Skip to main content
Log in

Analysis of gas flow behavior in an annular fluidized-bed reactor for polystyrene waste treatment

  • Special Feature: Original Article
  • Published:
Journal of Material Cycles and Waste Management Aims and scope Submit manuscript

Abstract

The characteristics of bubble properties and the chaotic flow behavior of gas were investigated in an annular fluidized bed (0.102 m in inner diameter and 2 m in height) because the behavior of gas flow in such a reactor is one of the important factors governing reactor operation, reactor performance, and the reaction itself. Pressure fluctuations as a state variable for the analysis of gas flow behavior were measured and analyzed. Bubble properties were determined by adopting the cross-correlation function of pressure fluctuations. The resultant chaotic flow behavior of gas was interpreted by means of chaotic parameters such as the Kolmogorov entropy. It was found that the Kolmogorov entropy could be utilized effectively to explain the nonlinear dynamic behavior of gas-solid flow in the annular fluidized bed. The pierced length and rising velocity of bubbles increased with increasing gas velocity, bed temperature, and particle size of the bed material. The bubble frequency increased with increasing gas velocity and bed temperature, while it decreased with increasing particle size of the bed material. Correlations to predict the bubble properties in annular fluidized-bed reactors were suggested.

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

Access this article

Price excludes VAT (USA)
Tax calculation will be finalised during checkout.

Instant access to the full article PDF.

Similar content being viewed by others

References

  1. Lee CG, Kang SH, Kim JS, Yun JS, Kang Y, Choi MJ (2004) Characteristics of catalytic pyrolysis of polystyrene. J Korean Ind Eng Chem 15:188–193

    CAS  Google Scholar 

  2. Lee CG, Kang SH, Kim JS, Choi MJ, Kang Y (2006) Treatment of polystyrene waste in a fluidized-bed/CSTR multiple-reactor process. J Korea Soc Waste Manag 23:486–492

    Google Scholar 

  3. Kang SH, Son SM, Song PS, Kang Y, Choi MJ (2006) Pyrolysis for the recycling of polystyrene plastic (PSP) wastes in a swirling fluidized-bed reactor. Stud Surf Sci Catal 159:529–532

    Article  CAS  Google Scholar 

  4. Lee CG, Cho YJ, Song PS, Kang Y, Kim JS, Choi MJ (2003) Effects of temperature distribution on the catalytic pyrolysis of polystyrene waste in a swirling fluidized-bed reactor. Catal Today 79:453–464

    Article  Google Scholar 

  5. Kunii D, Levenspiel O (1991) Fluidization engineering. Butterworth-Heinemann, Boston, pp 4–58

    Google Scholar 

  6. Wu B, He Z, Kantzas A, Bellehumeur CT, Kryuchkov S (2006) Hydrodynamics in a gas-solid fluidized bed using X-ray fluoroscopy and pressure fluctuation measurements. Macromol Symp 243:35–45

    Article  CAS  Google Scholar 

  7. Yang WC (2003) Handbook of fluidization and fluid-particle systems. Dekker, New York, pp 53–112

    Google Scholar 

  8. Andreux R, Chavuki J (2008) Behaviors of the bubble, cloud and emulsion phases in a fluidized bed. AIChE J 54:406–414

    Article  CAS  Google Scholar 

  9. Bi HT, Ellis N, Abba IA, Grace JR (2000) A state-of-the art review of gas-solid turbulent fluidization. Chem Eng Sci 55:4789–4825

    Article  CAS  Google Scholar 

  10. Formisani B, Girimont R, Pataro G (2002) The influence of operating temperature on the dense phase properties of bubbling fluidized beds of solids. Powder Technol 125:28–38

    Article  CAS  Google Scholar 

  11. Yates JG, Cheesman DJ, Lettieri P, Newton D (2002) X-ray analysis of fluidized and other multiphase systems. Koma 20:133–143

    Google Scholar 

  12. King DF, Mitchell FRG, Harrison D (1981) Dense phase viscosities of fluidized beds at elevated pressures. Powder Technol 28:55–58

