RU2006140090A - Твердый кислотный катализатор и способ его применения - Google Patents
Твердый кислотный катализатор и способ его применения Download PDFInfo
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- RU2006140090A RU2006140090A RU2006140090/04A RU2006140090A RU2006140090A RU 2006140090 A RU2006140090 A RU 2006140090A RU 2006140090/04 A RU2006140090/04 A RU 2006140090/04A RU 2006140090 A RU2006140090 A RU 2006140090A RU 2006140090 A RU2006140090 A RU 2006140090A
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- Prior art keywords
- composition according
- catalytic composition
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- oxide
- catalyst
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- 238000000034 method Methods 0.000 title claims 8
- 239000003054 catalyst Substances 0.000 title claims 6
- 239000011973 solid acid Substances 0.000 title 1
- 230000003197 catalytic effect Effects 0.000 claims 17
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims 9
- 238000006243 chemical reaction Methods 0.000 claims 6
- 229940075614 colloidal silicon dioxide Drugs 0.000 claims 5
- 239000000126 substance Substances 0.000 claims 5
- 150000002927 oxygen compounds Chemical class 0.000 claims 4
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 claims 4
- 230000000737 periodic effect Effects 0.000 claims 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims 4
- 229910001928 zirconium oxide Inorganic materials 0.000 claims 4
- 239000004215 Carbon black (E152) Substances 0.000 claims 3
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 claims 3
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 claims 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims 3
- 229930195733 hydrocarbon Natural products 0.000 claims 3
- 150000002430 hydrocarbons Chemical class 0.000 claims 3
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims 2
- 229910052782 aluminium Inorganic materials 0.000 claims 2
- -1 aluminum compound Chemical class 0.000 claims 2
- 239000008119 colloidal silica Substances 0.000 claims 2
- DIOQZVSQGTUSAI-UHFFFAOYSA-N decane Chemical compound CCCCCCCCCC DIOQZVSQGTUSAI-UHFFFAOYSA-N 0.000 claims 2
- 238000006317 isomerization reaction Methods 0.000 claims 2
- 229910052751 metal Inorganic materials 0.000 claims 2
- 239000002184 metal Substances 0.000 claims 2
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims 2
- BKIMMITUMNQMOS-UHFFFAOYSA-N nonane Chemical compound CCCCCCCCC BKIMMITUMNQMOS-UHFFFAOYSA-N 0.000 claims 2
- QGLKJKCYBOYXKC-UHFFFAOYSA-N nonaoxidotritungsten Chemical compound O=[W]1(=O)O[W](=O)(=O)O[W](=O)(=O)O1 QGLKJKCYBOYXKC-UHFFFAOYSA-N 0.000 claims 2
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 claims 2
- 239000002245 particle Substances 0.000 claims 2
- 229910052697 platinum Inorganic materials 0.000 claims 2
- 229910001930 tungsten oxide Inorganic materials 0.000 claims 2
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 claims 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical group [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical group [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 claims 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 claims 1
- 230000029936 alkylation Effects 0.000 claims 1
- 238000003442 catalytic alkylation reaction Methods 0.000 claims 1
- 238000004523 catalytic cracking Methods 0.000 claims 1
- 229910052750 molybdenum Inorganic materials 0.000 claims 1
- 239000011733 molybdenum Substances 0.000 claims 1
- 229910000476 molybdenum oxide Inorganic materials 0.000 claims 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims 1
- PQQKPALAQIIWST-UHFFFAOYSA-N oxomolybdenum Chemical compound [Mo]=O PQQKPALAQIIWST-UHFFFAOYSA-N 0.000 claims 1
- 229910052763 palladium Inorganic materials 0.000 claims 1
- 239000000377 silicon dioxide Substances 0.000 claims 1
- XOLBLPGZBRYERU-UHFFFAOYSA-N tin dioxide Chemical compound O=[Sn]=O XOLBLPGZBRYERU-UHFFFAOYSA-N 0.000 claims 1
- 229910001887 tin oxide Inorganic materials 0.000 claims 1
- 239000010936 titanium Substances 0.000 claims 1
- 229910052719 titanium Inorganic materials 0.000 claims 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims 1
- 238000010555 transalkylation reaction Methods 0.000 claims 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims 1
- 229910052721 tungsten Inorganic materials 0.000 claims 1
- 239000010937 tungsten Substances 0.000 claims 1
- 229910052726 zirconium Inorganic materials 0.000 claims 1
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- B01J23/56—Platinum group metals
- B01J23/64—Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/652—Chromium, molybdenum or tungsten
- B01J23/6527—Tungsten
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- C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
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- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
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- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
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- C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
- C10G49/02—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used
- C10G49/04—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used containing nickel, cobalt, chromium, molybdenum, or tungsten metals, or compounds thereof
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- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
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- B01J21/063—Titanium; Oxides or hydroxides thereof
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- 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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Claims (22)
1. Каталитическая композиция, содержащая
а) кислородное соединение элемента, выбранного из группы IVB или группы IVA Периодической системы элементов;
b) кислородное соединение элемента, выбранного из группы VIB или группы VIA Периодической системы элементов; и
с) не менее примерно 1 мас.% частиц коллоидального диоксида кремния по отношению к общей массе катализатора.
