RU2006132349A - Конверсия углеводородов с применением нанокристаллического цеолита y - Google Patents

Конверсия углеводородов с применением нанокристаллического цеолита y Download PDF

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RU2006132349A
RU2006132349A RU2006132349/04A RU2006132349A RU2006132349A RU 2006132349 A RU2006132349 A RU 2006132349A RU 2006132349/04 A RU2006132349/04 A RU 2006132349/04A RU 2006132349 A RU2006132349 A RU 2006132349A RU 2006132349 A RU2006132349 A RU 2006132349A
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zeolite
alkylation
approximately
alkylated
catalyst
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RU2006132349/04A
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RU2327520C1 (ru
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Синтао ГАО (US)
Синтао ГАО
Йоханнес Хендрик КЕГЛЕР (US)
Йоханнес Хендрик КЕГЛЕР
Лоренс Л. МЕРРЕЛЛ (US)
Лоренс Л. МЕРРЕЛЛ
Филип Дж. ЭНДЖИВАЙН (US)
Филип Дж. ЭНДЖИВАЙН
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Абб Ламмус Глобал Инк. (Us)
Абб Ламмус Глобал Инк.
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Claims (22)

1. Способ алкилирования углеводородного соединения, включающий a) получение катализатора, содержащего цеолит Y с размером кристалла не более 100 нм; b) осуществление взаимодействия алкилируемого углеводорода с алкилирующим агентом в присутствии указанного катализатора в условиях реакции алкилирования, приводящих к алкилированному продукту.
2. Способ по п.1, где способ алкилирования представляет собой способ алкилирования олефин/парафин.
3. Способ по п.2, где алкилируемым углеводородом является изобутан и алкилирующим агентом является бутен.
4. Способ по п.3, где алкилированный продукт включает бензин с октановым числом по исследовательскому методу, равным, по меньшей мере, 99,5.
5. Способ по п.1, где способ алкилирования представляет собой ароматическое алкилирование.
6. Способ по п.5, где алкилируемым углеводородом является бензол и алкилирующий агент выбирают из группы, включающей этилен, пропилен, 1-бутен, 2-бутен и изобутен.
7. Способ по п.1, где способ алкилирования включает переалкилирование, алкилируемым углеводородом является ароматическое соединение с "голым" циклом и алкилирующим агентом является полиалкилированное ароматическое соединение.
8. Способ по п.7, где ароматическим соединением с "голым" циклом является бензол и полиалкилированное ароматическое соединение выбирают из группы, включающей диэтилбензол и диизопропилбензол.
9. Способ по п.1, где стадия получения катализатора включает a) получение пористого неорганического оксида, b) пропитку пористого неорганического оксида жидким раствором, содержащим неорганический формирующий микропоры направляющий агент, обеспечивающий гидроксид-ионы, где количество жидкого раствора не превышает 100% от объема пор неорганического оксида и концентрация формирующего микропоры направляющего агента в жидком растворе изменяется в диапазоне приблизительно от 25 до 60 мас.%, и c) нагревание пропитанного пористого неорганического оксида при повышенных температурах синтеза на протяжении времени, достаточного для формирования содержащего цеолит продукта.
10. Способ по п.9, где жидкий раствор неорганического формирующего микропоры направляющего агента представляет собой водный раствор гидроксида натрия.
11. Способ по п.1, где цеолит Y имеет размер кристалла приблизительно не более 50 нм.
12. Способ по п.1, где цеолит Y имеет размер кристалла приблизительно не более 25 нм.
13. Способ по п.1, где цеолит Y имеет содержание натрия приблизительно не более 0,2 мас.%.
14. Способ по п.1, где цеолит Y имеет содержание натрия приблизительно не более 0,1 мас.%.
15. Способ по п.1, где цеолит Y имеет содержание натрия приблизительно не более 0,05 мас.%.
16. Способ по п.1, где катализатор включает тугоплавкий оксидный связующий материал.
17. Способ по п.16, где тугоплавкий оксидный связующий материал состоит из одного или более оксидов, выбираемых из группы, включающей диоксид кремния, оксида алюминия, диоксид кремния-оксида алюминия, диоксид титана и диоксид циркония.
18. Способ по п.1, где цеолит Y содержит один или более металлов, выбираемых из группы, включающей Pt, Pd, Ir, Ru, Rh, Os, Fe, Co, Ni, La, Ce, Pr, Ti, Zr, Hf, V, Nb, Ta, Cr, Mo, W, Cu, Ag и Au.
19. Способ по п.1, где цеолит Y включает лантан и где массовое соотношение лантана и цеолита равно, по меньшей мере, 0,04.
20. Способ по п.1, где цеолит Y имеет объемное соотношение мезопор и микропор приблизительно в пределах от 0,2 до 6,0.
21. Способ по п.1, где катализатор имеет площадь поверхности по БЭТ, по меньшей мере, около 275 м2/г и где цеолит Y содержит компонент редкоземельного металла при массовом соотношении редкоземельного металла и цеолита, равном, по меньшей мере, 0,04, где цеолит имеет объемное соотношение мезопор и микропор приблизительно в пределах от 0,2 до 6,0 и размер элементарной ячейки приблизительно от 24,6 Е до 24,9 Е.
22. Способ по п.1, где условия реакции алкилирования включают температуру приблизительно от -40°C до 250°C, давление приблизительно от 1 бар до 100 бар и WHSV приблизительно от 0,1 до 500 ч-1.
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Families Citing this family (35)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7405336B2 (en) * 2004-10-18 2008-07-29 Fina Technology, Inc. Promoters for controlling acidity and pore size of zeolite catalysts for use in alkylation
