EA201691848A1 - Способ запуска и эксплуатации реактора фишера-тропша - Google Patents

Способ запуска и эксплуатации реактора фишера-тропша

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EA201691848A1
EA201691848A1 EA201691848A EA201691848A EA201691848A1 EA 201691848 A1 EA201691848 A1 EA 201691848A1 EA 201691848 A EA201691848 A EA 201691848A EA 201691848 A EA201691848 A EA 201691848A EA 201691848 A1 EA201691848 A1 EA 201691848A1
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reactor
feed stream
gaseous feed
reaction temperature
concentration
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EA201691848A
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EA033844B1 (ru
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Геррит Лендерт БЕЗЕМЕР
Каролус Маттиас Анна Мария Местерс
Бреен Йохан Петер Ден
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Шелл Интернэшнл Рисерч Маатсхаппий Б.В.
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Publication of EA201691848A1 publication Critical patent/EA201691848A1/ru
Publication of EA033844B1 publication Critical patent/EA033844B1/ru

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  • Chemical & Material Sciences (AREA)
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  • General Chemical & Material Sciences (AREA)
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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

Изобретение относится к способу запуска и эксплуатации реактора Фишера-Тропша, включающему в себя стадии, на которых: (а) обеспечивают реактор неподвижным слоем восстановленного катализатора Фишера-Тропша, который содержит кобальт в качестве каталитически активного металла; (b) подают газообразный сырьевой поток, содержащий монооксид углерода и водород, в реактор, причем указанный газообразный сырьевой поток первоначально содержит азотсодержащее соединение, отличное от молекулярного азота, в начальной концентрации в диапазоне от 0,1 до 50 об.ч/млн, в расчете на объем газообразного сырьевого потока; (с) осуществляют конверсию монооксида углерода и водорода, поданных с газообразным сырьевым потоком в реактор, в углеводороды при начальной температуре реакции, при этом начальную температуру реакции устанавливают на значении по меньшей мере 200°С и углеводороды получают при первой величине выхода; (d) поддерживают начальную температуру реакции на установленном значении и поддерживают указанную первую величину выхода с помощью уменьшения концентрации азотсодержащего соединения в газообразном сырьевом потоке, подаваемом в реактор; (е) при необходимости повышают температуру реакции после уменьшения концентрации азотсодержащего соединения в газообразном сырьевом потоке до значения ниже 100 об.ч/млрд.
EA201691848A 2014-03-17 2015-03-16 Способ запуска и эксплуатации реактора фишера-тропша EA033844B1 (ru)

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EP14160190 2014-03-17
PCT/EP2015/055421 WO2015140099A1 (en) 2014-03-17 2015-03-16 A method for start-up and operation of a fischer-tropsch reactor

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EP (1) EP3119856A1 (ru)
CN (1) CN106103656B (ru)
AP (1) AP2016009375A0 (ru)
BR (1) BR112016021286B1 (ru)
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MY (1) MY190621A (ru)
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WO2016063043A2 (en) * 2014-10-20 2016-04-28 Velocys Technologies Limited Process of removing heat
AU2016313770B2 (en) * 2015-09-04 2019-12-05 Shell Internationale Research Maatschappij B.V. Fischer-Tropsch process

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US4595703A (en) 1984-06-29 1986-06-17 Exxon Research And Engineering Co. Preparation of hydrocarbons from synthesis gas
US4626552A (en) * 1986-01-06 1986-12-02 Exxon Research And Engineering Company Process for the start-up of a Fischer-Tropsch reactor
EP0833807B1 (en) 1995-06-16 2004-04-14 Shell Internationale Researchmaatschappij B.V. Catalyst and process for the preparation of hydrocarbons
EP1444040B1 (en) * 2001-10-25 2005-06-29 Sasol Technology (Proprietary) Limited Process for activating cobalt catalysts
US7045554B2 (en) * 2003-09-03 2006-05-16 Conocophillips Company Method for improved Fischer-Tropsch catalyst stability and higher stable syngas conversion
US20050154069A1 (en) 2004-01-13 2005-07-14 Syntroleum Corporation Fischer-Tropsch process in the presence of nitrogen contaminants
FR2878845B1 (fr) * 2004-12-03 2007-01-12 Inst Francais Du Petrole Procede d'interruption provisoire d'une reaction de type fischer-tropsch dans un reacteur a lit triphasique
US7524787B2 (en) * 2005-01-11 2009-04-28 Sasol Technology (Proprietary Limited) Producing supported cobalt catalysts for the Fisher-Tropsch synthesis
BRPI0619587B1 (pt) 2005-12-09 2016-05-24 Shell Int Research método para iniciar um processo em estado estacionário para produzir hidrocarbonetos a partir de gás de síntese, e, processo para produzir hidrocarbonetos a partir de uma alimentação hidrocarbonácea
EP2276718B1 (en) 2008-04-16 2018-08-29 University of Cape Town Process for the production of hydrocarbons including olefins from synthesis gas
EP2660229B1 (en) 2009-10-13 2018-04-25 Sasol Technology (PTY) Limited Production of hydrocarbons

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BR112016021286B1 (pt) 2021-05-11
WO2015140099A1 (en) 2015-09-24
MY190621A (en) 2022-04-27
ZA201605681B (en) 2018-03-28
CN106103656B (zh) 2018-07-24
CN106103656A (zh) 2016-11-09
BR112016021286A8 (pt) 2020-10-13
US9822312B2 (en) 2017-11-21
EA033844B1 (ru) 2019-12-02
AP2016009375A0 (en) 2016-08-31
EP3119856A1 (en) 2017-01-25

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