HYBRID APPARATUS FOR REFORMING HYDROCARBON

Disclosed is a hybrid apparatus to reform hydrocarbon. According to an embodiment of the present invention, the hybrid apparatus to reform hydrocarbon may comprise: a hybrid chamber receiving any one of gas containing oxygen or air, hydrocarbon, and steam; a burner disposed on one side of the hybrid...

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Bibliographische Detailangaben
Hauptverfasser:	WON, WANG YUN, JUNG, YONG WON, KO, DAE HO, AHN, EUI SUB
Format:	Patent
Sprache:	eng ; kor
Schlagworte:	BLASTING CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY CHEMISTRY COMPOUNDS THEREOF ENGINE PLANTS IN GENERAL ENGINE PLANTS NOT OTHERWISE PROVIDED FOR ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES HEATING INORGANIC CHEMISTRY LIGHTING MACHINES OR ENGINES IN GENERAL MECHANICAL ENGINEERING METALLURGY NON-METALLIC ELEMENTS PERFORMING OPERATIONS PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL STEAM ACCUMULATORS STEAM ENGINE PLANTS STEAM ENGINES THEIR RELEVANT APPARATUS TRANSPORTING WEAPONS
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Beschreibung
Zusammenfassung:	Disclosed is a hybrid apparatus to reform hydrocarbon. According to an embodiment of the present invention, the hybrid apparatus to reform hydrocarbon may comprise: a hybrid chamber receiving any one of gas containing oxygen or air, hydrocarbon, and steam; a burner disposed on one side of the hybrid chamber combusting hydrocarbon, gas, and steam to supply combustion heat and combustion gas into the hybrid chamber; at least one first reactor provided inside the hybrid chamber, generating an endothermic flow of synthetic gas by the hydrocarbon, steam, the combustion heat, the exothermic reaction heat, and an endothermic reaction between catalysts for a steam methane reformer (SMR), to generate hydrogen; and a second reactor disposed adjacent to the first reactor inside the hybrid chamber, generating an exothermic flow of synthetic gas by the combustion heat, the combustion gas, and an exothermic reaction between the catalysts for an autothermal reformer (ATR) to generate hydrogen and supply endothermic reaction heat to the first reactor.