Abstract
The fundamental understanding of metal contamination, including nickel, vanadium and iron, is a key step in developing capability of metals tolerance and the recycling or resource utilization for fluid catalytic cracking (FCC) catalysts. However, few studies have investigated the multiple performances of composite metal contamination at the level of real industrial equilibrium catalysts (E-Cat). This work investigates the single- and multiple metal contaminations at the level of E-Cat for nickel of 6970 μg/g, vanadium of 4940 μg/g and iron of 9228 μg/g, respectively. The results indicate that the deposited Ni has least destructive effect to catalyst structure and activity, the deposited V contributes the most amount of weak or strong acids and the highest deactivation effect to the E-Cat, causing high coke yield but low liquid recovery. While the deposited Fe reduces most of the acidic sites due to surface iron nodules resulting in lower conversion and higher bottoms yield. Multiple metal deposition leads to the strong reduction for the specific surface area, pore volume and the acid amount, resulting in more serious performance than that of E-Cat. These results bridge the gap of multiple performances of composite metal contamination, providing fundamental insights for the interaction and tolerance of composite metal contamination on FCC catalysts.
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Corma A, Sauvanaud L, Mathieu Y et al (2018) Direct crude oil cracking for producing chemicals: thermal cracking modeling. Fuel 211:726–736
Chen C, Zhou L, Ji X et al (2020) Adaptive modeling strategy integrating feature selection and random forest for fluid catalytic cracking processes. Ind Eng Chem Res 59(24):11265–11274
Zhu X, Yu M, Cheng M et al (2019) Conceptual fluid catalytic cracking process with the additional regenerated catalyst circulation path for gasoline reprocessing and upgrading with minimum loss. Energy Fuels 34(1):235–244
Naik DV, Karthik V, Kumar V et al (2017) Kinetic modeling for catalytic cracking of pyrolysis oils with VGO in a FCC unit. Chem Eng Sci 170:790–798
Usman A, Siddiqui MAB, Hussain A et al (2017) Catalytic cracking of crude oil to light olefins and naphtha: experimental and kinetic modeling. Chem Eng Res Des 120:121–137
Sheng Q, Wang G, Liu Y et al (2018) Pilot-scale evaluation of hydrotreating inferior coker gas oil prior to its fluid catalytic cracking. Fuel 226:27–34
Maximov A, Tsivadze A, Fridman A et al (2020) The prospects for processing reservoir oil sludge into hydrocarbons by low-temperature hydrogenation in sorbing electrochemical matrices in comparison with conventional high-temperature hydrocracking. Energies 13(20):1–12
Bai P, Etim UJ, Yan Z et al (2018) Fluid catalytic cracking technology: current status and recent discoveries on catalyst contamination. Catal Rev 61(3):333–405
Zhang R, Zhang Y, Liu T et al (2022) Immobilization of vanadium and nickel in spent fluid catalytic cracking (SFCC) catalysts-based geopolymer. J Clean Prod 332:130112
Mancini G, Palmeri F, Benina G et al (2022) FCC spent catalyst as an alternative reagent in Mo-contaminated hazardous waste enhanced stabilization. Sustain Chem Pharm 28:100733
Maryutina TA, Katasonova ON, Savonina EY et al (2017) Present-day methods for the determination of trace elements in oil and its fractions. J Anal Chem 72(5):490–509
Ma Y, Liao Y, Su Y et al (2021) A novel method to investigate the activity tests of fresh FCC catalysts: an experimental and prediction process from lab scale to commercial scale. Processes 9(2):209
Oloruntoba A, Zhang Y, Hsu CS (2022) State-of-the-art review of fluid catalytic cracking (FCC) catalyst regeneration intensification technologies. Energies 15(6):1–75
