发明名称 |
NATURAL GAS CONVERSION TO HYDROCARBONS AND AMMONIA |
摘要 |
A process for the production of hydrocarbons and ammonia, and more particularly a process for optimizing the production of hydrocarbons and ammonia using a combined hydrocarbon synthesis plant and ammonia synthesis plant. Synthesis gas exiting a reforming section of the hydrocarbon synthesis process is sent to a hydrogen extraction unit, where it is divided into a hydrogen-rich stream and a hydrogen-poor stream. The hydrogen-rich stream is then fed into an ammonia synthesis process. The hydrogen-poor stream may be returned to the hydrocarbon synthesis process or may be used as a fuel gas. The process reduces emission of CO<SUB>2 </SUB>into the atmosphere, and requires only one reforming section and one air separation unit for both processes. Removal of hydrogen from the hydrocarbon synthesis process before the synthesis gas enters a Fischer-Tropsch reactor also lowers the H<SUB>2</SUB>/CO ratio of the synthesis gas, therefore resulting in better hydrocarbon selectively. |
申请公布号 |
EP1204593(A2) |
申请公布日期 |
2002.05.15 |
申请号 |
EP20000962044 |
申请日期 |
2000.07.25 |
申请人 |
SASOL TECHNOLOGY (PROPRIETARY) LIMITED |
发明人 |
PRICE, JULIAN, GRAHAM;TINDALL, BARRY, ANTONY |
分类号 |
C01B3/02;C01B3/50;C01B3/56;C01C1/04;C01C3/02;C07C1/04;C10G2/00 |
主分类号 |
C01B3/02 |
代理机构 |
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代理人 |
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主权项 |
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地址 |
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