2. Каталитическая композиция по п.1, в которой коллоидальный диоксид кремния составляет не менее примерно 5 мас.% общей массы катализатора.
3. Каталитическая композиция по п.1, дополнительно включающая соединение алюминия.
4. Каталитическая композиция по п.3, в которой соединением алюминия является оксид алюминия.
5. Каталитическая композиция по п.1, дополнительно включающая металл группы VIII.
6. Каталитическая композиция по п.5, в которой металл группы VIII выбран из платины и палладия.
7. Каталитическая композиция по п.1, в которой элементом группы IVB является олово.
8. Каталитическая композиция по п.1, в которой элемент группы IVA выбран из группы, состоящей из титана и циркония.
9. Каталитическая композиция по п.1, в которой элементом группы VIB является молибден или вольфрам.
10. Каталитическая композиция по п.1, содержащая оксид вольфрама и оксид циркония.
11. Каталитическая композиция по п.1, содержащая оксид молибдена и оксид циркония.
12. Каталитическая композиция по п.1, содержащая сульфат и оксид циркония.
13. Каталитическая композиция по п.1, содержащая сульфат и оксид титана.
14. Каталитическая композиция по п.1, содержащая сульфат и оксид олова.
15. Каталитическая композиция по п.1, в которой коллоидальный диоксид кремния смешивают с коллоидным диоксидом кремния.
16. Каталитическая композиция по п.1, в которой коллоидальный диоксид кремния смешивают с глиноземом.
17. Каталитическая композиция по п.1, в которой коллоидальный диоксид кремния смешивается с осажденным диоксидом кремния.
18. Способ химической конверсии углеводорода, включающий взаимодействие углеводорода в условиях реакции химической конверсии с каталитической композицией, которая содержит
i) кислородное соединение элемента, выбранного из группы IVB или группы IVA Периодической системы элементов;
ii) кислородное соединение элемента, выбранного из группы VIB или группы VIA Периодической системы элементов; и
iii) не менее примерно 1 мас.% частиц коллоидального диоксида кремния по отношению к общей массе катализатора.
19. Способ по п.18, в котором способ химической конверсии выбран из группы, состоящей из изомеризации, каталитического крекинга, алкилирования и трансалкилирования.
20. Способ по п.19, в котором способ химической конверсии представляет собой изомеризацию, и условия химической конверсии включают температуру от примерно 93°C до примерно 425°C, давление от примерно 1 фунт/кв.дюйм до примерно 1000 фунт/кв.дюйм и LHSV от примерно 0,1 до примерно 10.
21. Способ по п.20, в котором углеводород выбран из группы, состоящей из н-бутана, н-пентана, н-гексана, циклогексана, н-гептана, н-октана, н-нонана и н-декана.
22. Способ по п.21, в котором каталитическая композиция содержит оксид вольфрама, оксид циркония, оксид алюминия и платину.
