abstract 1
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- 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J29/00—Catalysts comprising molecular sieves
- B01J29/03—Catalysts comprising molecular sieves not having base-exchange properties
- B01J29/0308—Mesoporous materials not having base exchange properties, e.g. Si-MCM-41
- B01J29/0316—Mesoporous materials not having base exchange properties, e.g. Si-MCM-41 containing iron group metals, noble metals or copper
- B01J29/0325—Noble metals
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- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/041—Mesoporous materials having base exchange properties, e.g. Si/Al-MCM-41
- B01J29/042—Mesoporous materials having base exchange properties, e.g. Si/Al-MCM-41 containing iron group metals, noble metals or copper
- B01J29/043—Noble metals
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- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
- B01J29/72—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65 containing iron group metals, noble metals or copper
- B01J29/74—Noble metals
- B01J29/7461—MRE-type, e.g. ZSM-48
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/31—Density
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- 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
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- 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
- C10G65/08—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 hydrogenation of the aromatic hydrocarbons
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- 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
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/063—Titanium; Oxides or hydroxides thereof
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/20—After treatment, characterised by the effect to be obtained to introduce other elements in the catalyst composition comprising the molecular sieve, but not specially in or on the molecular sieve itself
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/30—After treatment, characterised by the means used
- B01J2229/42—Addition of matrix or binder particles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/44—Palladium
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
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- 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
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/301—Boiling range
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- 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
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/302—Viscosity
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- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
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- 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
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- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
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Abstract
1. Способ получения базового масла, включающий: ! обеспечение первого катализатора, включающего по меньшей мере один металл VIII группы, нанесенный на носитель катализатора, и имеющего плотность 600 кг/м3 или менее; ! обеспечение второго катализатора, включающего по меньшей мере один металл VIII группы, имеющего производительность при депарафинизации достаточную для обеспечения обработки потока легких нейтральных (150N) углеводородов из установки для гидрокрекинга среднего давления, имеющего кинематическую вязкость при 100°С менее 5 и конечную температуру кипения менее 550°С, при 320°С и ЧОСЖ, равной 1, с получением базового масла, имеющего температуру застывания менее -15°С и ПВ по меньшей мере 160; ! приведение сырья в контакт с первым катализатором при эффективных условиях для обработки сырья, причем указанные эффективные условия являются эффективными для одного из процессов, выбранного из гидрообработки, гидроочистки или гидрирования ароматических соединений, и ! приведение обработанного сырья в контакт со вторым катализатором при условиях, эффективных для депарафинизации обработанного сырья. ! 2. Способ по п.1, в котором катализатор депарафинизации включает ZSM-48 с соотношением SiO2:Al2O3, составляющим от примерно 70 до примерно 110. ! 3. Способ по п.1, в котором катализатор депарафинизации имеет плотность 600 кг/м3 или менее. ! 4. Способ по п.1, в котором первый катализатор включает носитель M41S. ! 5. Способ по п.1, в котором первый катализатор включает МСМ-41. ! 6. Способ по п.1, в котором первый катализатор имеет плотность 550 кг/м3 или менее. ! 7. Способ по п.1, в котором первый катализатор имеет плотность 500 кг/м3 или менее. ! 8. Способ по п.1, в ко
Claims (15)
1. Способ получения базового масла, включающий:
обеспечение первого катализатора, включающего по меньшей мере один металл VIII группы, нанесенный на носитель катализатора, и имеющего плотность 600 кг/м3 или менее;
обеспечение второго катализатора, включающего по меньшей мере один металл VIII группы, имеющего производительность при депарафинизации достаточную для обеспечения обработки потока легких нейтральных (150N) углеводородов из установки для гидрокрекинга среднего давления, имеющего кинематическую вязкость при 100°С менее 5 и конечную температуру кипения менее 550°С, при 320°С и ЧОСЖ, равной 1, с получением базового масла, имеющего температуру застывания менее -15°С и ПВ по меньшей мере 160;
приведение сырья в контакт с первым катализатором при эффективных условиях для обработки сырья, причем указанные эффективные условия являются эффективными для одного из процессов, выбранного из гидрообработки, гидроочистки или гидрирования ароматических соединений, и
приведение обработанного сырья в контакт со вторым катализатором при условиях, эффективных для депарафинизации обработанного сырья.
2. Способ по п.1, в котором катализатор депарафинизации включает ZSM-48 с соотношением SiO2:Al2O3, составляющим от примерно 70 до примерно 110.
3. Способ по п.1, в котором катализатор депарафинизации имеет плотность 600 кг/м3 или менее.
4. Способ по п.1, в котором первый катализатор включает носитель M41S.
5. Способ по п.1, в котором первый катализатор включает МСМ-41.
6. Способ по п.1, в котором первый катализатор имеет плотность 550 кг/м3 или менее.
7. Способ по п.1, в котором первый катализатор имеет плотность 500 кг/м3 или менее.
8. Способ по п.1, в котором первый катализатор включает по меньшей мере один металл VIII группы, выбранный из Pt, Pd и их смеси.
9. Способ по п.8, в котором первый катализатор включает по меньшей мере 0,5 мас.% по меньшей мере одного металла VIII группы.
10. Способ по п.1, дополнительно включающий приведение депарафинизированного, обработанного сырья в контакт с третьим катализатором при условиях, эффективных для гидроочистки или гидрирования ароматических соединений, причем указанный третий катализатор имеет плотность 600 кг/м3 или менее.
11. Способ по п.10, в котором третий катализатор включает МСМ-41.
12. Способ по п.10, в котором третий катализатор имеет плотность 550 кг/м3 или менее.
13. Способ по п.10, в котором третий катализатор включает по меньшей мере один металл VIII группы, выбранный из Pt, Pd и их смеси.
14. Способ по п.10, в котором третий катализатор включает по меньшей мере 0,5 масс.% по меньшей мере одного металла VIII группы.
15. Способ получения базового масла, включающий:
приведение сырья в контакт с первым катализатором, причем указанный первый катализатор включает по меньшей мере один металл VIII группы, нанесенный на носитель катализатора, и имеет плотность 600 кг/м3 или менее, при эффективных условиях для обработки сырья, причем указанные эффективные условия являются эффективными для одного из процессов, выбранного из гидрообработки, гидроочистки или гидрирования ароматических соединений,и
приведение обработанного сырья в контакт с катализатором, включающим ZSM-48 с соотношением SiO2:Al2O3, составляющим от примерно 70 до примерно 110, и металлический гидрирующий компонент, при условиях, эффективных для депарафинизации обработанного сырья.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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US93453307P | 2007-06-13 | 2007-06-13 | |
US60/934,533 | 2007-06-13 |
Publications (2)
Publication Number | Publication Date |
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RU2009148675A true RU2009148675A (ru) | 2011-07-20 |
RU2458969C2 RU2458969C2 (ru) | 2012-08-20 |
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US (2) | US8864975B2 (ru) |
EP (1) | EP2155840B1 (ru) |
JP (1) | JP5282087B2 (ru) |
KR (1) | KR101488547B1 (ru) |
CN (1) | CN101765651A (ru) |
CA (1) | CA2692033C (ru) |
MY (1) | MY157681A (ru) |
RU (1) | RU2458969C2 (ru) |
SG (1) | SG184753A1 (ru) |
WO (1) | WO2008156698A2 (ru) |
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2911866B1 (fr) * | 2007-01-30 | 2009-03-06 | Inst Francais Du Petrole | Solide cristalise izm-1 et son procede de preparation. |
US8003074B2 (en) * | 2007-09-18 | 2011-08-23 | Exxonmobil Research And Engineering Company | Synthesis of high activity ZSM-48 |
US8906224B2 (en) * | 2009-12-23 | 2014-12-09 | Exxonmobil Research And Engineering Company | Sweet or sour service catalytic dewaxing in block mode configuration |
US20120000829A1 (en) * | 2010-06-30 | 2012-01-05 | Exxonmobil Research And Engineering Company | Process for the preparation of group ii and group iii lube base oils |
US20120000818A1 (en) * | 2010-06-30 | 2012-01-05 | Exxonmobil Research And Engineering Company | Process for the preparation of group ii and group iii lube base oils |
FR2969647B1 (fr) * | 2010-12-22 | 2012-12-21 | IFP Energies Nouvelles | Procede d'hydrocraquage de coupes hydrocarbonees utilisant un catalyseur a base d'heteropolyanions pieges dans un support oxyde mesostructure |
US9340733B2 (en) * | 2010-12-22 | 2016-05-17 | Centre National De La Recherche Scientifique | Process for Hydrodesulphuration of gasoil cuts using a catalyst based on heteropolyanions trapped in a mesostructured silica support |
FR2969646B1 (fr) * | 2010-12-22 | 2012-12-28 | IFP Energies Nouvelles | Procede d'hydrodesulfuration de coupes essences utilisant un catalyseur a base d'heteropolyanions pieges dans un support silicique mesostructure |
EP2691492A4 (en) * | 2011-03-31 | 2015-06-17 | Chevron Usa Inc | NEW METHOD AND CATALYST SYSTEM FOR IMPROVING THE DESIGN CATALYST STABILITY AND LUBRICATING OIL LEAKAGE |
US9029301B2 (en) * | 2011-12-15 | 2015-05-12 | Exxonmobil Research And Engineering Company | Saturation process for making lubricant base oils |
US9809762B2 (en) | 2011-12-15 | 2017-11-07 | Exxonmobil Research And Engineering Company | Saturation process for making lubricant base oils |
JP5998127B2 (ja) * | 2012-03-30 | 2016-09-28 | Jxエネルギー株式会社 | 潤滑油用基油の製造方法 |
CN105849044B (zh) * | 2013-12-26 | 2018-10-26 | 埃克森美孚研究工程公司 | Zsm-48晶体的合成 |
JP6034479B2 (ja) * | 2015-12-11 | 2016-11-30 | シェブロン ユー.エス.エー. インコーポレイテッド | 脱蝋触媒の安定性及び潤滑油の収率を改良するための新規なプロセス及び触媒システム |
WO2017102054A1 (en) * | 2015-12-18 | 2017-06-22 | Merck Patent Gmbh | Process for the production of hollow plastic articles by rotational molding polymeric compounds in a rotomold |
CA3038902A1 (en) * | 2016-10-14 | 2018-04-19 | Exxonmobil Research And Engineering Company | Lubricant basestock production with enhanced aromatic saturation |
Family Cites Families (23)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5857221B2 (ja) * | 1974-11-25 | 1983-12-19 | トウアネンリヨウコウギヨウ カブシキガイシヤ | スイソカシヨクバイ |
US4678766A (en) * | 1983-10-19 | 1987-07-07 | Mobil Oil Corporation | Enhancement of shape selectivity of zeolites |
US5075269A (en) * | 1988-12-15 | 1991-12-24 | Mobil Oil Corp. | Production of high viscosity index lubricating oil stock |
DE69312268T2 (de) * | 1992-01-30 | 1997-12-18 | Exxon Chemical Patents Inc | Alkenoligomerisierung |
JP3628023B2 (ja) * | 1994-10-27 | 2005-03-09 | モービル・オイル・コーポレイション | ロウ水素化異性化法 |
CA2263849C (en) | 1996-10-31 | 2004-12-07 | Mobil Oil Corporation | Process for highly shape selective dewaxing which retards catalyst aging |
US6096189A (en) * | 1996-12-17 | 2000-08-01 | Exxon Research And Engineering Co. | Hydroconversion process for making lubricating oil basestocks |
CN1290193A (zh) * | 1997-12-03 | 2001-04-04 | 埃克森化学专利公司 | 包含局部涂有第二沸石的沸石的催化剂及其用于烃类转化的用途 |
US6231749B1 (en) * | 1998-05-15 | 2001-05-15 | Mobil Oil Corporation | Production of high viscosity index lubricants |
US6190532B1 (en) * | 1998-07-13 | 2001-02-20 | Mobil Oil Corporation | Production of high viscosity index lubricants |
MY139353A (en) * | 2001-03-05 | 2009-09-30 | Shell Int Research | Process to prepare a lubricating base oil and a gas oil |
US6652735B2 (en) | 2001-04-26 | 2003-11-25 | Exxonmobil Research And Engineering Company | Process for isomerization dewaxing of hydrocarbon streams |
US6723229B2 (en) * | 2001-05-11 | 2004-04-20 | Exxonmobil Research And Engineering Company | Process for the production of medicinal white oil using M41S and sulfur sorbent |
DE10133175B4 (de) * | 2001-07-07 | 2006-04-20 | Korea Advanced Institute Of Science And Technology | Verfahren zur Herstellung metallhaltiger bi-funktionaler Katalysatoren zum Entparaffinieren |
US7282137B2 (en) * | 2002-10-08 | 2007-10-16 | Exxonmobil Research And Engineering Company | Process for preparing basestocks having high VI |
US7220350B2 (en) * | 2002-10-08 | 2007-05-22 | Exxonmobil Research And Engineering Company | Wax isomerate yield enhancement by oxygenate pretreatment of catalyst |
WO2004053027A1 (en) * | 2002-12-09 | 2004-06-24 | Shell Internationale Research Maatschappij B.V. | Process for the preparation of a lubricant |
DE60319422T2 (de) | 2002-12-09 | 2009-02-19 | Shell Internationale Research Maatschappij B.V. | Verfahren zur herstellung von basisöl mit einem viskositätsindex von 80 bis 140 |
JP4414181B2 (ja) | 2003-09-19 | 2010-02-10 | 株式会社Access | メッセージ表示端末及びゲートウェイサーバ、並びにメッセージ表示端末用プログラム及びゲートウェイサーバ用プログラム |
US6923949B1 (en) * | 2004-03-05 | 2005-08-02 | Exxonmobil Research And Engineering Company | Synthesis of ZSM-48 crystals with heterostructural, non ZSM-48, seeding |
BRPI0611906B1 (pt) * | 2005-06-23 | 2015-09-08 | Shell Int Research | formulação de óleo estável à oxidação, e, processo para preparar a formulação, e, uso da formulação |
US7482300B2 (en) * | 2005-12-13 | 2009-01-27 | Exxonmobil Research And Engineering Company | High activity ZSM-48 and methods for dewaxing |
TWI450762B (zh) * | 2005-12-13 | 2014-09-01 | Exxonmobil Res & Eng Co | 具有高活性之zsm-48及用以去蠟之方法 |
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- 2008-06-13 MY MYPI20095315A patent/MY157681A/en unknown
- 2008-06-13 CN CN200880020172A patent/CN101765651A/zh active Pending
- 2008-06-13 US US12/157,968 patent/US8864975B2/en active Active
- 2008-06-13 EP EP08768472.6A patent/EP2155840B1/en active Active
- 2008-06-13 KR KR1020107000654A patent/KR101488547B1/ko active IP Right Grant
- 2008-06-13 SG SG2012068169A patent/SG184753A1/en unknown
- 2008-06-13 RU RU2009148675/04A patent/RU2458969C2/ru not_active IP Right Cessation
- 2008-06-13 JP JP2010512209A patent/JP5282087B2/ja active Active
- 2008-06-13 US US12/157,971 patent/US8864976B2/en active Active
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Also Published As
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EP2155840A2 (en) | 2010-02-24 |
SG184753A1 (en) | 2012-10-30 |
MY157681A (en) | 2016-07-15 |
US8864975B2 (en) | 2014-10-21 |
US20080314797A1 (en) | 2008-12-25 |
JP5282087B2 (ja) | 2013-09-04 |
WO2008156698A2 (en) | 2008-12-24 |
CA2692033C (en) | 2016-07-19 |
US20090005627A1 (en) | 2009-01-01 |
CN101765651A (zh) | 2010-06-30 |
JP2010529280A (ja) | 2010-08-26 |
CA2692033A1 (en) | 2008-12-24 |
EP2155840B1 (en) | 2018-03-21 |
KR20100022523A (ko) | 2010-03-02 |
US8864976B2 (en) | 2014-10-21 |
RU2458969C2 (ru) | 2012-08-20 |
WO2008156698A3 (en) | 2009-02-19 |
KR101488547B1 (ko) | 2015-02-02 |
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