Gambino M, Vesely M, Filez M, Oord R, Ferreira Sanchez D, Grolimund D et al (2020) Nickel poisoning of a cracking catalyst unravelled by single-particle X-ray fluorescence-diffraction-absorption tomography. Angew Chem Int Ed Engl 59(10):3922–3927
Senter C, Mastry MC, Zhang CC et al (2021) Role of chlorides in reactivation of contaminant nickel on fluid catalytic cracking (FCC) catalysts. Appl Catal A 611:117978
Etim UJ, Xu B, Bai P et al (2016) Role of nickel on vanadium poisoned FCC catalyst: a study of physiochemical properties. J Energy Chem 25(4):667–676
Liu Z, Zhang Z, Liu P et al (2015) Iron Contamination mechanism and reaction performance research on FCC catalyst. J Nanotechnol 2015: 1–6
Souza NLA, Paniago R, Ardisson JD et al (2019) Iron contamination of FCC catalysts: quantification of different crystalline phases and valence states. Appl Catal A 569:57–65
Zhou Q, Qi Y, Liu Q et al (2020) A detailed speciation of iron on FCC catalysts based on an integrated use of advanced characterisation methods and thermodynamic equilibrium simulation. Appl Catal A 599:117597
Liao Y, Liu T, Du X et al (2021) Distribution of iron on FCC catalyst and Its effect on catalyst performance. Front Chem 9:640413
Kharas K, Mastry MC, Thompson A et al (2022) Iron Tolerance in FCC Catalysts from in situ synthesis: a combined Mössbauer spectroscopy and catalytic testing investigation. Appl Catal A Gener 644:118743
Etim UJ, Bai P, Liu X et al (2019) Vanadium and nickel deposition on FCC catalyst: influence of residual catalyst acidity on catalytic products. Microporous Mesoporous Mater 273:276–285
Souza NLA, Tkach I, Morgado E et al (2018) Vanadium poisoning of FCC catalysts: a quantitative analysis of impregnated and real equilibrium catalysts. Appl Catal A 560:206–214
Wang T, Ren J, Ravindra AV et al (2022) Kinetics of Ni, V and Fe leaching from a spent catalyst in microwave-assisted acid activation process. Molecules 27(7):1–16
Liao Y, Liu T, Zhao H et al (2021) A comparison of laboratory simulation methods of iron contamination for FCC catalysts. Catalysts 11(1):104
Almas Q, Naeem MA, Baldanza MAS et al (2019) Transformations of FCC catalysts and carbonaceous deposits during repeated reaction-regeneration cycles. Catal Sci Technol 9(24):6977–6992
Tangstad E, Myrstad T, Spjelkavik AI et al (2006) Vanadium species and their effect on the catalytic behavior of an FCC catalyst. Appl Catal A 299:243–249
Lahnafi A, Elgamouz A, Tijani N et al (2020) Hydrothermal synthesis of zeolite A and Y membrane layers on clay flat disc support and their potential use in the decontamination of water polluted with toxic heavy metals. Desalin Water Treat 182:175–186
Meirer F, Morris DT, Kalirai S et al (2015) Mapping metals incorporation of a whole single catalyst particle using element specific X-ray nanotomography. J Am Chem Soc 137(1):102–105
Ihli J, Ferreira Sanchez D, Jacob RR et al (2017) Localization and speciation of iron impurities within a fluid catalytic cracking catalyst. Angew Chem Int Ed Engl 56(45):14031–14035
Cristiano-Torres DV, Osorio-Pérez Y, Palomeque-Forero LA et al (2008) The action of vanadium over Y zeolite in oxidant and dry atmosphere. Appl Catal A 346(1):104–111
Acknowledgements
This research was funded by the Key R&D program of Gansu Province (No.20YF8GD139). The experimental method and operation were supported by the Lanzhou Petrochemical Research Center.
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Key R& D program of Gansu Province, 20YF8GD139
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Yang, Y., Liu, C., Ma, X. et al. Multiple Performances of Metal Contamination for Nickel, Vanadium and Iron on FCC Catalysts. Catal Lett 154, 1061–1071 (2024). https://doi.org/10.1007/s10562-023-04371-6
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DOI: https://doi.org/10.1007/s10562-023-04371-6