REFORMER ARRANGEMENT FOR PRODUCTION OF SYNTHESIS GAS AND/OR HYDROGEN
The invention discloses a reformer arrangement for production of synthesis gas and/or hydrogen, at least comprising the following elements: - a main reformer (1) connected to a main reformer reactant feed (2) and a main reformer product outlet (3); - a gas-heated reformer (GHR) (4) comprising a GHR...
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creator | SCHOLZ, Marco SIGGE, Sebastian |
description | The invention discloses a reformer arrangement for production of synthesis gas and/or hydrogen, at least comprising the following elements: - a main reformer (1) connected to a main reformer reactant feed (2) and a main reformer product outlet (3); - a gas-heated reformer (GHR) (4) comprising a GHR reformer interior (4h) with GHR reformer tubes (4a) disposed therein, a GHR raw gas inlet (4b) connected to the GHR reformer tubes (4a); a GHR shell (4c) of the GHR reformer tubes (4a); a GHR main reformer product gas inlet (4d) connected to the main reformer product outlet (3) and the GHR shell (4c); a GHR product outlet (4e); - a heat transferrer (5) with a heat transferrer inlet opening (5a) and a heat transferrer outlet opening (5c), wherein a heat duct (5b) is disposed between the heat transferrer inlet opening (5a) and the GHR product outlet (4e); characterized in that the GHR product outlet (4e) is disposed in a plane parallel with the heat transferrer (5) and the height measured from the base up to the centre axis of the GHR product outlet (4e) is not more than plus/minus 20% the height measured from the base up to the centre axis of the heat transferrer inlet opening (5a). |
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- a gas-heated reformer (GHR) (4) comprising a GHR reformer interior (4h) with GHR reformer tubes (4a) disposed therein, a GHR raw gas inlet (4b) connected to the GHR reformer tubes (4a); a GHR shell (4c) of the GHR reformer tubes (4a); a GHR main reformer product gas inlet (4d) connected to the main reformer product outlet (3) and the GHR shell (4c); a GHR product outlet (4e); - a heat transferrer (5) with a heat transferrer inlet opening (5a) and a heat transferrer outlet opening (5c), wherein a heat duct (5b) is disposed between the heat transferrer inlet opening (5a) and the GHR product outlet (4e); characterized in that the GHR product outlet (4e) is disposed in a plane parallel with the heat transferrer (5) and the height measured from the base up to the centre axis of the GHR product outlet (4e) is not more than plus/minus 20% the height measured from the base up to the centre axis of the heat transferrer inlet opening (5a).</description><language>eng ; fre ; ger</language><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS ; 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SIGGE, Sebastian</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_EP4003910A13</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; fre ; ger</language><creationdate>2022</creationdate><topic>ACYCLIC OR CARBOCYCLIC COMPOUNDS</topic><topic>AMMONIA</topic><topic>CHEMISTRY</topic><topic>COMPOUNDS THEREOF</topic><topic>CYANOGEN</topic><topic>INORGANIC CHEMISTRY</topic><topic>METALLURGY</topic><topic>NON-METALLIC ELEMENTS</topic><topic>ORGANIC CHEMISTRY</topic><toplevel>online_resources</toplevel><creatorcontrib>SCHOLZ, Marco</creatorcontrib><creatorcontrib>SIGGE, Sebastian</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>SCHOLZ, Marco</au><au>SIGGE, Sebastian</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>REFORMER ARRANGEMENT FOR PRODUCTION OF SYNTHESIS GAS AND/OR HYDROGEN</title><date>2022-06-01</date><risdate>2022</risdate><abstract>The invention discloses a reformer arrangement for production of synthesis gas and/or hydrogen, at least comprising the following elements: - a main reformer (1) connected to a main reformer reactant feed (2) and a main reformer product outlet (3); - a gas-heated reformer (GHR) (4) comprising a GHR reformer interior (4h) with GHR reformer tubes (4a) disposed therein, a GHR raw gas inlet (4b) connected to the GHR reformer tubes (4a); a GHR shell (4c) of the GHR reformer tubes (4a); a GHR main reformer product gas inlet (4d) connected to the main reformer product outlet (3) and the GHR shell (4c); a GHR product outlet (4e); - a heat transferrer (5) with a heat transferrer inlet opening (5a) and a heat transferrer outlet opening (5c), wherein a heat duct (5b) is disposed between the heat transferrer inlet opening (5a) and the GHR product outlet (4e); characterized in that the GHR product outlet (4e) is disposed in a plane parallel with the heat transferrer (5) and the height measured from the base up to the centre axis of the GHR product outlet (4e) is not more than plus/minus 20% the height measured from the base up to the centre axis of the heat transferrer inlet opening (5a).</abstract><oa>free_for_read</oa></addata></record> |
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subjects | ACYCLIC OR CARBOCYCLIC COMPOUNDS AMMONIA CHEMISTRY COMPOUNDS THEREOF CYANOGEN INORGANIC CHEMISTRY METALLURGY NON-METALLIC ELEMENTS ORGANIC CHEMISTRY |
title | REFORMER ARRANGEMENT FOR PRODUCTION OF SYNTHESIS GAS AND/OR HYDROGEN |
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