发明名称 |
Fischer Tropsch process using improved extrudates |
摘要 |
A process for performing a Fischer Tropsch reaction comprising (a) providing syngas to a reactor, said reactor comprising catalyst particles that have been produced by extruding a paste using a die comprising a plurality of channels extending from an inlet to an outlet, wherein from the inlet to the outlet each channel comprises a first section with a helical bore with a non-circular cross-section, and a second section with a cylindrical bore which has a diameter equal or greater than that of the first section, wherein the second section is at least twice as long as a diameter of the first section; (b) providing the following process conditions in the reactor: a temperature from 125 to 350° C., and a pressure from 5 to 150 bar absolute, and a gaseous hourly space velocity from 500 to 10000 Nl/l/h; and (c) removing Fischer Tropsch product from the reactor. |
申请公布号 |
US8835516(B2) |
申请公布日期 |
2014.09.16 |
申请号 |
US201113327436 |
申请日期 |
2011.12.15 |
申请人 |
Shell Oil Company |
发明人 |
Barthel Rene Georges Ernst;Van Wieringen Maria Johanna Wilhelmina;Van Der Sman Leonardus Maria;Domokos László |
分类号 |
C07C27/00 |
主分类号 |
C07C27/00 |
代理机构 |
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代理人 |
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主权项 |
1. A process for performing a Fischer Tropsch reaction comprising the following steps:
providing syngas to a reactor, said reactor comprising catalyst particles that have been produced by extruding a paste comprising (i) a porous refractor oxide, (ii) a liquid, and (iii) a metal compound, said extrusion having been performed using a die comprising a plurality of channels extending from an inlet to an outlet, wherein from the inlet to the outlet each channel comprises a first section with a helical bore with a non-circular cross-section, and a second section with a cylindrical bore which has a diameter equal or greater than that of the first section, wherein the second section is at least twice as long as a diameter of the first section; providing the following process conditions in the reactor: a temperature in the range from 125 to 350° C., and a pressure in the range from 5 to 150 bar absolute, and a gaseous hourly space velocity in the range from 500 to 10000 Nl/l/h; removing Fischer Tropsch product from the reactor. |
地址 |
Houston TX US |