Abstract

The effects of different iron contamination content on the formation of iron nodules and the performance of FCC catalysts have been studied by cyclic deactivation treatment using iron naphthenate. The catalysts were characterized by X-ray diffraction, N2 adsorption-desorption, and SEM. The catalysts’ performance was evaluated by the Advanced Cracking Evaluation device. It has been found that there will be obvious nodulation on the catalyst when the iron concentration exceeds 7,400 μg/g. With the iron deposition from 53 μg/g to 11,690 μg/g, the crystal structure of zeolite will not be destroyed by iron. The surface area and pore volume of the catalyst decreased significantly; the surface area decreased from 125.3 m2/g to 91.0 m2/g, and the pore volume decreased from 0.21 cm3/g to 0.16 cm3/g. The studies also showed that the increase of iron deposition will lead to the decrease of catalytic reaction efficiency. With the iron deposition from 53 μg/g to 11,690 μg/g, the conversion decreased by 4.83%. Under the same 78 wt.% conversion, bottoms yield and coke yield increased by 2.15% and 1.31%, while gasoline yield and LCO yield decreased by 2.59% and 2.16%, respectively. The real state of the industrial iron contaminated equilibrium catalyst can be mimicked by using the cyclic deactivation method.

Highlights

  • Fluid catalytic cracking (FCC) technology is one of the most important conversion processes for efficient residue processing, and it plays an important role in the oil refining field (Harding et al, 2001; Mehla et al, 2019)

  • In order to simulate the actual state of the iron contaminated equilibrium catalyst in FCC unit, different amounts of iron deposition and appropriate conditions have been selected to carry out cyclic deactivation method

  • Due to the existence of a certain amount of iron compounds in raw materials such as kaolin used in the preparation of the catalyst, the existing iron content in the catalyst should be deducted when calculating the iron deposition on the catalyst surface (Brandt et al, 2019)

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Summary

Introduction

Fluid catalytic cracking (FCC) technology is one of the most important conversion processes for efficient residue processing, and it plays an important role in the oil refining field (Harding et al, 2001; Mehla et al, 2019). In order to simulate the actual state of the iron contaminated equilibrium catalyst in FCC unit, different amounts of iron deposition and appropriate conditions have been selected to carry out cyclic deactivation method. In order to investigate the effect of different iron loading on the surface area and pore volume of the catalyst, the pore structure properties of the samples were analyzed by automatic physical adsorption instrument.

Results
Conclusion
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