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This article makes an analysis on the major technical difficulties encountered in the process of revamping and expanding the capacity of the continuous catalytic reforming (CCR) unit from 600 kt/a to 800 kt/a at Tianjin Petrochemical Company. The requirements for expanding the CCR unit capacity to 800 kt/a have been met through adopting the low carbon-make PS-VI catalyst, properly lowering the RONC of the reformate, and appropriately retrofitting the towers and furnaces while keeping the reaction system, the catalyst regeneration system and the recycle hydrogen compressor intact. The calibration results have revealed that the liquid yield of reformate products, the octane rating of reformate, the pure hydrogen yield, the aromatics yield and the overall conversion rate all have met the revamp design targets.
This article makes an analysis on the major technical difficulties encountered in the process of revamping and expanding the capacity of the continuous catalytic reforming (CCR) unit from 600 kt / a to 800 kt / a at Tianjin Petrochemical Company. The requirements for expanding the CCR unit capacity to 800 kt / a have been met through adopting the low carbon-make PS-VI catalyst, properly lowering the RONC of the reformate, and suitably retrofitted the towers and furnaces while keeping the reaction system, the catalyst regeneration system and the recycle hydrogen compressor intact. The calibration results have revealed that the liquid yield of reformate products, the octane rating of reformate, the pure hydrogen yield, the aromatics yield and the overall conversion rate all have the revamp design targets.