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The impact of particle size in fluidized bed on heat transfer behavior: a review

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Warianty tytułu
PL
Wpływ wielkości cząstek w złożu fluidalnym na przenoszenia ciepła: przegląd
Języki publikacji
EN
Abstrakty
EN
This review paper explores the significance of fluidized bed heat exchangers in various industrial applications. By delving into the operation of fluidized beds as multiphase flow systems, the aim is to enhance their capabilities and efficiency. Key parameters such as minimum fluidization velocity and local gas holdup are crucial for characterizing the hydrodynamic behavior of materials within fluidized beds. Fluidization, achieved by passing atmospheric air through particulate solids, imparts fluid-like properties to the bed. Fluidized beds serve as reactors where this phenomenon takes place, offering several advantages in industrial processes, including high rates of heat and mass transfer, low pressure drops, and uniform temperature distribution. In future work, a focus on understanding and optimizing the fluidization process will contribute to further advancements in the performance of fluidized bed heat exchangers.
PL
W artykule przedstawiono przegląd literatury dotyczący znaczenia wymienników ciepła ze złożem fluidalnym w różnych zastosowaniach przemysłowych. Zwiększenie możliwości i wydajności złóż fluidalnych jest celem badań tych wielofazowych systemów przepływowych. Kluczowe parametry, takie jak minimalna prędkość fluidyzacji i lokalne zatrzymywanie gazu, mają kluczowe znaczenie dla scharakteryzowania zachowania hydro-dynamicznego materiałów w złożach fluidalnych. Fluidyzacja, osiągnięta poprzez przepuszczanie powietrza atmosferycznego przez cząstki stałe, nadaje złożu właściwości zbliżone do płynu. Złoża fluidalne służą jako reaktory, w których zachodzi zjawisko fluidyzacji, oferując szereg korzyści w procesach przemysłowych, w tym wysokie szybkości wymiany ciepła i masy, niskie spadki ciśnienia i równomierny rozkład temperatury. W przyszłych pracach skupienie się na zrozumieniu i optymalizacji procesu fluidyzacji przyczyni się do dalszego postępu w wydajności wymienników ciepła ze złożem fluidalnym.
Rocznik
Strony
39--46
Opis fizyczny
Bibliogr. 38 poz., rys., tab.
Twórcy
  • Northern Technical University/Technical College of Engineering, Kirkuk, Iraq
  • Northern Technical University/Technical College of Engineering, Kirkuk, Iraq
Bibliografia
  • 1. Al-Busoul, M., & Abu-Ein, S. (2003). Local heat transfer coefficients around a horizontal heated tube immersed in a gas fluidized bed. Heat and Mass Transfer Journal, 39, 355–358. https://doi.org/10.1007/s00231-002-0330-y
  • 2. Andersson, B. Å. (1996). Effects of bed particle size on heat transfer in circulating fluidized bed boilers. Powder Technology, 87(3), 239–248. https://doi.org/10.1016/0032-5910(96)03092-6
  • 3. Arena, U. (2013). 17 - Fluidized bed gasification. In F. Scala (Ed.). Fluidized bed gasification. fluidized bed technologies for near-zero emission combustion and gasification (pp. 765–812). Woodhead Publishing Limited.
  • 4. Baskakov, P., Berg, B. V., Vitt, O. K., Filippovsky, N. F., Kirakosyan, V. A., Goldobin, J. M., & Maskaev, V. K. (1973). Heat transfer to objects immersed in fluidized beds. Powder Technology, 8(5–6), 273–282. https://doi.org/10.1016/0032-5910(73)80092-0
  • 5. Berkache, A., Amroune, S., Golbaf, A., & Mohamad, B. (2022). Experimental and numerical investigations of a turbulent boundary layer under variable temperature gradients. Journal of the Serbian Society for Computational Mechanics, 16(1), 1–15. https://doi.org/10.24874/jsscm.2022.16.01.01
  • 6. Blaszczuk, A., & Jagodzik, S. (2021). Investigation of heat transfer in a large-scale external heat exchanger with horizontal smooth tube bundle. Energies, 14(17), Article 5553. https://doi.org/10.3390/en14175553
  • 7. Blaszczuk, A., Pogorzelec, M., & Shimizu, T. (2018). Heat transfer characteristics in a large-scale bubbling fluidized bed with immersed horizontal tube bundles. Energy, 162, 10−19. https://doi.org/10.1016/j.energy.2018.08.008
  • 8. Cai, R., Zhang, M., Ge, R., Zhang, X., Cai, J., Zhang, Y., Huang, Y., Yang, H., & Lyu, J. (2019). Experimental study on local heat transfer and hydrodynamics with single tube and tube bundles in an external heat exchanger. Applied Thermal Engineering, 149, 924−938. https://doi.org/10.1016/j.applthermaleng.2018.12.040
  • 9. Chen, P., & Pei, D. C. T. (1985). A model of heat transfer between fluidized beds and immersed surfaces. International Journal of Heat and Mass Transfer, 28(3), 675–682. https://doi.org/10.1016/0017-9310(85)90189-9
  • 10. Cui, Y., Liu, X., & Zhong, W. (2020). Simulations of coal combustion in a pressurized supercritical CO2 circulating fluidized bed. Energy & Fuels, 34(4), 4977−4992. https://doi.org/10.1021/acs.energyfuels.0c00418
  • 11. Das, H. J., Mahanta, P., Saikia, R., & Aamir, M. S. (2020). Performance evaluation of drying characteristics in conical bubbling fluidized bed dryer. Powder Technology, 374, 534−543. https://doi.org/10.1016/j.powtec.2020.06.051
  • 12. Devaru, C. B., & Kolar, A. K. (1995, May 7-10). Heat transfer from a horizontal finned tube bundle in bubbling fluidized beds of small and large particles. Proceedings of the 13th International Conference on Fluidized-Bed Combustion, Orlando, FL, USA.
  • 13. Dietrich, F., