| 摘要 |
Methods and systems for operating a carbon to liquids system are provided. The method includes receiving a flow of syngas, shifting the syngas to increase an H2/CO ratio of the syngas, mixing hydrogen with the shifted syngas to increase the H2/CO ratio, reacting the hydrogen/shifted syngas mixture with a catalyst in a vessel at a pressure of approximately 600 psia such that approximately 40% of the hydrogen/shifted syngas mixture is converted, recycling an un-reacted hydrogen/shifted syngas mixture to the vessel, and recycling naphta to a catalyst recovery system
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