MX2017011714A - Proceso integrado de deshidrogenacion de hidrocarburos de c3-c4. - Google Patents

Proceso integrado de deshidrogenacion de hidrocarburos de c3-c4.

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Publication number
MX2017011714A
MX2017011714A MX2017011714A MX2017011714A MX2017011714A MX 2017011714 A MX2017011714 A MX 2017011714A MX 2017011714 A MX2017011714 A MX 2017011714A MX 2017011714 A MX2017011714 A MX 2017011714A MX 2017011714 A MX2017011714 A MX 2017011714A
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MX
Mexico
Prior art keywords
catalyst
olefin
product
feed
dehydrogenation
Prior art date
Application number
MX2017011714A
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English (en)
Inventor
T Pretz Matthew
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Dow Global Technologies Llc
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Publication date
Application filed by Dow Global Technologies Llc filed Critical Dow Global Technologies Llc
Publication of MX2017011714A publication Critical patent/MX2017011714A/es

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    • C07C5/32Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
    • C07C5/327Formation of non-aromatic carbon-to-carbon double bonds only
    • C07C5/333Catalytic processes
    • C07C5/3332Catalytic processes with metal oxides or metal sulfides
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Abstract

La presente invención se refiere a un proceso integrado, adecuado para uso en una planta nueva o reacondicionada, para producir una olefina o di-olefina a través de la deshidrogenación de una alimentación de hidrocarburos de C3-C4 apropiado que incluye (1) poner en contacto la alimentación y un catalizador de deshidrogenación que tiene una clasificación de Geldart A o Geldart B en un lecho fluidizado a una temperatura desde 550°C a 760°C y una presión desde aproximadamente 41.4 a aproximadamente 308.2 kPa (aproximadamente 6.0 a aproximadamente 44.7 psia) y una relación de catalizador a alimentación, p/p, desde 5 a 100 para formar un producto deshidrogenado; separar el producto deshidrogenado y mezcla de alimentación de partida sin reaccionar de una porción del catalizador por medio de un sistema de separación ciclónica; reactivar el catalizador en un regenerador fluidizado por combustión a 660° C a 850°C, seguido por contacto con un fluido que contiene oxígeno a 660°C o mayor, y retornar el catalizador al reactor de deshidrogenación; (2) comprimir la mezcla de productos para formar una mezcla de productos comprimida; y (3) fraccionar la mezcla de productos comprimida para formar una corriente de productos que incluye al menos la olefina o di-olefina objetivo. El proceso integrado ofrece una capacidad de la planta, aumentada, economía mejorada, y efecto ambiental reducido en comparación con otros procesos conocidos y convencionales.
MX2017011714A 2015-03-30 2016-03-07 Proceso integrado de deshidrogenacion de hidrocarburos de c3-c4. MX2017011714A (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US201562139938P 2015-03-30 2015-03-30
PCT/US2016/021127 WO2016160273A1 (en) 2015-03-30 2016-03-07 Integrated c3-c4 hydrocarbon dehydrogenation process

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MX2017011714A true MX2017011714A (es) 2017-11-10

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US (2) US10227271B2 (es)
EP (2) EP3699163B1 (es)
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