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RU2008102375A - Компактный редуктор реформинга - Google Patents

Компактный редуктор реформинга Download PDF

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Publication number
RU2008102375A
RU2008102375A RU2008102375/15A RU2008102375A RU2008102375A RU 2008102375 A RU2008102375 A RU 2008102375A RU 2008102375/15 A RU2008102375/15 A RU 2008102375/15A RU 2008102375 A RU2008102375 A RU 2008102375A RU 2008102375 A RU2008102375 A RU 2008102375A
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Russia
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section
combustion
reactor
closed volume
named
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RU2008102375/15A
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English (en)
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RU2415073C2 (ru
Inventor
Михаел БОЭ (DK)
Михаел БОЭ
Джон Бегил ХАНСЕН (DK)
Джон Бегил ХАНСЕН
Original Assignee
Хальдор Топсеэ А/С (DK)
Хальдор Топсеэ А/С
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Publication of RU2008102375A publication Critical patent/RU2008102375A/ru
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Publication of RU2415073C2 publication Critical patent/RU2415073C2/ru

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    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
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    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/384—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts the catalyst being continuously externally heated
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Abstract

1. Реактор реформинга для превращения исходной жидкости в водород, включающий не менее чем один подающий патрубок, несущий поступающую на превращение исходную жидкость, секцию реформинга, находящуюся в закрытом объеме, секцию кипения и секцию горения, в котором названная секция реформинга содержит одну или несколько заполненных катализатором реформинга катализаторных трубок, названная секция кипения имеет один или несколько сквозных каналов для прохождения газообразных продуктов горения из секции горения, и названная секция горения снабжена не менее чем одной горелкой, при этом теплообменная среда, которая нужна для реформинга названной исходной жидкости в одной или в нескольких катализаторных трубках, представляет собой газожидкостную смесь, которая самопроизвольно циркулирует, находясь в названном закрытом объеме, и при этом по крайней мере часть названного закрытого объема находится внутри названной секции кипения. ! 2. Реактор по п.1, в котором часть названного закрытого объема, внутри которого происходит самопроизвольная циркуляция газожидкостной смеси, находится в секции кипения в виде одного элемента удлиненной формы или в виде нескольких элементов удлиненной формы, образующих множество расположенных по кругу или расположенных радиально элементов удлиненной формы, при этом названные элементы удлиненной формы свободно сообщаются между собой. ! 3. Реактор по п.2, в котором секция кипения реактора снабжена несколькими расположенными вертикально или расположенными горизонтально дефлекторами, причем названные дефлекторы расположены преимущественно поперек движения потока газообразных проду�

Claims (9)

1. Реактор реформинга для превращения исходной жидкости в водород, включающий не менее чем один подающий патрубок, несущий поступающую на превращение исходную жидкость, секцию реформинга, находящуюся в закрытом объеме, секцию кипения и секцию горения, в котором названная секция реформинга содержит одну или несколько заполненных катализатором реформинга катализаторных трубок, названная секция кипения имеет один или несколько сквозных каналов для прохождения газообразных продуктов горения из секции горения, и названная секция горения снабжена не менее чем одной горелкой, при этом теплообменная среда, которая нужна для реформинга названной исходной жидкости в одной или в нескольких катализаторных трубках, представляет собой газожидкостную смесь, которая самопроизвольно циркулирует, находясь в названном закрытом объеме, и при этом по крайней мере часть названного закрытого объема находится внутри названной секции кипения.
2. Реактор по п.1, в котором часть названного закрытого объема, внутри которого происходит самопроизвольная циркуляция газожидкостной смеси, находится в секции кипения в виде одного элемента удлиненной формы или в виде нескольких элементов удлиненной формы, образующих множество расположенных по кругу или расположенных радиально элементов удлиненной формы, при этом названные элементы удлиненной формы свободно сообщаются между собой.
3. Реактор по п.2, в котором секция кипения реактора снабжена несколькими расположенными вертикально или расположенными горизонтально дефлекторами, причем названные дефлекторы расположены преимущественно поперек движения потока газообразных продуктов горения, образующихся в секции горения.
4. Реактор по п.2, у которого один или несколько элементов удлиненной формы, имеющих в предпочтительном случае форму трубок, снабжены рукавами для того, чтобы представить возможность прохождения газообразных продуктов горения через боковую полость, образованную названными элементами удлиненной формы и названными рукавами.
5. Реактор по п.1, в котором названный не менее чем один подающий патрубок, несущий поступающую на превращение исходную жидкость, проходит в названный закрытый объем реактора.
6. Реактор по п.1, в котором названный не менее чем один подающий патрубок, несущий поступающую на превращение исходную жидкость, входит в реактор через фланец, расположенный на внешней стенке реактора, при этом названная перерабатываемая жидкость предварительно нагревается за счет непрямого контакта с выходящим из секции реформинга реактора газом, полученным в результате превращения.
7. Реактор по п.1, в котором названный не менее чем один подающий патрубок проходит в вертикальном направлении в промежуточное отделение, из которого не менее чем один подающий патрубок, несущий подаваемый на переработку газ, продолжается в вертикальном направлении внутри закрытого объема реактора, где не менее чем один названный подающий патрубок, несущий поступающий на переработку газ, образует кольцо.
8. Реактор по п.1, в котором названный закрытый объем, включающий названную секцию реформинга и секцию кипения, практически полностью окружен изолирующим корпусом, причем названный изолирующий корпус прилегает к первой боковой полости, несущей газообразные продукты горения, и ко второй боковой полости, несущей воздух для горения.
9. Реактор по одному из пп. от 1 до 8, у которого названная секция горения снабжена одной единственной каталитической горелкой, при этом названная каталитическая горелка снабжена слоями проволочной сетки, расположенными один за другим и покрытыми керамикой с пропиткой катализатором окисления, причем генерируемое в процессе горения тепло переносится конвекционным путем от образовавшихся газообразных продуктов горения на самопроизвольно циркулирующую газожидкостную смесь.
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