US8105968B2 (en) * 2006-10-17 2012-01-31 Lummus Technology Inc. Bimetallic alkylation catalysts
US7655824B2 (en) * 2006-10-30 2010-02-02 Uop Llc Processes for producing alkylbenzenes over solid acid catalyst at low benzene to olefin ratios and low heavies make
US7381676B1 (en) 2007-01-16 2008-06-03 Exxonmobil Chemical Patents Inc. Catalyst composition and its use thereof in aromatics alkylation
FR2920423B1 (fr) * 2007-09-04 2009-11-13 Inst Francais Du Petrole Preparation d'un materiau composite poreux a base de zeolithe eu-1 et sa mise en oeuvre en isomerisation des aromatiques en c8.
US20090275791A1 (en) * 2008-05-05 2009-11-05 Saudi Arabian Oil Company Ceramic foam catalyst support for gasoline alkylation
JP5564769B2 (ja) * 2008-08-12 2014-08-06 株式会社明電舎 低級炭化水素芳香族化触媒及び芳香族化合物の製造方法
US8395006B2 (en) * 2009-03-13 2013-03-12 Exxonmobil Research And Engineering Company Process for making high octane gasoline with reduced benzene content by benzene alkylation at high benzene conversion
US20110143920A1 (en) * 2009-12-16 2011-06-16 Uop Llc Rare Earth Exchanged Catalyst for Use in Detergent Alkylation
TW201139336A (en) * 2010-02-05 2011-11-16 Fina Technology Styrene production processes and catalysts for use therein
WO2011155400A1 (ja) * 2010-06-10 2011-12-15 宇部興産株式会社 アルキル化反応用触媒及び該触媒を用いたアルキル芳香族炭化水素化合物の製造方法
RU2445165C1 (ru) * 2010-09-09 2012-03-20 Учреждение Российской Академии Наук Ордена Трудового Красного Знамени Институт Нефтехимического Синтеза Им. А.В. Топчиева Ран (Инхс Ран) Катализатор, способ его получения (варианты) и способ жидкофазного алкилирования изобутана олефинами c2-c4 в его присутствии
US8791040B2 (en) * 2010-11-03 2014-07-29 Fina Technology, Inc. Catalysts containing nano-materials and methods of making and using same
DE102011101877A1 (de) * 2011-05-18 2012-11-22 Süd-Chemie AG Niedertemperatur-Oxidationskatalysator mit besonders ausgeprägten hydrophoben Eigenschaften für die Oxidation organischer Schadstoffe
US20130005564A1 (en) * 2011-06-30 2013-01-03 Uop Llc Synthesis of crystalline long-ranged ordered materials from preformed amorphous solids
RU2478429C1 (ru) * 2011-07-28 2013-04-10 Федеральное государственное бюджетное учреждение науки Ордена Трудового Красного Знамени Институт нефтехимического синтеза им. А.В. Топчиева Российской академии наук (ИНХС РАН) Катализатор, способ его получения и способ трансалкилирования бензола диэтилбензолами с его использованием
US20130064757A1 (en) * 2011-09-09 2013-03-14 Uop Llc Methods for forming zeolites from homogeneous amorphous silica alumina
RU2505357C2 (ru) * 2011-10-27 2014-01-27 Российская Федерация, от имени которой выступает Министерство промышленности и торговли Российской Федерации (Минпромторг России) Разработка технологии производства катализаторов алкилирования
US20130172649A1 (en) * 2011-12-30 2013-07-04 Sivadinarayana Chinta Supported nano sized zeolite catalyst for alkylation reactions
RU2482917C1 (ru) * 2012-04-05 2013-05-27 Федеральное государственное бюджетное учреждение науки Ордена Трудового Красного Знамени Институт нефтехимического синтеза им. А.В. Топчиева Российской академии наук (ИНХС РАН) Способ получения гетерогенного катализатора для получения ценных и энергетически насыщенных компонентов бензинов
CN103540340B (zh) * 2012-07-12 2015-10-21 中国石油化工股份有限公司 汽油精制方法
CN104692412A (zh) * 2013-12-06 2015-06-10 中国石油大学(北京) 一种合成NaY分子筛的方法及其合成的NaY分子筛
PL3167026T3 (pl) * 2014-07-07 2019-11-29 Albemarle Europe Sprl Sposób alkilowania przy użyciu katalizatora zawierającego bogate w cer zeolity z zawartością pierwiastków ziem rzadkich i metal uwodorniający
RU2579512C1 (ru) * 2014-12-30 2016-04-10 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Санкт-Петербургский государственный технологический институт (технический университет)". Способ приготовления катализатора и катализатор алкилирования изобутана изобутеном
CA2989428A1 (en) 2015-06-22 2016-12-29 Exelus, Inc. Catalyzed alkylation, alkylation catalysts, and methods of making alkylation catalysts
CN107866267B (zh) * 2016-09-26 2020-07-07 中国石油化工股份有限公司 用于合成环己基苯的催化剂
SG11201907913RA (en) * 2017-03-01 2019-09-27 Albemarle Europe Srl Alkylation process with improved octane number
RU2700792C2 (ru) * 2017-12-25 2019-09-23 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Санкт-Петербургский государственный технологический институт (технический университет)" (СПбГТИ(ТУ)) Способ получения катализатора для осуществления процесса алкилирования парафинов олефинами
CN108722406B (zh) * 2018-06-04 2020-10-23 山东麟丰化工科技有限公司 一种钨基催化剂、制备方法及其在异丁烷-丁烯烷基化反应中的用途
CN110562995B (zh) * 2018-06-06 2021-05-28 中国石油化工股份有限公司 纳米y沸石的合成方法、合成的纳米y沸石及用途
CN112387301B (zh) * 2019-08-15 2023-05-26 中国石油天然气股份有限公司 一种含y分子筛的碳四烷基化催化剂及其制备方法
US11078431B2 (en) 2019-12-16 2021-08-03 Saudi Arabian Oil Company Modified ultra-stable Y (USY) zeolite catalyst for deolefinization of hydrocarbon streams
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
RU2751336C1 (ru) * 2020-10-02 2021-07-13 Общество с ограниченной ответственностью "Газпром нефтехим Салават" (ООО "Газпром нефтехим Салават") Катализатор, способ его получения и способ трансалкилирования бензола диэтилбензолами с его использованием
US11484869B2 (en) 2020-12-09 2022-11-01 Saudi Arabian Oil Company Modified ultra-stable Y (USY) zeolite catalyst for dealkylation of aromatics

