EA025435B1 - Способ риформинга углеводородов - Google Patents

Способ риформинга углеводородов Download PDF

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EA025435B1
EA025435B1 EA201490176A EA201490176A EA025435B1 EA 025435 B1 EA025435 B1 EA 025435B1 EA 201490176 A EA201490176 A EA 201490176A EA 201490176 A EA201490176 A EA 201490176A EA 025435 B1 EA025435 B1 EA 025435B1
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cho
cco
reactor
gas
partial oxidation
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EA201490176A
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EA201490176A1 (ru
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Ким Аасберг-Петерсен
Сейер Петер Кристензен
Сандаль Томас Кристензен
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Хальдор Топсёэ А/С
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Priority claimed from EP11009101.4A external-priority patent/EP2594527A1/en
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Publication of EA201490176A1 publication Critical patent/EA201490176A1/ru
Publication of EA025435B1 publication Critical patent/EA025435B1/ru

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Abstract

Изобретение касается способа получения синтез-газа посредством автотермического риформинга, в котором остаточный газ, полученный в ходе последующего синтеза Фишера-Тропша, гидрогенизируют, а затем вводят в стадию автотермического риформинга.

Description

Настоящее изобретение касается способа получения синтез-газа, используемого для получения углеводородов путем синтеза Фишера-Тропша. В частности, изобретение касается способа получения синтез-газа посредством автотермического риформинга, в котором остаточный газ, полученный в ходе последующего процесса, в частности, в ходе синтеза Фишера-Тропша, гидрогенизируют, а затем вводят в процесс автотермического риформинга. В соответствии с более общим аспектом настоящее изобретение охватывает удаление олефинов в газе для уменьшения металлического запыливания металлических частей, находящихся в контакте с газом, в частности, для уменьшения металлического запыливания в АТР (установке автотермического риформинга), КЧО (реакторе каталитического частичного окисления) или ЧО (реакторе частичного окисления), а также в другом оборудовании, расположенном на последующих стадиях технологического процесса, через которое проходит газ.

Claims (1)

1. Способ получения синтез-газа из углеводородного сырья с пониженной склонностью к металлическому запыливанию по меньшей мере частей камеры сгорания установки автотермического риформинга (АТР), реактора каталитического частичного окисления (КЧО) или реактора частичного окисления (ЧО), включающий стадии, на которых подают указанное углеводородное сырье в реактор АТР, КЧО или ЧО и отводят поток полученного горячего синтез-газа из АТР, КЧО или ЧО, при этом подают непосредственно в указанный реактор АТР, КЧО или ЧО гидрогенизированный остаточный газ, полученный пропусканием остаточного газа из стадии синтеза Фишера-Тропша, через стадию гидрогенизации с использованием катализатора гидрогени-
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