Commercial Application of the PS-Ⅵ Catalyst in the Revamped 0.8 Mt/a Catalytic Reforming Unit
- 期刊名字:中国炼油与石油化工(英文版)
- 文件大小:
- 论文作者:Leng Jiachang,Hou Zhanggui
- 作者单位:Aromatics Division
- 更新时间:2022-12-12
- 下载次数:次
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 800kt/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.
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