发明名称 |
Apparatuses and methods for reforming of hydrocarbons |
摘要 |
Apparatuses and methods for reforming of hydrocarbons are presented. In one example, a method comprises burning fuel gas to form a hot flue gas and heat a reforming-zone feedstock that contains (C5-C11) hydrocarbons to form a heated reforming-zone feed stream. The heated reforming-zone feed stream is partially reformed to form a partially reformed effluent. The partially reformed effluent is advanced through a process heat recovery coil arrangement that is recovering heat from the hot flue gas to form a heated partially reformed effluent. The heated partially reformed effluent is contacted with reforming catalyst at reforming conditions effective to form a reforming reaction-zone effluent. The reforming reaction-zone effluent comprises H2, C5+ hydrocarbons including aromatics, and C4− hydrocarbons. |
申请公布号 |
US9327259(B2) |
申请公布日期 |
2016.05.03 |
申请号 |
US201313871271 |
申请日期 |
2013.04.26 |
申请人 |
UOP LLC |
发明人 |
Hartman William M.;Zhu Xin X.;Lane Lisa M.;Yanez William |
分类号 |
C10J3/46;B01J8/04;B01J8/00;C10G35/04 |
主分类号 |
C10J3/46 |
代理机构 |
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代理人 |
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主权项 |
1. An apparatus for reforming of hydrocarbons, the apparatus comprising:
a reforming heating-zone configured to heat a reforming-zone feedstock that contains (C5-C11) hydrocarbons to form a heated reforming-zone feed stream, wherein the reforming heating-zone has a radiant furnace section that is configured to burn fuel gas to form hot flue gas and a common convection section that is in fluid communication with the radiant furnace section to receive the hot flue gas, and wherein the reforming heating-zone comprises a process heat recovery coil arrangement disposed in the common convection section for recovering heat from the hot flue gas; and a reforming reaction-zone that receives the heated reforming-zone feed stream and that comprises:
a plurality of staged reactor catalyst beds that is in fluid communication with the radiant furnace section; andan additional reactor catalyst bed that is in fluid communication with the process heat recovery coil arrangement disposed within the common convection section, wherein the reforming heating-zone, the plurality of staged reactor catalyst beds, and the additional reactor catalyst bed are cooperatively configured for interstage heating and reforming of the heated reforming-zone feed stream to form a reforming reaction-zone effluent that comprises H2, C5+ hydrocarbons including aromatics, and C4− hydrocarbons. |
地址 |
Des Plaines IL US |