Skip to main content

Series of MIP Process

  • Chapter
  • First Online:
Diameter-Transformed Fluidized Bed

Part of the book series: Particle Technology Series ((POTS,volume 27))

  • 302 Accesses

Abstract

This Chapter introduces a series of FCC processes based on the DTFB engineering platform. Starting from the FCC process with two reaction zones by creating the cracking and conversion reaction zones in the DTFB reactor, the process for maximizing Iso-paraffins (MIP), process for cleanser gasoline and propylene production (CGP), process for light cycle oil (LCO) to gasoline production (LTG), process for dry gas and coke reduction (DCR), the fine fluidized catalytic cracking (fFCC) process, and catalytic cracking process for producing gasoline with ultra-low olefins (Ultra LOF) have been successfully developed.

This is a preview of subscription content, log in via an institution to check access.

Access this chapter

Chapter
USD 29.95
Price excludes VAT (USA)
  • Available as PDF
  • Read on any device
  • Instant download
  • Own it forever
eBook
USD 149.00
Price excludes VAT (USA)
  • Available as EPUB and PDF
  • Read on any device
  • Instant download
  • Own it forever
Softcover Book
USD 199.99
Price excludes VAT (USA)
  • Compact, lightweight edition
  • Dispatched in 3 to 5 business days
  • Free shipping worldwide - see info
Hardcover Book
USD 199.99
Price excludes VAT (USA)
  • Durable hardcover edition
  • Dispatched in 3 to 5 business days
  • Free shipping worldwide - see info

Tax calculation will be finalised at checkout

Purchases are for personal use only

Institutional subscriptions

References

  1. Chen, J.W., Xu, Y.H. (eds.): Catalytic Cracking Process and Engineering (in Chinese), 3rd edn. China Petrochemical Press, Beijing (2015)

    Google Scholar 

  2. Cao, X.H.: The choice of China’s gasoline production process for the future. Pet Process Petrochem (in Chinese). 43(8), 1–6 (2012)

    CAS  Google Scholar 

  3. Scherzer, J.: Octane-enhancing, zeolitic FCC catalysts: scientific and technical aspects. Catal. Rev. Sci. Eng. 31(3), 215–354 (1989)

    Article  CAS  Google Scholar 

  4. Xu, Y.H., Zhang, J.S., Long, J.: A modified FCC process MIP for maximizing iso-paraffins in cracked naphtha. Pet Process Petrochem (in Chinese). 32(8), 1–5 (2001)

    CAS  Google Scholar 

  5. Xu, Y.H., Cui, S.Y.: A novel fluid catalytic cracking process for maximizing isoparaffins: from fundamentals to commercialization. Front. Chem. Sci. Eng. 12(1), 9–23 (2018)

    Article  CAS  Google Scholar 

  6. Xu, Y.H.: Study on the effect of hydrogen transfer reaction on olefin conversion. Pet Process Petrochem (in Chinese). 33(1), 38–41 (2002)

    Google Scholar 

  7. Xu, Y.H., Zhang, J.S., Xu, H., Hao, X.R.: Commercial application of a novel FCC process for maximizing iso-paraffin in cracked naphtha. Pet Process Petrochem (in Chinese). 34(11), 1–6 (2003)

    Google Scholar 

  8. Xu, Y.H., Zhang, J.S., Long, J., He, M.Y., Xu, H., Hao, X.R.: Development and commercial application of FCC process for maximizing iso-paraffins (MIP) in cracked naphtha. Eng Sci (in Chinese). 5(5), 55–58 (2003)

    Google Scholar 

  9. Xu, Y.H., Zhang, J.S., Ma, J.G., Long, J.: Catalytic cracking technology for producing naphtha with clean gasoline composition and increasing propylene. Pet Process Petrochem (in Chinese). 35(9), 1–4 (2004)

    Google Scholar 

  10. Xu, Y.H., Zhang, J.S., Ma, J.G., Long, J., He, M.Y.: Controllability of cracking reaction in MIP process. Acta Pet Sin (Pet Process Sect, in Chinese). 20(3), 1–6 (2004)

    Google Scholar 

  11. Xu, Y.H.: Chemistry and Process of Catalytic Cracking (in Chinese). Science Press, Beijing (2013)

    Google Scholar 

  12. Yang, J., Xie, X.D., Cai, Z., Xu, Y.H.: Commercial trial of MIP-CGP. Pet Process Petrochem (in Chinese). 37(8), 54–59 (2006)

    Google Scholar 

  13. Dai, B.H., Shi, J.L., Xu, Y.H., Liu, X.L.: Commercialization of maximum isoparaffin process for cleaner gasoline and more propylene. Petrochem Technol (in Chinese). 35(7), 665–669 (2006)

    CAS  Google Scholar 

  14. Cui, S.Y., Xu, Y.H.: Study on the selective catalytic conversion of light diesel fraction. Pet Process Petrochem (in Chinese). 40(12), 1–7 (2009)

    CAS  Google Scholar 

  15. Jiang, N., Xu, Y.H., Cui, S.Y.: Study on parameters of MIP-LTG process for maximizing gasoline. Pet Process Petrochem (in Chinese). 45(3), 35–39 (2014)

