发明名称 PRODUCTION OF SYNTHESIS GAS
摘要 In a process for steam reforming of a hydrocarbon gas feedstream wherein: (a) the hydrocarbon gas feedstream is partially reformed at elevated temperatures in indirect heat exchange with hot combustion gases in a direct fired primary reforming furnace provided with a convection section for recovery of excess heat from said combustion gases; and (b) the partially reformed feedstream is then further reformed in the presence of an oxygen-containing gas and steam in a secondary reformer to form a secondary reformer gaseous effluent; the improvement which comprises recovering waste heat from said secondary reformer effluent gas and from said primary reforming combustion products by (i) heating a high pressure saturated steam in a first steam superheating zone by indirect heat exchange with at least a portion of said secondary reformer effluent gas to form a first superheated steam stream; and (ii) further heating said first superheated steam in a second steam superheating zone by indirect heat exchange with at least a portion of said primary reformer hot combustion gases to form a second superheated steam stream.
申请公布号 AU3528284(A) 申请公布日期 1985.05.16
申请号 AU19840035282 申请日期 1984.11.09
申请人 EXXON RESEARCH AND ENGINEERING CO. 发明人 ROBERT M. OSMAN
分类号 C01B3/38 主分类号 C01B3/38
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