Abstract
This Chapter introduces how to determine the key design parameters of the diameter-transformed fluidized bed (DFB) reactors, i.e., the diameter expanding ratio and the height of multiple reaction zones, based on the “choking” phenomenon captured by numerical investigation with multiscale CFD simulations. To achieve the steady operation in multiple reaction zones, related ancillary techniques are subsequently developed, such as the distributor installed between the first reaction zone and second reaction zone. Meanwhile, the proprietary catalysts are also being developed. The FCC process with two reaction zones, effective utilization of heavy oil and light-olefin production process are exploited in succession by using the DTFB as the core reactor.
Access this chapter
Tax calculation will be finalised at checkout
Purchases are for personal use only
References
Wang, W., Lu, B., Zhang, N., Shi, Z., Li, J.: A review of multiscale CFD for gas-solid CFB modeling. Int J. Multiphase Flow. 36(2), 109–118 (2010)
Chen, J.W., Xu, Y.H. (eds.): Catalytic cracking process and engineering (in Chinese), 3rd edn. China Petrochemical Press, Beijing (2015)
Karri, S.B.R., Knowlton, T.M.: In: Yang W.-C (ed.) Gas distributor and plenum design in fluidized beds, in Fluidization, Solids Handling, and Processing, pp. 209–235. William Andrew Publishing, Westwood (1999)
Sadeghbeigi, R.: Fluid catalytic cracking handbook, 3rd edn. Elsevier, Amsterdam (2012)
Xu, Y.H., Yu, B.D., Zhang, Z.G.: Advance in China fluid catalytic cracking (FCC) process. Scientia Sinica (Chimica). 44(1), 13–24 (2014)
Xu, Y.H.: Chemistry and Process of Catalytic Cracking (in Chinese). Science Press, Beijing (2013)
Molecular sieve group (Dalian Institute of Chemical Physics C.A.o.S., Zeolite (in Chinese). Science Press, Beijing (1978)
Qian, B.Z.: MIP revamping of heavy oil catalytic cracking unit in Fushun petrochemical company of PetroChina. Petroleum Refinery Eng. (in Chinese). 41(02), 56 (2011)
Mi, Y.Z.: Study on optimization technology of 1.2Mt/a vacuum residue RFCC unit. Energy Chem. Indust. (in Chinese). 36(2), 35–38 (2015)
Sun, S.H., Song, S.K., Shen, Z.F.: Industrial application of MIP series technologies in FCC units. China Petrochemical Press, Beijing (2017)
Treese, S.A., Pujadó, P.R., David, S.J.J. (eds.): Handbook of petroleum processing, 2nd edn. Springer, Cham (2015)
Dharia, D., Long, J., Xu, Y.H., Zhang, J.S., Yuan, E., Gim, S., Xu, S.: Consider new processes for clean gasoline and olefins production. Hydrocarb. Process. 9, 85–90 (2011)
Xie, Z.K., Zhou, X.G., Chen, F.Q.: Light olefins fundamentals of catalytic processes (in Chinese). China Petrochemical Press, Beijing (2013)
Xu, Y.H., Qu, J.H., Yang, Y.T., Xu, L.: Composition characteristics and octane number analysis of MIP series technical gasoline. Petroleum Process. Petrochem. (in Chinese). 40(1), 10–14 (2009)
Xu, Y.H., Wang, X., Zhang, Y.Y., Liu, T.: Study on fine fluid catalytic cracking technology. Petroleum Process. Petrochem. (in Chinese). 49(10), 1–8 (2018)
Xu, Y.H., Xu, L., Wang, X., Xu, G.L.: Key technologies and development of China's vehicle gasoline quality upgrading. Petroleum Process. Petrochem. (in Chinese). 50(2), 1–11 (2019)
Author information
Authors and Affiliations
Corresponding author
Rights and permissions
Copyright information
© 2020 Springer Nature Switzerland AG
About this chapter
Cite this chapter
Xu, Y., He, M. (2020). Engineering Aspects and Application of DTFB. In: Diameter-Transformed Fluidized Bed. Particle Technology Series, vol 27. Springer, Cham. https://doi.org/10.1007/978-3-030-47583-3_5
Download citation
DOI: https://doi.org/10.1007/978-3-030-47583-3_5
Published:
Publisher Name: Springer, Cham
Print ISBN: 978-3-030-47582-6
Online ISBN: 978-3-030-47583-3
eBook Packages: Chemistry and Materials ScienceChemistry and Material Science (R0)