| 摘要 |
A multi-reactor hydrocarbon catalytic conversion system includes at least three reactors, a feed source and apparatus for sequentially backwardly rotating the reactors during operation. In each cycle, at least one reactor is regenerated, while other reactors operate in process mode positions. A reactor with regenerated catalyst is in a terminal position, and a reactor having least fresh catalyst is first. The first reactor receives fresh feed while the terminal reactor, having freshest catalyst, receives the partially converted feed. Method and apparatus are provided for rotation of the reactors, without the necessity of stopping operation of the catalytic conversion process while the shifting of the reactors is being performed. Heat exchangers are provided to control the inlet temperature of effluent provided to downstream reactors. The heat exchangers can occupy fixed process positions or, alternatively, can swing with the reactors in the sequential rotation process. |