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US10/824,390 US7304199B2 (en) | 2004-04-14 | 2004-04-14 | Solid acid catalyst and method of using same |
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CN (2) | CN1968747B (ru) |
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KR100931792B1 (ko) | 2007-05-25 | 2009-12-11 | 주식회사 엘지화학 | 탄화수소 수증기 열분해용 촉매, 그의 제조방법 및 이를이용한 올레핀의 제조방법 |
KR100999304B1 (ko) * | 2007-07-05 | 2010-12-08 | 주식회사 엘지화학 | 올레핀 제조용 탄화수소 열분해 방법 |
US8105969B2 (en) * | 2008-12-29 | 2012-01-31 | Fina Technology Inc. | Catalyst with an ion-modified binder |
US8067658B2 (en) * | 2009-01-23 | 2011-11-29 | Conocophillips Company | Isomerization process |
US8426666B2 (en) * | 2009-02-17 | 2013-04-23 | Phillips 66 Company | Isomerization of wet hexanes |
US7659438B1 (en) | 2009-02-17 | 2010-02-09 | Conocophillips Company | Isomerization of wet hexanes |
US20110301021A1 (en) * | 2009-03-02 | 2011-12-08 | Sud-Chemie Inc. | Promoted zirconium oxide catalyst support |
US8153548B2 (en) | 2010-04-19 | 2012-04-10 | King Fahd University Of Petroleum & Minerals | Isomerization catalyst |
US20130079578A1 (en) * | 2011-09-23 | 2013-03-28 | Cpc Corporation | Modified Zirconia Catalysts and Associated Methods Thereof |
RU2470000C1 (ru) * | 2012-05-29 | 2012-12-20 | Открытое акционерное общество "Научно-производственное предприятие Нефтехим" (ОАО "НПП Нефтехим") | Способ изомеризации парафиновых углеводородов c4-c7 |
EP2801564A1 (de) | 2013-05-06 | 2014-11-12 | LANXESS Deutschland GmbH | Decarboxylirung von 6-Methylsalicylsäure |
CN106140197B (zh) * | 2015-03-24 | 2019-03-12 | 中国石油天然气股份有限公司 | 固体超强酸催化剂及其制备方法及轻质正构烷烃的异构化方法 |
RU2595341C1 (ru) * | 2015-06-29 | 2016-08-27 | Акционерное общество "Специальное конструкторско-технологическое бюро "Катализатор" | Катализатор изомеризации парафиновых углеводородов и способ его приготовления |
CN106215969B (zh) * | 2016-07-25 | 2018-08-21 | 江苏大学 | 一种铈掺杂固体超强酸催化剂及其制备方法 |
JP2019027765A (ja) * | 2017-08-04 | 2019-02-21 | 日立アプライアンス株式会社 | 冷蔵庫 |
WO2020060888A2 (en) | 2018-09-17 | 2020-03-26 | Chevron Phillips Chemical Company Lp | Modified supported chromium catalysts and ethylene-based polymers produced therefrom |
EP4031518A1 (en) | 2019-09-16 | 2022-07-27 | Chevron Phillips Chemical Company LP | Chromium-catalyzed production of alcohols from hydrocarbons |
EP4031279A1 (en) | 2019-09-16 | 2022-07-27 | Chevron Phillips Chemical Company Lp | Chromium-based catalysts and processes for converting alkanes into higher and lower aliphatic hydrocarbons |
CN113731435B (zh) * | 2020-05-27 | 2023-10-10 | 中国石油化工股份有限公司 | 一种降烯烃脱硫催化剂及其制备方法和烃油脱硫方法 |
CN113731436B (zh) * | 2020-05-27 | 2023-10-13 | 中国石油化工股份有限公司 | 一种具有芳构化功能的脱硫催化剂及其制备方法和烃油脱硫方法 |
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JP4675956B2 (ja) | 2011-04-27 |
RU2338589C2 (ru) | 2008-11-20 |
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US7304199B2 (en) | 2007-12-04 |
CN1968747B (zh) | 2011-08-24 |
CN1968747A (zh) | 2007-05-23 |
EP1735092A1 (en) | 2006-12-27 |
CA2560339A1 (en) | 2005-10-27 |
KR101114242B1 (ko) | 2012-04-16 |
US20050234283A1 (en) | 2005-10-20 |
JP2007532307A (ja) | 2007-11-15 |
CA2560339C (en) | 2011-11-29 |
CN101797503A (zh) | 2010-08-11 |
BRPI0508644B1 (pt) | 2014-10-14 |
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WO2005099896A1 (en) | 2005-10-27 |
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