    Article  Google Scholar 

  13. Piepers HW, Cottaar EJE, Verkooijen AHM, Rietema K (1984) Effects of pressure and type of gas on particle-particle interaction and the consequences for gas-solid fluidization behavior. Powder Technol 37:55–70

    Article  CAS  Google Scholar 

  14. Chan IH, Sishtla C, Knowlton TM (1987) The effect of pressure on bubble parameters in gas-fluidized beds. Powder Technol 53:217–235

    Article  CAS  Google Scholar 

  15. Kang SH, Kang Y, Jin GT, Yi CG, Han KH (2003) Heat transfer characteristics of the horizontal tube in a pressurized fluidized bed. J Korean Ind Eng Chem 14:475–480

    CAS  Google Scholar 

  16. Kang SH, Kim JS, Kim SJ, Kang Y (2001) Analysis of dispersion behavior of fluidized particles in gas-solid fluidized bed. J Korean Ind Eng Chem 12:584–589

    CAS  Google Scholar 

  17. Fan LT, Ho TC, Walawender WP (1983) Measurements of the rise velocities of bubbles, slugs and pressure waves in a gas-solid fluidized bed using pressure fluctuation signals. AIChE J 29:33–39

    Article  CAS  Google Scholar 

  18. Horio M, Nonaka A (1987) A generalized bubble diameter correlation for gas-solid fluidized beds. AIChE J 33:1865–1871

    Article  CAS  Google Scholar 

  19. Kang SH, Kang Y, Han KH, Jin GT (2004) Effects of pressure on the minimum fluidization velocity and bubble properties in a gas-solid fluidized bed. J Ind Eng Chem 10:330–336

    CAS  Google Scholar 

  20. Werther J, Merlus O (1973) The local structure of gas fluidized beds II. The spatial distribution of bubbles. Int J Multiphase Flow 1:123

    Article  Google Scholar 

  21. Fan LT, Ho TC, Hiraoka S, Walawender WP (1981) Pressure fluctuations in a fluidized bed. AIChE J 27:388–396

    Article  Google Scholar 

  22. Ott E, Sauer T, Yorke JA (1994) Coping with chaos. Wiley, New York, pp 18–39

    Google Scholar 

  23. Grassberger P, Procaccia I (1983) Measuring the strangeness of strange attractors. Physica D 9:189–194

    Article  Google Scholar 

  24. Fuller TA, Flynn TJ, Daw CS (1996) Analysis of dynamic boiler measurements: a practical approach. Chem Eng J 64:179–189

    CAS  Google Scholar 

  25. Clark NN, Mckenzie EA, Gautam M (1991) Differential pressure measurements in a slugging fluidized bed. Powder Technol 67: 187–199

    Article  CAS  Google Scholar 

  26. Kang Y, Cho YJ, Woo KJ, Kim SD (1999) Diagnosis of bubble distribution and mass transfer in pressurized bubble columns with viscous liquid medium. Chem Eng Sci 54:4887–4893

    Article  CAS  Google Scholar 

  27. Kang Y, Cho YJ, Woo KJ, Kim KI, Kim SD (2002) Bubble properties and pressure fluctuations in pressurized bubble columns. Chem Eng Sci 55:411–419

    Google Scholar 

  28. Cho YJ, Woo KJ, Kang Y, Kim SD (2002) Dynamic characteristics of heat transfer coefficient in pressurized bubble columns with viscous liquid medium. Chem Eng Process 41:699–706

    Article  CAS  Google Scholar 

  29. Son SM, Kang SH, Kim UY, Kang Y, Kim SD (2007) Bubble properties in three-phase inverse fluidized beds with viscous liquid medium. Chem Eng Process 46:736–741

    Article  CAS  Google Scholar 

Download references

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to Yong Kang.

Rights and permissions

Reprints and permissions

About this article

Cite this article

Son, S.M., Kim, U.Y., Shin, I.S. et al. Analysis of gas flow behavior in an annular fluidized-bed reactor for polystyrene waste treatment. J Mater Cycles Waste Manag 11, 138–143 (2009). https://doi.org/10.1007/s10163-008-0226-0

Download citation

  • Received:

  • Accepted:

  • Published:

  • Issue Date:

  • DOI: https://doi.org/10.1007/s10163-008-0226-0

Key words

Navigation