EA201600533A1 - Катализатор и способ ароматизации c-cгазов, легких углеводородных фракций и алифатических спиртов, а также их смесей - Google Patents

Катализатор и способ ароматизации c-cгазов, легких углеводородных фракций и алифатических спиртов, а также их смесей

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EA201600533A1
EA201600533A1 EA201600533A EA201600533A EA201600533A1 EA 201600533 A1 EA201600533 A1 EA 201600533A1 EA 201600533 A EA201600533 A EA 201600533A EA 201600533 A EA201600533 A EA 201600533A EA 201600533 A1 EA201600533 A1 EA 201600533A1
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catalyst
mass
zeolite
amount
hydrocarbon
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EA201600533A
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EA031119B1 (ru
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Иосиф Изралиевич Лищинер
Ольга Васильевна МАЛОВА
Андрей Леонидович ТАРАСОВ
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Акционерное Общество Нгт Глобал
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    • C07C2/862Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation between a hydrocarbon and a non-hydrocarbon the non-hydrocarbon contains only oxygen as hetero-atoms
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    • B01J29/405Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead
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  • Chemical & Material Sciences (AREA)
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  • Materials Engineering (AREA)
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Abstract

Изобретение относится к технологии переработки углеводородного сырья, в частности к катализаторам и технологии ароматизации углеводородных газов C-С, легких низкооктановых углеводородных фракций и кислородсодержащих соединений (алифатических спиртов C-C), а также их смесей с получением концентрата ароматических углеводородов (КАУ). Катализатор содержит механическую смесь 2 цеолитов, первый из которых охарактеризован силикатным модулем SiO/AlO=20, предварительно обработан водным раствором щелочи и модифицирован оксидами редкоземельных элементов в количестве от 0,5 до 2,0 мас.% от массы первого цеолита, а второй охарактеризован силикатным модулем SiO/AlO=82, содержит остаточные количества оксида натрия 0,04 мас.% от массы второго цеолита, модифицирован оксидом магния в количестве от 0,5 до 5,0 мас.% от массы второго цеолита, причем цеолиты использованы в массовом соотношении от 1,7/1 до 2,8/1, а связующее содержит, по меньшей мере, оксид кремния и использовано в количестве от 20 до 25 мас.% от массы катализатора. Процесс проводят с использованием разработанного катализатора в изотермическом реакторе без использования рециркуляции газов сепарации путем контактирования стационарного слоя катализатора с испаренным и нагретым в преднагревателе газообразным сырьем. Технический результат - достижение более высокого выхода АрУ при практически полной конверсии у/в сырья и оксигенатов, повышенной селективности в отношении образования ксилолов в составе КАУ, при одновременном упрощении технологического оформления процесса за счет использования пониженного (в том числе атмосферного) давления.
EA201600533A 2014-01-28 2014-12-17 Катализатор и способ ароматизации c-cгазов, легких углеводородных фракций и алифатических спиртов, а также их смесей EA031119B1 (ru)

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RU2014102625/04A RU2544017C1 (ru) 2014-01-28 2014-01-28 Катализатор и способ ароматизации с3-с4 газов, легких углеводородных фракций алифатических спиртов, а также их смесей
PCT/RU2014/000953 WO2015115932A1 (ru) 2014-01-28 2014-12-17 Катализатор и способ ароматизации с3-с4 газов, легких углеводородных фракций и алифатических спиртов, а также их смесей

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EP (1) EP3100784A4 (ru)
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AU (1) AU2014380443B2 (ru)
BR (1) BR112016017158A2 (ru)
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WO2015115932A1 (ru) 2015-08-06
US10131592B2 (en) 2018-11-20
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