Operation of a steam methane reformer by direct feeding of...

C - Chemistry – Metallurgy – 10 – J

Patent

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C10J 3/06 (2006.01) B09B 3/00 (2006.01) C01B 3/02 (2006.01) C02F 11/04 (2006.01) C10J 3/20 (2006.01) C10J 3/86 (2006.01) C01B 31/18 (2006.01) C07C 9/04 (2006.01)

Patent

CA 2657656

An improved, economical alternative method to supply steam and methane to a steam methane reformer (SMR) is accomplished by a combination of procedures, wherein product gas from a steam hydro-gasification reactor (SHR) is used as the feedstock for the SMR by removing impurities from the product stream from the SHR with a gas cleanup unit that operates substantially at process pressures and at a temperature above the boiling point of water at the process pressure, is located between the SHR and SMR.

L'invention concerne un procédé alternatif économique et amélioré, destiné à fournir de la vapeur et du méthane à un reformeur de méthane à la vapeur (SMR), qui consiste en une combinaison de procédures dans lesquelles on utilise le gaz produit par un réacteur d'hydrogazéification à vapeur (SHR) en tant que matière de base pour le SMR, en éliminant les impuretés du flux de produits provenant du SHR à l'aide d'une unité d'épuration de gaz qui fonctionne essentiellement à des pressions de traitement, et à une température supérieure au point d'ébullition de l'eau à la pression de traitement, qui se situe entre le SHR et le SMR.

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