首页> 外文会议>Proceedings of the 11th International Conference on Fluidized Bed Technology >START-UP OF AN ADVANCED FCC PILOT PLANT WITH INTERNALLY CIRCULATING FLUIDIZED BED
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START-UP OF AN ADVANCED FCC PILOT PLANT WITH INTERNALLY CIRCULATING FLUIDIZED BED

机译:内部循环流化床的先进FCC试点工厂的启动

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In this publication a newly constructed FCC pilot plant with an internally circulating fluidized bed is presented.The design of an existing FCC pilot plant was improved and new features were added to enhance the flexibility and controllability of the device.Experiments which validate the operability of the new pilot plant were carried out successfully.Leakage between regenerator and riser reactor was determined and satisfactory results were obtained.Due to the high importance of the C/O-ratio the impact of different factors on the circulation rate was evaluated.A variation of the cross sectional area by a cone has proven to be effective.Experiments with hydro treated VGO were carried out to investigate the influence of the C/O-ratio on product lumps.An increase of the C/O-ratio led to a higher conversion.The gas and the coke lumps both increased significantly;however, the gasoline and LCO+residue lumps decreased.
机译:在本出版物中,介绍了新建的带有内部循环流化床的FCC中试设备,改进了现有FCC中试设备的设计并增加了新功能,以增强设备的灵活性和可控制性。实验验证了该设备的可操作性成功进行了新的中试装置,确定了蓄热室和提升管反应器之间的泄漏并获得了满意的结果。由于C / O比的重要性,因此评估了不同因素对循环速率的影响。锥面截面积已被证明是有效的。进行了VGO氢化处理的实验研究了C / O比对产品结块的影响.C / O比的增加导致更高的转化率。煤气和焦炭结块均显着增加;但是汽油和LCO +残渣块减少。

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