RU2323779C2 - Новый цеолитсодержащий композиционный материал, способ получения и способ применения указанного материала в качестве катализатора - Google Patents
Новый цеолитсодержащий композиционный материал, способ получения и способ применения указанного материала в качестве катализатора Download PDFInfo
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- RU2323779C2 RU2323779C2 RU2006117333/04A RU2006117333A RU2323779C2 RU 2323779 C2 RU2323779 C2 RU 2323779C2 RU 2006117333/04 A RU2006117333/04 A RU 2006117333/04A RU 2006117333 A RU2006117333 A RU 2006117333A RU 2323779 C2 RU2323779 C2 RU 2323779C2
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- 238000000034 method Methods 0.000 title claims abstract 47
- 239000010457 zeolite Substances 0.000 title claims abstract 15
- 229910021536 Zeolite Inorganic materials 0.000 title claims abstract 14
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title claims abstract 14
- 239000003054 catalyst Substances 0.000 title claims abstract 8
- 238000004519 manufacturing process Methods 0.000 title abstract 2
- 239000002131 composite material Substances 0.000 title 1
- 229910052809 inorganic oxide Inorganic materials 0.000 claims abstract 14
- 239000000463 material Substances 0.000 claims abstract 10
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract 7
- 229930195733 hydrocarbon Natural products 0.000 claims abstract 7
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract 7
- 230000032798 delamination Effects 0.000 claims abstract 4
- 230000000694 effects Effects 0.000 claims abstract 2
- 230000002687 intercalation Effects 0.000 claims abstract 2
- 238000009830 intercalation Methods 0.000 claims abstract 2
- 239000003921 oil Substances 0.000 claims 13
- 238000009835 boiling Methods 0.000 claims 10
- 238000010438 heat treatment Methods 0.000 claims 10
- 239000000203 mixture Substances 0.000 claims 10
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 claims 9
- 238000005917 acylation reaction Methods 0.000 claims 8
- 238000006243 chemical reaction Methods 0.000 claims 8
- 150000002894 organic compounds Chemical class 0.000 claims 8
- 239000011363 dried mixture Substances 0.000 claims 7
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims 6
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 claims 6
- 230000010933 acylation Effects 0.000 claims 6
- 230000003197 catalytic effect Effects 0.000 claims 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 6
- 239000002243 precursor Substances 0.000 claims 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims 4
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims 4
- 238000001354 calcination Methods 0.000 claims 3
- 239000003795 chemical substances by application Substances 0.000 claims 3
- NXQMCAOPTPLPRL-UHFFFAOYSA-N 2-(2-benzoyloxyethoxy)ethyl benzoate Chemical compound C=1C=CC=CC=1C(=O)OCCOCCOC(=O)C1=CC=CC=C1 NXQMCAOPTPLPRL-UHFFFAOYSA-N 0.000 claims 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims 2
- GYHNNYVSQQEPJS-UHFFFAOYSA-N Gallium Chemical compound [Ga] GYHNNYVSQQEPJS-UHFFFAOYSA-N 0.000 claims 2
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical group O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims 2
- UWHCKJMYHZGTIT-UHFFFAOYSA-N Tetraethylene glycol, Natural products OCCOCCOCCOCCO UWHCKJMYHZGTIT-UHFFFAOYSA-N 0.000 claims 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims 2
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 claims 2
- SLINHMUFWFWBMU-UHFFFAOYSA-N Triisopropanolamine Chemical compound CC(O)CN(CC(C)O)CC(C)O SLINHMUFWFWBMU-UHFFFAOYSA-N 0.000 claims 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims 2
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 claims 2
- 239000012670 alkaline solution Substances 0.000 claims 2
- 229910052782 aluminium Inorganic materials 0.000 claims 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims 2
- 150000001491 aromatic compounds Chemical class 0.000 claims 2
- 239000011230 binding agent Substances 0.000 claims 2
- 238000004523 catalytic cracking Methods 0.000 claims 2
- 238000004517 catalytic hydrocracking Methods 0.000 claims 2
- 239000003093 cationic surfactant Substances 0.000 claims 2
- 229910052804 chromium Inorganic materials 0.000 claims 2
- 239000011651 chromium Substances 0.000 claims 2
- 239000011280 coal tar Substances 0.000 claims 2
- 229910017052 cobalt Inorganic materials 0.000 claims 2
- 239000010941 cobalt Substances 0.000 claims 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims 2
- 229910052802 copper Inorganic materials 0.000 claims 2
- 239000010949 copper Substances 0.000 claims 2
- 238000001035 drying Methods 0.000 claims 2
- 229910052733 gallium Inorganic materials 0.000 claims 2
- 230000003993 interaction Effects 0.000 claims 2
- 229910052742 iron Inorganic materials 0.000 claims 2
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 claims 2
- 229910052751 metal Inorganic materials 0.000 claims 2
- 239000002184 metal Substances 0.000 claims 2
- 229910021645 metal ion Inorganic materials 0.000 claims 2
- 229910052750 molybdenum Inorganic materials 0.000 claims 2
- 239000011733 molybdenum Substances 0.000 claims 2
- 238000000465 moulding Methods 0.000 claims 2
- 229910052759 nickel Inorganic materials 0.000 claims 2
- 239000003079 shale oil Substances 0.000 claims 2
- HXJUTPCZVOIRIF-UHFFFAOYSA-N sulfolane Chemical compound O=S1(=O)CCCC1 HXJUTPCZVOIRIF-UHFFFAOYSA-N 0.000 claims 2
- 239000011275 tar sand Substances 0.000 claims 2
- FAGUFWYHJQFNRV-UHFFFAOYSA-N tetraethylenepentamine Chemical compound NCCNCCNCCNCCN FAGUFWYHJQFNRV-UHFFFAOYSA-N 0.000 claims 2
- 229910052719 titanium Inorganic materials 0.000 claims 2
- 239000010936 titanium Substances 0.000 claims 2
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N triethylene glycol Chemical compound OCCOCCOCCO ZIBGPFATKBEMQZ-UHFFFAOYSA-N 0.000 claims 2
- 229910052720 vanadium Inorganic materials 0.000 claims 2
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 claims 2
- 229910052725 zinc Inorganic materials 0.000 claims 2
- 239000011701 zinc Substances 0.000 claims 2
- 229910052726 zirconium Inorganic materials 0.000 claims 2
- 229920002472 Starch Polymers 0.000 claims 1
- 150000001266 acyl halides Chemical class 0.000 claims 1
- 230000029936 alkylation Effects 0.000 claims 1
- 238000005804 alkylation reaction Methods 0.000 claims 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims 1
- 238000005899 aromatization reaction Methods 0.000 claims 1
- 239000010426 asphalt Substances 0.000 claims 1
- 150000001244 carboxylic acid anhydrides Chemical class 0.000 claims 1
- 230000018044 dehydration Effects 0.000 claims 1
- 238000006297 dehydration reaction Methods 0.000 claims 1
- 238000006356 dehydrogenation reaction Methods 0.000 claims 1
- 239000002283 diesel fuel Substances 0.000 claims 1
- 238000006471 dimerization reaction Methods 0.000 claims 1
- 238000007323 disproportionation reaction Methods 0.000 claims 1
- 238000004299 exfoliation Methods 0.000 claims 1
- 230000036571 hydration Effects 0.000 claims 1
- 238000006703 hydration reaction Methods 0.000 claims 1
- 238000005984 hydrogenation reaction Methods 0.000 claims 1
- 238000005470 impregnation Methods 0.000 claims 1
- 238000005342 ion exchange Methods 0.000 claims 1
- 238000006317 isomerization reaction Methods 0.000 claims 1
- 239000010687 lubricating oil Substances 0.000 claims 1
- 238000006384 oligomerization reaction Methods 0.000 claims 1
- 230000003647 oxidation Effects 0.000 claims 1
- 238000007254 oxidation reaction Methods 0.000 claims 1
- 238000006116 polymerization reaction Methods 0.000 claims 1
- 238000002203 pretreatment Methods 0.000 claims 1
- 239000000377 silicon dioxide Substances 0.000 claims 1
- 235000019698 starch Nutrition 0.000 claims 1
- 239000008107 starch Substances 0.000 claims 1
- 238000009210 therapy by ultrasound Methods 0.000 claims 1
- 239000012855 volatile organic compound Substances 0.000 claims 1
- 238000002360 preparation method Methods 0.000 abstract 2
- 239000003153 chemical reaction reagent Substances 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
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Classifications
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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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
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Abstract
Изобретение относится к уникальному каталитическому материалу, содержащему цеолит, внедренный в носитель катализатора, и в частности, к микропористому цеолиту, внедренному в мезопористый носитель. Описаны каталитический материал, который включает микропористые цеолиты, нанесенные на мезопористый носитель из неорганического оксида, в котором, по меньшей мере, 97% об. суммарного объема микропор и мезопор составляет объем мезопор; способ получения каталитического материала, включающий предварительную обработку слоистого цеолита, где предварительная обработка включает расслаивание и интеркалирование слоистого цеолита, а также описан способ обработки углеводородного сырья. Технический результат - получение катализатора с идеальным распределением пор по размерам, который способствует транспорту реагентов к активным сайтам катализатора и транспорту продуктов из катализатора, высокая активность и селективность катализатора.
3 н. и 40 з.п. ф-лы, 4 табл., 12 ил.
Description
Claims (43)
1. Способ получения каталитического материала, включающий следующие стадии:
a) предварительная обработка слоистого цеолита;
b) объединение предварительно обработанного слоистого цеолита с водой, неорганическим оксидом или предшественником неорганического оксида и, по меньшей мере, одним органическим соединением, образующим мезопоры, с получением смеси;
c) сушка смеси;
d) нагревание высушенной смеси до температуры и в течение периода времени, достаточных для образования мезопористой структуры неорганического оксида;
где предварительная обработка включает расслаивание или интеркалирование слоистого цеолита.
2. Способ по п.1, где указанное расслаивание проводится контактированием слоистого цеолита со щелочным раствором катионогенного поверхностно-активного вещества в условиях, позволяющих слоистому цеолиту набухать и расслаиваться.
3. Способ по п.1, где расслаивание цеолита включает ультразвуковую обработку цеолита.
4. Способ по п.1, где предварительная обработка включает ионный обмен, импрегнирование, иммобилизацию функциональных производных и/или обработку паром.
5. Способ по п.1, где органическое соединение, образующее мезопоры, выбрано из группы, включающей глицерин, диэтиленгликоль, триэтиленгликоль, тетраэтиленгликоль, пропиленгликоль, триэтаноламин, триизопропаноламин, крахмал, сульфолан, тетраэтиленпентамин и диэтиленгликольдибензоат.
6. Способ по п.1, где температура кипения указанного органического соединения, образующего мезопоры, равна, по меньшей мере, 150°С.
7. Способ по п.1, где неорганический оксид образуется в результате взаимодействия предшественника неорганического оксида с водой.
8. Способ по п.1, где значение pH смеси поддерживают на уровне выше примерно 7,0.
9. Способ по п.2, где смесь подвергают сушке нагреванием на воздухе до температуры и в течение периода времени, достаточных для удаления, по меньшей мере, большей части воды и органического соединения, образующего мезопоры.
10. Способ по п.1, где стадия нагревания (d) включает нагревание высушенной смеси до температуры в интервале от примерно 100 до примерно 250°С.
11. Способ по п.1, дополнительно включающий стадию кальцинирования нагретой высушенной смеси при температуре от примерно 300 до примерно 1000°С в течение периода времени, по меньшей мере, достаточного для удаления органического соединения, образующего мезопоры, из мезопористого неорганического оксидного носителя.
12. Способ по п.1, дополнительно включающий добавление к смеси ионов металлов, где металл выбран из группы, включающей алюминий, титан, ванадий, цирконий, галлий, марганец, цинк, медь, хром, молибден, никель, кобальт и железо.
13. Способ по п.1, дополнительно включающий стадии смешения связующего вещества с каталитическим материалом и формования каталитического материала в предопределенную форму.
14. Способ получения каталитического материала, включающий следующие стадии:
a) контактирование слоистого структурированного цеолита со щелочным раствором катионогенного поверхностно-активного вещества в условиях, позволяющих слоистому цеолиту набухать;
b) объединение набухшего цеолита с водой, неорганическим оксидом или предшественником неорганического оксида и, по меньшей мере, одним органическим соединением, образующим мезопоры, для получения смеси;
c) расслаивание слоистого цеолита;
d) сушка смеси;
e) нагревание высушенной смеси до температуры и в течение периода времени, достаточных для образования мезопористой структуры оксида.
15. Способ по п.14, где указанное органическое соединение, образующее мезопоры, выбрано из группы, включающей глицерин, диэтиленгликоль, триэтиленгликоль, тетраэтиленгликоль, пропиленгликоль, триэтаноламин, триизопропаноламин, сульфолан, тетраэтиленпентамин и диэтиленгликольдибензоат.
16. Способ по п.14, где температура кипения указанного органического соединения, образующего мезопоры, равна, по меньшей мере, 150°С.
17. Способ по п.14, где неорганический оксид образуется в результате взаимодействия предшественника неорганического оксида с водой.
18. Способ по п.17, где предшественник неорганического оксида выбран из группы, включающей источники оксида кремния и источники оксида алюминия.
19. Способ по п.14, где значение pH смеси поддерживают на уровне выше примерно 7,0.
20. Способ по п.14, где смесь сушат нагреванием на воздухе при температуре и в течение периода времени, достаточных для удаления воды и летучих органических соединений.
21. Способ по п.14, где стадия нагревания (е) включает нагревание высушенной смеси до температуры в интервале от примерно 100 до примерно 250°С.
22. Способ по п.14, где стадия нагревания (е) включает нагревание высушенного материала до температуры в интервале от примерно 150 до примерно 200°С.
23. Способ по п.14, дополнительно включающий стадию кальцинирования нагретой высушенной смеси при температуре в интервале от примерно 300 до примерно 1000°С.
24. Способ по п.14, дополнительно включающий стадию кальцинирования нагретой высушенной смеси при температуре в интервале от примерно 400 до примерно 700°С в течение периода от примерно 2 до примерно 40 ч.
25. Способ по п.14, дополнительно включающий объединение ионов металлов со смесью, где металл выбран из группы, включающей алюминий, титан, ванадий, цирконий, галлий, марганец, цинк, медь, хром, молибден, никель, кобальт и железо.
26. Способ по п.14, дополнительно включающий стадии смешения связующего вещества с каталитическим материалом и формование каталитического материала в предопределенную форму.
27. Способ обработки углеводородного сырья, включающий контактирование исходного сырья, содержащего, по меньшей мере, один углеводородный компонент, с каталитически эффективным количеством катализатора, полученного способом по п.14, причем в указанном пористом неорганическом оксиде по меньшей мере 97 об.% общего объема мезопор и микропор пористого неорганического оксида составляет объем мезопор, удельная площадь поверхности составляет примерно от 400 до 1100 м2/г и его рентгенограмма содержит, по меньшей мере, один пик в интервале от 0,3 до 3° в 2θ.
28. Способ по п.27, где превращение углеводородного компонента осуществляют посредством реакции, выбранной из группы, включающей ацилирование, алкилирование, димеризацию, олигомеризацию, полимеризацию, депарафинирование, гидратацию, дегидратацию, диспропорционирование, гидрирование, дегидрирование, ароматизацию, избирательное окисление, изомеризацию, гидрообработку, каталитический крекинг и гидрокрекинг.
29. Способ по п.27, где указанное исходное сырье включает ароматическое соединение и агенты ацилирования и реакция представляет собой реакцию ацилирования, проводимую в условиях реакции ацилирования, достаточных для осуществления ацилирования ароматического соединения с помощью агентов ацилирования.
30. Способ по п.29, где указанные агенты ацилирования включают ангидриды карбоновых кислот, ацилгалогениды.
31. Способ по п.29, где условия реакции ацилирования включают температуру в интервале от примерно 20 до примерно 350°С, давление в интервале от примерно 1 до примерно 110 бар и объемную скорость подачи сырья в интервале от примерно 0,1 до примерно 20 WHSV.
32. Способ по п.27, где указанное исходное сырье включает фракцию нефти и условия реакции достаточны для осуществления каталитического крекинга указанной фракции.
33. Способ по п.32, где указанная фракция нефти включает, по меньшей мере, один компонент с начальной температурой кипения в интервале от примерно 200 до примерно 260°С и конечной температурой кипения в интервале от примерно 400 до примерно 455°С.
34. Способ по п.33, где указанная фракция нефти дополнительно включает, по меньшей мере, один компонент с температурой кипения выше примерно 540°С.
35. Способ по п.34, где компонент с температурой кипения выше 540°С представляет собой недеасфальтированный нефтяной остаток, деасфальтированный нефтяной остаток, битуминозный песок, сланцевое масло или каменноугольную смолу.
36. Способ по п.32, где условия реакции включают температуру от примерно 400 до примерно 650°С и массовое соотношение катализатора и исходного сырья находится в интервале от примерно 3:1 до 10:1.
37. Способ по п.27, где указанное исходное сырье включает фракцию нефти и условия реакции достаточны для осуществления гидрокрекинга фракции для получения относительно более легкого углеводородного продукта.
38. Способ по п.37, где указанная нефтяная фракция содержит, по меньшей мере, один компонент с температурой кипения выше примерно 260°С.
39. Способ по п.37, где указанная нефтяная фракция содержит, по меньшей мере, один компонент с температурой кипения выше примерно 290°С.
40. Способ по п.37, где указанная нефтяная фракция содержит, по меньшей мере, один компонент с температурой кипения выше примерно 340°С.
41. Способ по п.38, где указанная нефтяная фракция дополнительно включает, по меньшей мере, один компонент, выбранный из группы, включающей недеасфальтированный нефтяной остаток, деасфальтированный нефтяной остаток, битуминозный песок, сланцевое масло и каменноугольную смолу.
42. Способ по п.37, где указанный относительно более легкий углеводородный продукт включает компонент, выбранный из группы, включающей компонент газойля с температурой кипения в интервале от 150 до 400°С, дизельное топливо и масло смазочной основы.
43. Способ по п.27, где конверсия углеводородного компонента осуществляется посредством гидроизомеризации и условия реакции включают температуру в интервале от примерно 150 до примерно 500°С, давление в интервале от примерно 1 до примерно 240 бар и WHSV от примерно 0,1 до примерно 20.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2473385C1 (ru) * | 2011-08-25 | 2013-01-27 | Окрытое акционерное общество "Газпромнефть-Омский НПЗ" | Микросферический катализатор для крекинга нефтяных фракций и способ его приготовления |
RU2497589C2 (ru) * | 2008-06-06 | 2013-11-10 | Эни С.П.А. | Способ крекинга и улучшенные катализаторы для осуществления указанного способа |
Families Citing this family (173)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7084087B2 (en) * | 1999-09-07 | 2006-08-01 | Abb Lummus Global Inc. | Zeolite composite, method for making and catalytic application thereof |
US7985400B2 (en) * | 2004-01-26 | 2011-07-26 | Lummus Technology Inc. | Method for making mesoporous or combined mesoporous and microporous inorganic oxides |
US7589041B2 (en) | 2004-04-23 | 2009-09-15 | Massachusetts Institute Of Technology | Mesostructured zeolitic materials, and methods of making and using the same |
CN101035618A (zh) * | 2004-09-07 | 2007-09-12 | Abb路慕斯全球股份有限公司 | 具有沸石和高度中孔性的加氢处理催化剂 |
US7538065B2 (en) * | 2004-09-08 | 2009-05-26 | International Business Machines Corporation | Noble metal-containing catalyst containing a specific ratio of silica to aluminum in the framework |
CN1332761C (zh) * | 2005-07-13 | 2007-08-22 | 清华大学 | 覆载型硅磷铝分子筛的制备方法 |
KR100663111B1 (ko) | 2005-08-23 | 2007-01-02 | 한국과학기술연구원 | 인 이온교환용 메조 기공성 지르코늄 황산염 구조체 및 그제조 방법 |
US8299312B2 (en) * | 2005-10-28 | 2012-10-30 | Neste Oil Oyj | Process for dimerizing olefins |
FR2894851B1 (fr) * | 2005-12-15 | 2009-02-06 | Total France Sa | Composition catalytique et procede de craquage catalytique en lit fluidise utilisant une telle composition |
WO2007083684A1 (ja) * | 2006-01-21 | 2007-07-26 | Tokyo Institute Of Technology | 触媒およびそれを用いるオレフィンの製造方法 |
US7569510B2 (en) * | 2006-02-27 | 2009-08-04 | Philip Morris Usa Inc. | Catalysts to reduce carbon monoxide such as in the mainstream smoke of a cigarette |
WO2007114012A1 (ja) * | 2006-03-31 | 2007-10-11 | Nippon Oil Corporation | 水素化分解触媒および燃料基材の製造方法 |
CN100413784C (zh) * | 2006-04-06 | 2008-08-27 | 辽宁石油化工大学 | 一种y沸石与mapo-5双结构分子筛的合成方法 |
CN100406416C (zh) * | 2006-07-03 | 2008-07-30 | 中国石油化工集团公司 | 一种制取乙烯和丙烯的方法及用于该方法的催化剂 |
CN101134172B (zh) * | 2006-08-31 | 2010-10-27 | 中国石油化工股份有限公司 | 一种烃类转化催化剂 |
EP2073930B1 (en) * | 2006-10-17 | 2021-12-01 | Lummus Technology Inc. | Bimetallic alkylation catalysts |
FR2909012B1 (fr) | 2006-11-23 | 2009-05-08 | Inst Francais Du Petrole | Catalyseur a base d'un materiau a porosite hierarchisee comprenant du silicium et procede d'hydrocraquage/ hydroconversion et d'hydrotraitement de charges hydrocarbonees. |
ES2319007B1 (es) * | 2006-12-07 | 2010-02-16 | Rive Technology, Inc. | Metodos para fabricar materiales zeoliticos mesoestructurados. |
US7919421B2 (en) * | 2006-12-21 | 2011-04-05 | Exxonmobil Chemical Patents Inc. | Catalyst composition, the method of manufacturing and the process of use thereof in aromatics alkylation |
US7381676B1 (en) * | 2007-01-16 | 2008-06-03 | Exxonmobil Chemical Patents Inc. | Catalyst composition and its use thereof in aromatics alkylation |
EP2134815B1 (en) * | 2007-02-09 | 2013-05-01 | Exxonmobil Chemical Patents Inc. A Corporation Of The State Of Delaware | Improved alkylaromatic production process |
EP2517777A3 (en) * | 2007-04-26 | 2013-01-09 | Johnson Matthey Public Limited Company | Transition metal/cha-zeolite scr catalyst |
US7790940B2 (en) * | 2007-06-21 | 2010-09-07 | Exxonmobil Chemical Patents Inc. | Liquid phase alkylation process |
US8816145B2 (en) | 2007-06-21 | 2014-08-26 | Exxonmobil Chemical Patents Inc. | Liquid phase alkylation process |
US20090048094A1 (en) * | 2007-08-13 | 2009-02-19 | Zbigniew Ring | Sulfur-resistant noble metal nano-particles encapsulated in a zeolite cage as a catalyst enhancer |
US7629283B2 (en) * | 2007-10-08 | 2009-12-08 | Uop Llc | Aromatic isomerization catalyst and isomerization process |
US20090093662A1 (en) * | 2007-10-08 | 2009-04-09 | Whitchurch Patrick C | Aromatic isomerization catalyst |
US8206498B2 (en) | 2007-10-25 | 2012-06-26 | Rive Technology, Inc. | Methods of recovery of pore-forming agents for mesostructured materials |
WO2009108166A2 (en) * | 2007-11-05 | 2009-09-03 | Regents Of The University Of Minnesota | Layered zeolite materials and methods related thereto |
CN101514018B (zh) * | 2008-02-20 | 2011-11-30 | 中国石油化工股份有限公司 | Zsm-5/丝光沸石/mcm-56三相共生分子筛及其合成方法 |
WO2009136547A1 (ja) * | 2008-05-07 | 2009-11-12 | 出光興産株式会社 | アダマンタン構造を有する化合物の製造方法 |
WO2010010879A1 (ja) * | 2008-07-23 | 2010-01-28 | 三井化学株式会社 | エチレンのオリゴマー化触媒およびその用途 |
US8653315B2 (en) | 2008-07-30 | 2014-02-18 | King Fahd University Of Petroleum And Minerals | Multiple zeolite catalyst and method of using the same for toluene disproportionation |
US20100029467A1 (en) * | 2008-07-30 | 2010-02-04 | Tomoyuki Inui | Multiple zeolite catalyst |
US8912109B2 (en) * | 2008-12-29 | 2014-12-16 | Fina Technology, Inc. | Catalyst with an ion-modified binder |
US8231778B2 (en) * | 2008-12-31 | 2012-07-31 | Uop Llc | Hydrocracking processes yielding a hydroisomerized product for lube base stocks |
US8524625B2 (en) | 2009-01-19 | 2013-09-03 | Rive Technology, Inc. | Compositions and methods for improving the hydrothermal stability of mesostructured zeolites by rare earth ion exchange |
WO2010083488A2 (en) | 2009-01-19 | 2010-07-22 | Rive Technologies, Inc. | Introduction of mesoporosity in low si/ai zeolites |
CA2760181C (en) * | 2009-04-29 | 2016-12-20 | Pq Corporation | Zeolite y |
PL2440328T3 (pl) | 2009-06-12 | 2017-06-30 | Albemarle Europe Sprl. | Katalizatory z sitem molekularnym sapo, ich otrzymywanie i zastosowania |
EP2272939B1 (en) * | 2009-07-03 | 2012-09-12 | BP Corporation North America Inc. | Alkene oligomerization process |
WO2011041184A2 (en) * | 2009-09-30 | 2011-04-07 | Exxonmobil Chemical Patents Inc. | Production of aromatics from methane |
US8685875B2 (en) | 2009-10-20 | 2014-04-01 | Rive Technology, Inc. | Methods for enhancing the mesoporosity of zeolite-containing materials |
CN102039158B (zh) * | 2009-10-21 | 2012-08-29 | 中国石油化工股份有限公司 | 一种mcm-22/氧化硅复合物的制备方法 |
CN102039200B (zh) * | 2009-10-22 | 2012-07-18 | 中国石油天然气股份有限公司 | 一种Y-Beta/MCM-41双微孔-介孔复合分子筛及制备方法 |
US8212099B2 (en) * | 2009-11-05 | 2012-07-03 | Chevron U.S.A. Inc. | N-paraffin selective hydroconversion process using borosilicate ZSM-48 molecular sieves |
US8142757B2 (en) * | 2009-11-05 | 2012-03-27 | Chevron U.S.A. Inc. | Method for making borosilicate ZSM-48 molecular sieves |
US8685231B2 (en) | 2009-11-27 | 2014-04-01 | Shell Oil Company | Process for conversion of paraffinic feedstock |
TW201139336A (en) * | 2010-02-05 | 2011-11-16 | Fina Technology | Styrene production processes and catalysts for use therein |
JP5468957B2 (ja) * | 2010-03-29 | 2014-04-09 | Jx日鉱日石エネルギー株式会社 | 水素化異性化触媒、その製造方法、炭化水素油の脱蝋方法、炭化水素の製造方法及び潤滑油基油の製造方法 |
WO2011146189A2 (en) | 2010-05-20 | 2011-11-24 | Exxonmobil Chemical Patents Inc. | Improved alkylation process |
US8877669B2 (en) | 2010-08-02 | 2014-11-04 | Basf Corporation | Hydroisomerization catalysts for biological feedstocks |
WO2012030440A1 (en) | 2010-08-30 | 2012-03-08 | Exxonmobil Chemical Patents Inc. | Improved alkylation process |
US8557106B2 (en) * | 2010-09-30 | 2013-10-15 | Exxonmobil Research And Engineering Company | Hydrocracking process selective for improved distillate and improved lube yield and properties |
WO2012050655A2 (en) * | 2010-10-15 | 2012-04-19 | Exxonmobil Chemical Patents Inc. | Selecting an improved catalyst composition and hydrocarbon conversion process using same |
CN101973560B (zh) * | 2010-10-19 | 2012-05-23 | 大连理工大学 | 一种itq-2分子筛的制备方法 |
US8791040B2 (en) | 2010-11-03 | 2014-07-29 | Fina Technology, Inc. | Catalysts containing nano-materials and methods of making and using same |
CN102008976B (zh) * | 2010-11-09 | 2013-07-31 | 中国海洋石油总公司 | 一种脱烯烃催化剂的制备方法 |
US9522390B2 (en) | 2010-12-10 | 2016-12-20 | The Regents Of The University Of California | Oxide materials and synthesis by fluoride/chloride anion promoted exfoliation |
CN102553650B (zh) * | 2010-12-17 | 2013-07-31 | 中国石油天然气股份有限公司 | 一种加氢裂化催化剂载体及其制备方法 |
US8778171B2 (en) | 2011-07-27 | 2014-07-15 | Exxonmobil Research And Engineering Company | Hydrocracking catalysts containing stabilized aggregates of small crystallites of zeolite Y associated hydrocarbon conversion processes |
US8852326B2 (en) | 2011-03-07 | 2014-10-07 | Exxonmobil Research And Engineering Company | Aggregates of small particles of synthetic faujasite zeolite |
US8882993B2 (en) | 2011-03-07 | 2014-11-11 | Exxonmobil Research And Engineering Company | Stabilized aggregates of small crystallites of zeolite Y |
US8778824B2 (en) | 2011-03-07 | 2014-07-15 | Exxonmobil Research And Engineering Company | Aggregates of small crystallites of zeolite Y |
EP2694438A4 (en) * | 2011-04-08 | 2014-11-05 | Rive Technology Inc | MESOPOROUS ZEOLITE WITH MODIFIED FRAME |
JP5750300B2 (ja) * | 2011-04-28 | 2015-07-22 | 日揮触媒化成株式会社 | 新規ヘテロ接合多孔性結晶体の合成方法および新規ヘテロ接合多孔性結晶体 |
CN102910641B (zh) * | 2011-08-01 | 2015-04-01 | 中国石油化工股份有限公司 | 具有规整介孔结构Y-Beta复合分子筛及其合成方法 |
RU2487112C2 (ru) * | 2011-08-22 | 2013-07-10 | Учреждение Российской Академии Наук Институт Нефтехимии И Катализа Ран | СПОСОБ ПОЛУЧЕНИЯ ОЛИГОМЕРОВ ВЫСШИХ ЛИНЕЙНЫХ α-ОЛЕФИНОВ |
RU2473384C1 (ru) * | 2011-08-25 | 2013-01-27 | Открытое акционерное общество "Газпромнефть-Омский НПЗ" | Микросферический бицеолитный катализатор для повышения октанового числа бензина крекинга вакуумного газойля и способ его приготовления |
RU2472586C1 (ru) * | 2011-08-26 | 2013-01-20 | Открытое акционерное общество "Газпромнефть-Омский НПЗ" | Микросферический катализатор для снижения содержания серы в бензине крекинга и способ его приготовления |
KR101701578B1 (ko) | 2011-09-16 | 2017-02-01 | 엑손모빌 케미칼 패턴츠 인코포레이티드 | 개선된 액체상 알킬화 방법 |
US20130172649A1 (en) * | 2011-12-30 | 2013-07-04 | Sivadinarayana Chinta | Supported nano sized zeolite catalyst for alkylation reactions |
US9376324B2 (en) | 2012-01-13 | 2016-06-28 | Rive Technology, Inc. | Introduction of mesoporosity into zeolite materials with sequential acid, surfactant, and base treatment |
CN103930369A (zh) | 2012-01-13 | 2014-07-16 | 瑞弗科技有限公司 | 低硅沸石的中孔隙率的引入 |
WO2013123297A2 (en) * | 2012-02-17 | 2013-08-22 | Kior, Inc. | Catalyst composition with increased bulk active site accessibility for the catalytic thermoconversion of biomass to liquid fuels and chemicals and for upgrading bio-oils |
CN103373888A (zh) * | 2012-04-24 | 2013-10-30 | 中国石油天然气股份有限公司 | 一种磺酸基介孔有机硅催化剂的应用 |
CN102698795B (zh) * | 2012-05-22 | 2014-01-22 | 凯瑞化工股份有限公司 | 一种正丁烯骨架异构化催化剂及其制备方法 |
US20140007493A1 (en) * | 2012-07-06 | 2014-01-09 | Kior, Inc. | Hybrid silica and alumina as catalyst matrix and/or binder in biomass conversion catalysts and bio-oil upgrading |
US9914672B2 (en) | 2012-10-19 | 2018-03-13 | Lummus Technology Inc. | Conversion of alcohols to distillate fuels |
KR101451902B1 (ko) * | 2012-11-26 | 2014-10-22 | 한국과학기술원 | 메조기공을 갖는 mre 구조의 제올라이트 또는 유사 mre 제올라이트 물질 및 그의 제조 방법 |
US8765660B1 (en) | 2013-03-08 | 2014-07-01 | Rive Technology, Inc. | Separation of surfactants from polar solids |
JP6383779B2 (ja) * | 2013-03-13 | 2018-08-29 | ビーエーエスエフ コーポレーション | Fe含有モレキュラーシーブを基材とした水素化異性化触媒 |
WO2014150541A1 (en) * | 2013-03-19 | 2014-09-25 | Fina Technology, Inc. | Method of forming c5 di-olefins |
CN104117388B (zh) * | 2013-04-23 | 2016-06-15 | 上海碧科清洁能源技术有限公司 | 一种sapo-11/zsm-5混合分子筛催化剂及其制备和应用 |
US9795951B2 (en) | 2013-05-31 | 2017-10-24 | Chevron U.S.A. Inc. | Delamination of borosilicate layered zeolite |
EP3016738B1 (en) * | 2013-07-04 | 2019-04-24 | Total Research & Technology Feluy | Catalyst compositions comprising small size molecular sieves crystals deposited on a porous material |
CN103551186B (zh) * | 2013-07-22 | 2015-07-15 | 中国海洋石油总公司 | 一种含复合分子筛的中油型加氢裂化催化剂及其制备方法和应用 |
CN104250010B (zh) * | 2013-07-22 | 2016-08-24 | 中国海洋石油总公司 | 一种含两种改性分子筛的硅铝载体及其制备方法与应用 |
WO2015066539A1 (en) * | 2013-11-01 | 2015-05-07 | Chevron U.S.A. Inc. | Delaminated zeolite catalyzed aromatic alkylation |
US9662640B2 (en) | 2013-12-27 | 2017-05-30 | Rive Technology, Inc. | Introducing mesoporosity into zeolite materials with a modified acid pre-treatment step |
WO2015179735A1 (en) * | 2014-05-22 | 2015-11-26 | Saudi Arabian Oil Company | Framework substituted zeolite catalyst for fluidized catalytic cracking and method for fluidized catalytic cracking |
CN105293521A (zh) * | 2014-07-11 | 2016-02-03 | 中国石油化工股份有限公司 | 制备高堆积密度球状zsm-5沸石的方法 |
CN105582980B (zh) * | 2014-10-22 | 2017-11-24 | 中国石油化工股份有限公司大连石油化工研究院 | 一种低碳烷烃异构化催化剂的制备方法 |
CN105521811B (zh) * | 2014-10-22 | 2017-08-22 | 中国石油化工股份有限公司大连石油化工研究院 | 一种石脑油异构化催化剂的制备方法 |
CN105582983B (zh) * | 2014-10-22 | 2017-10-27 | 中国石油化工股份有限公司 | 一种石蜡烃择型异构化催化剂的制备方法 |
CN105582984B (zh) * | 2014-10-22 | 2017-10-27 | 中国石油化工股份有限公司 | 一种乙苯脱烷基催化剂的制备方法 |
CN105521816B (zh) * | 2014-10-22 | 2017-10-03 | 中国石油化工股份有限公司大连石油化工研究院 | 一种石蜡烃择型异构化催化剂的制备方法 |
CN105582986B (zh) * | 2014-10-22 | 2017-10-27 | 中国石油化工股份有限公司大连石油化工研究院 | 一种c8芳烃异构化催化剂的制备方法 |
EP3230208B1 (en) | 2014-12-11 | 2022-05-18 | W. R. Grace & Co.-Conn. | Preparation of mesoporous zeolites with reduced processing |
ES2574500B1 (es) | 2014-12-17 | 2017-03-31 | Consejo Superior De Investigaciones Científicas (Csic) | Síntesis de la zeolita con la estructura cristalina CHA, procedimiento de síntesis y su uso en aplicaciones catalíticas |
US10626019B2 (en) | 2014-12-30 | 2020-04-21 | W. R. Grace & Co.-Conn. | Methods for preparing zeolites with surfactant-templated mesoporosity and tunable aluminum content |
CN105984876B (zh) * | 2015-01-30 | 2018-06-29 | 中国科学院大连化学物理研究所 | 一种金属改性sapo分子筛的制备方法 |
JP5901817B2 (ja) * | 2015-04-06 | 2016-04-13 | 日揮触媒化成株式会社 | 重質炭化水素油の接触分解、水素化分解触媒用ヘテロ接合多孔性結晶体 |
RU2592548C1 (ru) * | 2015-06-24 | 2016-07-27 | федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Российский государственный университет нефти и газа имени И.М. Губкина" | Способ переработки тяжелого углеводородного сырья |
WO2017070336A1 (en) * | 2015-10-21 | 2017-04-27 | Saudi Arabian Oil Company | Cationic polymers and porous materials |
BR102016026135B1 (pt) * | 2015-11-09 | 2021-09-21 | Shanghai Research Institute Of Petrochemical Technology, Sinopec | Peneira molecular que apresenta a estrutura sfe, processo para sua produção, composição e uso |
WO2017112558A1 (en) * | 2015-12-21 | 2017-06-29 | Exxonmobil Research And Engineering Company | Trim dewaxing of distillate fuel |
JP6733501B2 (ja) * | 2016-01-18 | 2020-08-05 | 東ソー株式会社 | 芳香族化合物製造触媒及び芳香族化合物の製造方法 |
RU2613516C1 (ru) * | 2016-01-29 | 2017-03-16 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Российский государственный университет нефти и газа (национальный исследовательский университет) имени И.М. Губкина" | Способ получения композита на основе микропористого цеолита и мезопористого оксида кремния |
CN107519925B (zh) * | 2016-06-21 | 2019-10-11 | 中国石油天然气股份有限公司 | Y/Sm2O3/SBA-3/ASA复合材料及其制备方法 |
CN107758688B (zh) * | 2016-08-23 | 2020-08-07 | 中国石油化工股份有限公司 | 不同致密性的纳米聚集盘状丝光沸石 |
WO2018071905A1 (en) * | 2016-10-14 | 2018-04-19 | Gevo, Inc. | Conversion of mixtures of c2-c8 olefins to jet fuel and/or diesel fuel in high yield from bio-based alcohols |
CN106582809B (zh) * | 2016-12-22 | 2019-08-30 | 红宝丽集团股份有限公司 | 一种烯烃环氧化催化剂及其制备方法 |
CN108262059A (zh) * | 2016-12-30 | 2018-07-10 | 中国石油天然气股份有限公司 | 一种催化裂化助催化剂 |
US10494574B2 (en) | 2017-02-23 | 2019-12-03 | Saudi Arabian Oil Company | Systems and methods for cracking hydrocarbon streams such as crude oils utilizing catalysts which include zeolite mixtures |
US10526546B2 (en) | 2017-02-23 | 2020-01-07 | Saudi Arabian Oil Company | Systems and methods for cracking hydrocarbon streams utilizing cracking catalysts |
WO2018183009A1 (en) * | 2017-03-29 | 2018-10-04 | Exxonmobil Chemical Patents Inc. | Catalyst compositions and their use in aromatic alkylation processes |
TWI665012B (zh) * | 2017-03-29 | 2019-07-11 | 美商艾克頌美孚化學專利股份有限公司 | 自烴流移除雜質之方法及其於芳族烷基化製程之用途 |
SG11201908901UA (en) | 2017-03-29 | 2019-10-30 | Exxonmobil Chemical Patents Inc | Catalyst compositions and their use in aromatic alkylation processes |
US11230515B2 (en) | 2017-03-29 | 2022-01-25 | Exxonmobil Chemical Patents Inc. | Methods for removing impurities from a hydrocarbon stream and their use in aromatic alkylation processes |
GB201705241D0 (en) * | 2017-03-31 | 2017-05-17 | Johnson Matthey Catalysts (Germany) Gmbh | Catalyst composition |
US10661260B2 (en) * | 2017-06-15 | 2020-05-26 | King Fahd University Of Petroleum And Minerals | Zeolite composite catalysts for conversion of heavy reformate to xylenes |
US11097262B2 (en) | 2017-06-15 | 2021-08-24 | Saudi Arabian Oil Company | Composite hierarchical zeolite catalyst for heavy reformate conversion to xylenes |
PL235544B1 (pl) | 2017-06-28 | 2020-09-07 | Politechnika Krakowska Im Tadeusza Kosciuszki | Sposób otrzymywania katalizatora zeolitowego zawierającego cząstki miedzi lub jej tlenku, zastosowanie ultradźwięków w sposobie wytwarzania katalizatora zeolitowego oraz jego zastosowanie w reakcji selektywnej katalitycznej redukcji SCR |
CN107285972A (zh) * | 2017-07-11 | 2017-10-24 | 江南大学 | 一种从合成气生产芳香族化合物的连续反应工艺 |
US20200368734A1 (en) * | 2017-08-08 | 2020-11-26 | Basf Se | A composition comprising a mixed metal oxide and a molding comprising a zeolitic material having framework type cha and an alkaline earth metal |
CN109420521A (zh) * | 2017-09-04 | 2019-03-05 | 中国科学院大连化学物理研究所 | 一种用于费托合成反应的催化剂及其制备和应用 |
CN109704355A (zh) * | 2017-10-25 | 2019-05-03 | 北京思达安新材料科技有限公司 | 一种多级孔沸石及制备方法 |
CN109701609B (zh) * | 2017-10-26 | 2021-11-30 | 中国石油化工股份有限公司 | Aei复合分子筛催化剂、制备方法及其应用 |
CN109806908A (zh) * | 2017-11-20 | 2019-05-28 | 中国科学院大连化学物理研究所 | 一种生物质基合成气制液体燃料的催化剂及其制备和应用 |
CN107983402B (zh) * | 2017-12-06 | 2020-12-25 | 中国科学院山西煤炭化学研究所 | 一种丙烷芳构化催化剂及制备方法和应用 |
CN109876866B (zh) * | 2017-12-06 | 2022-03-08 | 中国石油化工股份有限公司 | 一种用于芳香醛合成芳香胺的催化剂及其制备方法 |
RU2705574C1 (ru) * | 2018-02-27 | 2019-11-08 | Индийская Нефтяная Корпорация Лимитэд | Каталитическая композиция для превращения алканов в алкены и способ ее получения |
CN108212204B (zh) * | 2018-03-23 | 2021-02-09 | 安徽理工大学 | 一种微波辅助甲烷直接制备高碳烯烃的催化剂及催化工艺 |
CN108579793B (zh) * | 2018-04-17 | 2020-10-20 | 连云港鹏辰特种新材料有限公司 | 一种基于纳米催化剂的高沸点芳烃溶剂的制备方法 |
CN108706607B (zh) * | 2018-07-02 | 2021-12-03 | 南京工业大学 | 一种沸石分子筛、制备方法及其应用 |
WO2020018449A1 (en) | 2018-07-16 | 2020-01-23 | Battelle Energy Alliance, Llc | Composite media for non-oxidative ethane dehydrogenation, and related ethane activation systems and method of processing an ethane-containing stream |
CN110759357B (zh) * | 2018-07-25 | 2021-08-27 | 中国石油天然气股份有限公司 | 一种zsm-35/zsm-5共晶分子筛的合成方法 |
EP3841064A1 (en) | 2018-08-24 | 2021-06-30 | UMICORE AG & Co. KG | Method for the preparation of a molecular sieve of the cha-type |
US10807078B2 (en) * | 2018-11-19 | 2020-10-20 | Saudi Arabian Oil Company | Method of synthesis of nano-sized beta zeolites containing mesopores and uses thereof |
CN110156554B (zh) * | 2019-05-21 | 2020-09-11 | 浙江大学 | 一种促进烃类原料热裂解的方法 |
CN110127718A (zh) * | 2019-05-28 | 2019-08-16 | 华东师范大学 | 一种zsm-35/zsm-5复合分子筛及其制备方法 |
RU2707179C1 (ru) * | 2019-08-02 | 2019-11-25 | федеральное государственное автономное образовательное учреждение высшего образования "Российский государственный университет нефти и газа (национальный исследовательский университет) имени И.М. Губкина" | Бицеолитный катализатор изомеризации ароматических углеводородов с-8 |
CN112320815B (zh) * | 2019-08-05 | 2023-05-30 | 中国石油化工股份有限公司 | 巯基功能化mcm分子筛的制备方法和应用 |
CN112934258B (zh) * | 2019-11-26 | 2023-10-13 | 国家能源投资集团有限责任公司 | 复合分子筛及其制备方法和加氢异构催化剂及费托合成油加氢异构的方法 |
US11185850B2 (en) | 2019-12-02 | 2021-11-30 | Saudi Arabian Oil Company | Dual functional composite catalyst for olefin metathesis and cracking |
US11078431B2 (en) | 2019-12-16 | 2021-08-03 | Saudi Arabian Oil Company | Modified ultra-stable Y (USY) zeolite catalyst for deolefinization of hydrocarbon streams |
US10981160B1 (en) | 2019-12-19 | 2021-04-20 | Saudi Arabian Oil Company | Composite hierarchical zeolite catalyst for heavy reformate conversion to xylenes |
US11098256B2 (en) | 2020-01-08 | 2021-08-24 | Saudi Arabian Oil Company | Modified ultra-stable Y (USY) zeolite catalyst for improving cold flow properties of distillates |
US20230167041A1 (en) * | 2020-02-18 | 2023-06-01 | Symrise Ag | Method for producing limonene and composition containing limonene |
US11446645B2 (en) | 2020-07-02 | 2022-09-20 | Saudi Arabian Oil Company | FCC catalyst compositions for fluid catalytic cracking and methods of using the FCC catalyst compositions |
US11213810B1 (en) | 2020-07-06 | 2022-01-04 | Saudi Arabian Oil Company | Method of producing a cracking catalyst |
US11278873B2 (en) | 2020-07-16 | 2022-03-22 | Saudi Arabian Oil Company | Method of producing an aromatization catalyst |
US11332678B2 (en) | 2020-07-23 | 2022-05-17 | Saudi Arabian Oil Company | Processing of paraffinic naphtha with modified USY zeolite dehydrogenation catalyst |
US11274068B2 (en) | 2020-07-23 | 2022-03-15 | Saudi Arabian Oil Company | Process for interconversion of olefins with modified beta zeolite |
US11420192B2 (en) | 2020-07-28 | 2022-08-23 | Saudi Arabian Oil Company | Hydrocracking catalysts containing rare earth containing post-modified USY zeolite, method for preparing hydrocracking catalysts, and methods for hydrocracking hydrocarbon oil with hydrocracking catalysts |
US11154845B1 (en) | 2020-07-28 | 2021-10-26 | Saudi Arabian Oil Company | Hydrocracking catalysts containing USY and beta zeolites for hydrocarbon oil and method for hydrocracking hydrocarbon oil with hydrocracking catalysts |
CN112023919B (zh) * | 2020-07-30 | 2022-07-08 | 浙江恒逸石化研究院有限公司 | 用于制备高顺反比2,2,4,4-四甲基-1,3-环丁二醇的催化剂、装置及方法 |
US11142703B1 (en) | 2020-08-05 | 2021-10-12 | Saudi Arabian Oil Company | Fluid catalytic cracking with catalyst system containing modified beta zeolite additive |
CN114073930A (zh) * | 2020-08-19 | 2022-02-22 | 同济大学 | 一种沸石/介孔二氧化硅复合微球材料及制备方法 |
US11484869B2 (en) | 2020-12-09 | 2022-11-01 | Saudi Arabian Oil Company | Modified ultra-stable Y (USY) zeolite catalyst for dealkylation of aromatics |
CN112843766B (zh) * | 2020-12-29 | 2022-06-14 | 复榆(张家港)新材料科技有限公司 | 变压吸附分离溶剂水二元共沸物的吸附分离工艺 |
KR20230160252A (ko) * | 2021-03-29 | 2023-11-23 | 셰브런 유.에스.에이.인크. | 방향족 및 시클로파라핀 고리를 포함하는 탄화수소 종에 대한 개환 공정 및 촉매 |
CN113751056B (zh) * | 2021-10-15 | 2022-07-26 | 河南大学 | 用于催化烃类裂解制取丙烯的分子筛催化剂及其制备方法和用途 |
CN116062766B (zh) * | 2021-10-29 | 2024-05-07 | 中国石油化工股份有限公司 | 一种改性zsm-5分子筛及其制备方法和应用 |
KR102641139B1 (ko) * | 2021-11-12 | 2024-02-27 | 한국화학연구원 | 휘발성 유기화합물 흡착-산화용 제올라이트 복합체 제조방법 |
CN113967538A (zh) * | 2021-11-30 | 2022-01-25 | 郑州轻工业大学 | 一种有机烟雾多污染物深度净化装置及应用 |
US11618858B1 (en) | 2021-12-06 | 2023-04-04 | Saudi Arabian Oil Company | Hydrodearylation catalysts for aromatic bottoms oil, method for producing hydrodearylation catalysts, and method for hydrodearylating aromatic bottoms oil with hydrodearylation catalysts |
CN114917865B (zh) * | 2022-06-06 | 2023-08-22 | 中海油天津化工研究设计院有限公司 | 一种芳烃吸附剂及其在增产乙烯裂解原料中的应用 |
US11725149B1 (en) | 2022-06-13 | 2023-08-15 | Saudi Arabian Oil Company | Fluidized catalytic cracking processes and additives for improving gasoline yield and quality |
CN115532307B (zh) * | 2022-09-28 | 2023-09-01 | 河北工业大学 | 一种多级孔分子筛负载金属氧化物复合材料及其制备方法和应用 |
CN115650251B (zh) * | 2022-11-02 | 2024-02-02 | 吉林大学 | 一种mor沸石分子筛整料及其制备方法和应用 |
CN115970750A (zh) * | 2022-11-30 | 2023-04-18 | 嘉庚创新实验室 | 一种沸石分子筛基催化剂及其制备方法,以及油脂一步加氢异构制备生物基柴油的方法 |
Family Cites Families (59)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2073294A (en) * | 1935-01-17 | 1937-03-09 | Caillau Marcel Urbain | Hose clamp |
US3912920A (en) * | 1974-02-06 | 1975-10-14 | Josuke Kubota | Polarized light illumination device |
US4963448A (en) * | 1987-08-31 | 1990-10-16 | Agency Of Industrial Science & Technology | Photorecording element and liquid crystal cell comprising the same |
US4988659A (en) * | 1988-11-23 | 1991-01-29 | Chevron Research Company | Silica/alumina cogel catalysts |
US4974941A (en) * | 1989-03-08 | 1990-12-04 | Hercules Incorporated | Process of aligning and realigning liquid crystal media |
US4899659A (en) * | 1989-06-30 | 1990-02-13 | The United States Of America As Represented By The Secretary Of The Navy | Safe and arm device |
JPH0336527A (ja) * | 1989-07-03 | 1991-02-18 | Agency Of Ind Science & Technol | 光学素子 |
US5102643A (en) | 1990-01-25 | 1992-04-07 | Mobil Oil Corp. | Composition of synthetic porous crystalline material, its synthesis |
US5110572A (en) | 1990-01-25 | 1992-05-05 | Mobil Oil Corp. | Synthesis of mesoporous crystalline material using organometallic reactants |
US5264203A (en) | 1990-01-25 | 1993-11-23 | Mobil Oil Corporation | Synthetic mesoporous crystalline materials |
US5108725A (en) | 1990-01-25 | 1992-04-28 | Mobil Oil Corp. | Synthesis of mesoporous crystalline material |
US5057296A (en) | 1990-12-10 | 1991-10-15 | Mobil Oil Corp. | Method for synthesizing mesoporous crystalline material |
US5021178A (en) * | 1990-02-07 | 1991-06-04 | Mobil Oil Corporation | Acylation of lower olefin oligomers |
GB9013859D0 (en) * | 1990-06-21 | 1990-08-15 | Ici Plc | Zeolites |
EP0492216B1 (de) * | 1990-12-21 | 1995-10-11 | F. Hoffmann-La Roche Ag | Optisch nichtlineare Polymerschichten |
US5191148A (en) | 1991-05-06 | 1993-03-02 | Mobil Oil Corporation | Isoparaffin/olefin alkylation |
US5191134A (en) | 1991-07-18 | 1993-03-02 | Mobil Oil Corporation | Aromatics alkylation process |
EP0525477B1 (de) * | 1991-07-26 | 1998-09-16 | Rolic AG | Orientierte Photopolymere und Verfahren zu ihrer Herstellung |
EP0525473B1 (de) * | 1991-07-26 | 1998-05-06 | Rolic AG | Flüssigkristall-Zelle |
US5221648A (en) * | 1991-12-30 | 1993-06-22 | Exxon Research & Engineering Company | Highly attrition resistant mesoporous catalytic cracking catalysts |
US5453862A (en) * | 1992-09-04 | 1995-09-26 | Stanley Electric Co., Ltd. | Rubbing-free (chiral) nematic liquid crystal display |
JP2572537B2 (ja) * | 1993-02-10 | 1997-01-16 | スタンレー電気株式会社 | 液晶表示装置とその製造方法 |
DE59403063D1 (de) * | 1993-02-17 | 1997-07-17 | Hoffmann La Roche | Optisches Bauelement |
US5539074A (en) * | 1993-02-17 | 1996-07-23 | Hoffmann-La Roche Inc. | Linear and cyclic polymers or oligomers having a photoreactive ethene group |
JP2777056B2 (ja) * | 1993-05-20 | 1998-07-16 | エルジー電子株式会社 | 液晶セルの配向物質 |
JP2693368B2 (ja) * | 1993-06-29 | 1997-12-24 | スタンレー電気株式会社 | 液晶表示素子とその製造方法 |
US5601798A (en) * | 1993-09-07 | 1997-02-11 | Pq Corporation | Process for preparing zeolite Y with increased mesopore volume |
KR970000356B1 (ko) * | 1993-09-18 | 1997-01-08 | 엘지전자 주식회사 | 액정표시소자(lcd)용 광 폴리머 배향막 형성방법 |
EP0688443B1 (en) * | 1994-01-10 | 2002-09-25 | Honeywell Inc. | Multi-domain color filter substrate |
US5712696A (en) * | 1994-02-17 | 1998-01-27 | Stanley Electric, Co., Ltd. | Manufacture of LCD device by transferring the orientation state from a parent substrate to a child substrate |
JP3075917B2 (ja) * | 1994-05-27 | 2000-08-14 | シャープ株式会社 | 液晶表示装置、その製造方法およびその製造装置 |
IT1270230B (it) * | 1994-06-16 | 1997-04-29 | Enichem Sintesi | Composizione catalitica e processo per l'alchilazione di composti aromatici |
US5840264A (en) | 1994-08-22 | 1998-11-24 | Board Of Trustees Operating Michigan State University | Crystalline inorganic oxide compositions prepared by neutral templating route |
JP2708382B2 (ja) * | 1994-10-14 | 1998-02-04 | インターナショナル・ビジネス・マシーンズ・コーポレイション | 液晶表示装置用基板の製造方法、液晶表示装置の製造方法及び液晶表示装置 |
US5578351A (en) * | 1995-01-20 | 1996-11-26 | Geo-Centers, Inc. | Liquid crystal composition and alignment layer |
JP3599815B2 (ja) * | 1995-03-15 | 2004-12-08 | アルプス電気株式会社 | 紫外線架橋化合物、液晶表示素子用配向膜及び液晶表示素子 |
US5786041A (en) * | 1995-06-07 | 1998-07-28 | International Business Machines Corporation | Alignment film, a method for producing the alignment film and a liquid crystal display device using the alignment film |
GB9519860D0 (en) * | 1995-09-29 | 1995-11-29 | Secr Defence | Polymers for liquid crystal alignment |
JPH09127525A (ja) * | 1995-11-06 | 1997-05-16 | Sharp Corp | 液晶表示素子およびその製造方法 |
KR0179115B1 (ko) * | 1995-11-20 | 1999-05-01 | 구자홍 | 액정배향용 감광성물질 및 이를 이용한 액정표시장치 |
US5853566A (en) * | 1995-11-28 | 1998-12-29 | Shell Oil Company | Zeolite-beta containing catalyst compositions and their use in hydrocarbon conversion processes for producing low boiling point materials |
KR0181782B1 (ko) * | 1995-12-08 | 1999-05-01 | 구자홍 | 광을 이용한 벤드배향된 액정셀 제조방법 |
KR0169016B1 (ko) * | 1995-12-29 | 1999-03-20 | 구자홍 | 광을 이용한 트위스트네메틱 액정셀 제조방법 |
US5889571A (en) * | 1996-02-01 | 1999-03-30 | Lg Electronics Inc. | Ultraviolet irradiating device for photo-alignment process and an irradiating method using the same |
US5731405A (en) * | 1996-03-29 | 1998-03-24 | Alliant Techsystems Inc. | Process and materials for inducing pre-tilt in liquid crystals and liquid crystal displays |
US5849258A (en) * | 1996-06-06 | 1998-12-15 | Intevep, S.A. | Material with microporous crystalline walls defining a narrow size distribution of mesopores, and process for preparing same |
KR100247137B1 (ko) * | 1996-07-29 | 2000-03-15 | 구본준 | 멀티도메인 액정셀의 제조방법 |
KR100191787B1 (ko) * | 1996-09-20 | 1999-06-15 | 구자홍 | 광시야각을 가지는 액정셀의 제조방법 |
KR100201841B1 (ko) * | 1996-11-29 | 1999-06-15 | 구자홍 | 액정셀 제조방법 |
IT1290846B1 (it) | 1996-12-12 | 1998-12-14 | Enichem Spa | Composizione catalitica e processo per l'alchilazione e/o la transalchilazione di composti aromatici |
US6133186A (en) | 1997-03-06 | 2000-10-17 | Shell Oil Company | Process for the preparation of a catalyst composition |
US6814950B1 (en) * | 1999-09-07 | 2004-11-09 | Abb Lummus Global Inc. | Inorganic oxides with mesoporosity or combined meso-and microporosity and process for the preparation thereof |
US7084087B2 (en) * | 1999-09-07 | 2006-08-01 | Abb Lummus Global Inc. | Zeolite composite, method for making and catalytic application thereof |
US6762143B2 (en) | 1999-09-07 | 2004-07-13 | Abb Lummus Global Inc. | Catalyst containing microporous zeolite in mesoporous support |
CN100509623C (zh) * | 1999-09-07 | 2009-07-08 | 代尔夫特科技大学 | 具有中孔或复合的中孔和微孔的无机氧化物及其制备方法 |
CA2385328C (en) | 1999-09-20 | 2009-10-13 | Consejo Superior De Investigaciones Cientificas | Aromatics alkylation |
FR2802120B1 (fr) * | 1999-12-14 | 2002-02-01 | Inst Francais Du Petrole | Solide silicoaluminate micro et mesoporeux, procede de preparation, utilisation comme catalyseur et en conversion d'hydrocarbures |
US6346140B2 (en) | 2000-03-31 | 2002-02-12 | Kabushiki Kaisha Toyota Chuo Kenkyusho | Porous solid for gas adsorption separation and gas adsorption separation process employing it |
US6843977B2 (en) | 2000-05-25 | 2005-01-18 | Board Of Trustees Of Michigan State University | Ultrastable porous aluminosilicate structures and compositions derived therefrom |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2497589C2 (ru) * | 2008-06-06 | 2013-11-10 | Эни С.П.А. | Способ крекинга и улучшенные катализаторы для осуществления указанного способа |
RU2473385C1 (ru) * | 2011-08-25 | 2013-01-27 | Окрытое акционерное общество "Газпромнефть-Омский НПЗ" | Микросферический катализатор для крекинга нефтяных фракций и способ его приготовления |
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US20060128555A1 (en) | 2006-06-15 |
TW200528189A (en) | 2005-09-01 |
ZA200603144B (en) | 2007-04-25 |
AU2010200214B2 (en) | 2011-02-10 |
US20060264318A1 (en) | 2006-11-23 |
AU2010200214B8 (en) | 2011-06-09 |
RU2006117333A (ru) | 2007-11-27 |
US7550405B2 (en) | 2009-06-23 |
WO2005042148A1 (en) | 2005-05-12 |
AU2004285859B2 (en) | 2010-02-25 |
AU2004285859A1 (en) | 2005-05-12 |
AU2010200214A1 (en) | 2010-10-21 |
AU2010200213A1 (en) | 2010-10-21 |
AU2010200214A8 (en) | 2011-06-09 |
AR075385A2 (es) | 2011-03-30 |
AU2010200213B2 (en) | 2012-02-23 |
KR20070004530A (ko) | 2007-01-09 |
AR046556A1 (es) | 2005-12-14 |
US20040138051A1 (en) | 2004-07-15 |
US7470645B2 (en) | 2008-12-30 |
EP1677909A1 (en) | 2006-07-12 |
BRPI0415621A (pt) | 2006-12-12 |
JP2007508935A (ja) | 2007-04-12 |
US7084087B2 (en) | 2006-08-01 |
AR075800A2 (es) | 2011-04-27 |
CN1871065A (zh) | 2006-11-29 |
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