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1.发明申请公开(公告)号：US20140134099A1
公开(公告)日：2014-05-15
申请号：US14076321
申请日：2013-11-11
Applicant: Phillips 66 Company
Inventor： Uchenna P. Paul , Bruce B. Randolph , Jon M. Nelson , Kristi A. Fjare , Danielle K. Smith , Mark Rumel Cragun , Richard D. Sadok
IPC: C01B3/32
CPC classification number: C01B3/323 , C01B2203/0233 , C01B2203/0405 , C01B2203/0415 , C01B2203/043 , C01B2203/1041 , C01B2203/1058 , C01B2203/1076 , C01B2203/1082 , C01B2203/1094 , C01B2203/1211 , C01B2203/1217 , C01B2203/1223 , C01B2203/1229
Abstract: A process is described for flowing an oxygenate feed over a catalyst in an adiabatic fixed bed reactor to product a reactor effluent and heat. The reaction inside the adiabatic fixed bed reactor occurs at a reaction temperature from about 200° C. to about 375° C. The reactor effluent is then condensed to separate the liquid products and the gaseous products. A separation step then separates the gaseous products into hydrogen and off-gas.
Abstract translation: 描述了一种将含氧化合物进料在绝热固定床反应器中的催化剂上流动以产生反应器流出物和热量的方法。 绝热固定床反应器中的反应在约200℃至约375℃的反应温度下进行。然后将反应器流出物冷凝以分离液体产物和气态产物。 然后分离步骤将气态产物分离成氢气和废气。
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2.发明授权Process scheme for catalytic production of renewable hydrogen from oxygenate feedstocks 有权从含氧化合物原料催化生产可再生氢的工艺方案公开(公告)号：US09452931B2
公开(公告)日：2016-09-27
申请号：US14076321
申请日：2013-11-11
Applicant: PHILLIPS 66 COMPANY
Inventor： Uchenna P. Paul , Bruce B. Randolph , Jon M. Nelson , Kristi A. Fjare , Danielle K. Smith , Mark Rumel Cragun , Richard D. Sadok
IPC: C01B3/32
CPC classification number: C01B3/323 , C01B2203/0233 , C01B2203/0405 , C01B2203/0415 , C01B2203/043 , C01B2203/1041 , C01B2203/1058 , C01B2203/1076 , C01B2203/1082 , C01B2203/1094 , C01B2203/1211 , C01B2203/1217 , C01B2203/1223 , C01B2203/1229
Abstract: A process is described for flowing an oxygenate feed over a catalyst in an adiabatic fixed bed reactor to product a reactor effluent and heat. The reaction inside the adiabatic fixed bed reactor occurs at a reaction temperature from about 200° C. to about 375° C. The reactor effluent is then condensed to separate the liquid products and the gaseous products. A separation step then separates the gaseous products into hydrogen and off-gas.
Abstract translation: 描述了一种将含氧化合物进料在绝热固定床反应器中的催化剂上流动以产生反应器流出物和热量的方法。 绝热固定床反应器中的反应在约200℃至约375℃的反应温度下进行。然后将反应器流出物冷凝以分离液体产物和气态产物。 然后分离步骤将气态产物分离成氢气和废气。
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