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3549557A (en) 1968-06-26 1970-12-22 Union Carbide Corp Isoparaffin alkylation process and catalyst for use therein
US3815004A (en) 1973-06-06 1974-06-04 Hyper Loop Rotary motor
US3851004A (en) 1973-09-27 1974-11-26 Union Carbide Corp Hydrocarbon alkylation process using catalyst regeneration
US4899008A (en) * 1986-06-27 1990-02-06 Mobil Oil Corporation Direct catalytic alkylation of mononuclear aromatics with lower alkanes
FR2662438B1 (fr) * 1990-05-22 1993-10-29 Institut Francais Petrole Procede de production d'alkylbenzenes utilisant des catalyseurs a base de zeolithe y desaluminee.
US5177284A (en) * 1991-05-28 1993-01-05 Mobil Oil Corporation Catalysts/process to synthesize alkylated naphthalene synthetic fluids with increased alpha/beta isomers for improving product qualities
US5601798A (en) * 1993-09-07 1997-02-11 Pq Corporation Process for preparing zeolite Y with increased mesopore volume
WO1998023560A1 (en) * 1996-11-27 1998-06-04 Akzo Nobel N.V. Process for alkylating hydrocarbons
US6004527A (en) 1997-09-29 1999-12-21 Abb Lummus Global Inc. Method for making molecular sieves and novel molecular sieve compositions
US6057485A (en) * 1998-11-17 2000-05-02 Fina Technology, Inc. Gas phase alkylation with split load of catalyst
AU2001266005A1 (en) * 2000-05-30 2001-12-11 Akzo Nobel N.V. Novel alkylation catalyst and its use in alkylation
US6793911B2 (en) * 2002-02-05 2004-09-21 Abb Lummus Global Inc. Nanocrystalline inorganic based zeolite and method for making same
JP4541688B2 (ja) * 2003-11-28 2010-09-08 薫 藤元 イソパラフィン−オレフィンアルキル化法

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