    CAS  Google Scholar 

  16. Cui, S.Y., Xu, Y.H., Liu, X.L., Yang, Y.N., Liu, S.J.: A Catalytic Conversion Method for Reducing Benzene Content in Gasoline. China, 2009, CN200710120108.4

    Google Scholar 

  17. Cui, S.Y., Xu, Y.H.: Experimental study on catalytic cracking of hydrogenated LCO mixed with hydrogenated VGO. Pet Process Petrochem (in Chinese). 49(9), 1–5 (2018)

    Google Scholar 

  18. Cui S.Y., Xu Y.H., Liu X.L., Yang Y.N., Liu S.J.: A Catalytic Conversion Method for Producing High Octane Number Gasoline. China, 2009, CN200710120107. X

    Google Scholar 

  19. Pan, L.Q., Yan, G., Nie, B.Q., Cui, S.Y.: Commercial application of recycling light diesel fraction to enhance octane gasoline yield in MIP unit. Pet Process Petrochem (in Chinese). 42(1), 33–36 (2011)

    Google Scholar 

  20. Zhu, X.Y., Liu, Z.L., Xu, Y.Q., Liu, Y.R., Tian, S.B.: Diesel detailed analysis by GC field ionization time-of-flight high-resolution mass spectrometry. Acta Pet Sin (Pet Process Sect, in Chinese). 26(2), 277–282 (2010)

    CAS  Google Scholar 

  21. Song, C.Y.: Study on conversion technology for low-quality FCC diesel. Pet Ref Eng (in Chinese). 46(10), 7–12 (2016)

    Google Scholar 

  22. Shen, X., Xia, J.P., Liu, J.M., Wu, L.C.: Commercial application of blending hydrotreated diesel into FCCU feed to increase gasoline production. Pet Ref Eng (in Chinese). 47(2), 35–38 (2017)

    Google Scholar 

  23. Xu, Y.H., Gong, J.H., Zhang, J.S., Long, J.: Study on the MIP process for reducing dry gas and coke yields. Pet Process Petrochem (in Chinese). 38(10), 7–11 (2007)

    CAS  Google Scholar 

  24. Gong, J.H., Xu, Y.H., Cai, Z., Xie, K.Q.: Development and commercial application of MIP-DCR process. Pet Process Petrochem (in Chinese). 44(3), 6–11 (2013)

    CAS  Google Scholar 

  25. Haag, W.O., Dessau, R.M.: Duality of mechanism for acid-catalyzed cracking. In: Proceedings of the 8th International Congress on Catalysis. Dechema, Frankfurt am Main (1984)

    Google Scholar 

  26. Lercher, J.A., Van Santen, R.A., Vinek, H.: Carbonium ion formation in zeolite catalysis. Catal. Lett. 27(1), 91–96 (1994)

    Article  CAS  Google Scholar 

  27. Corma, A., Orchillés, A.V.: Current views on the mechanism of catalytic cracking. Microporous Mesoporous Mater. 35–36, 21–30 (2000)

    Article  Google Scholar 

  28. Wielers, A.F.H., Vaarkamp, M., Post, F.M.: Relation between properties and performance of zeolites in paraffin cracking. J. Catal. 127(1), 51–56 (1991)

    Article  CAS  Google Scholar 

  29. Cao, X.H.: Constructing a green low carbon, rational layout transportation fuel production system. Pet Pet Today (in Chinese). 24(4), 1–9 (2016)

    Google Scholar 

  30. Li, Z.Y., Huang, G.S., Ren, W.P., Wang, H.Q.: The structure adjustment and development of China’s oil refining and petrochemical industry during the 13th five-year plan period. Int Petrol Econ (in Chinese). 24(9), 88–96 (2016)

    Google Scholar 

  31. Li, Y.L.: Technologies and measures for increasing gasoline production. Pet Process Petrochem (in Chinese). 48(5), 60–69 (2017)

    Google Scholar 

  32. Xu, Y.H., Dai, L.S., Long, J., Nie, H.: Integrated technology (IHCC) of hydrotreating FCC gas oil and highly selective catalytic cracking for maximizing liquid yield. Pet Process Petrochem (in Chinese). 42(3), 7–12 (2011)

    CAS  Google Scholar 

  33. Xu, Y.H., Wang, X., Zhang, Y.Y., Liu, T.: Study on fine fluid catalytic cracking technology. Pet Process Petrochem (in Chinese). 49(10), 1–8 (2018)

    CAS  Google Scholar 

Download references

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to Youhao Xu .

Rights and permissions

Reprints and permissions

Copyright information

© 2020 Springer Nature Switzerland AG

About this chapter

Check for updates. Verify currency and authenticity via CrossMark

Cite this chapter

Xu, Y., He, M. (2020). Series of MIP Process. In: Diameter-Transformed Fluidized Bed. Particle Technology Series, vol 27. Springer, Cham. https://doi.org/10.1007/978-3-030-47583-3_6

Download citation

Publish with us

Policies and ethics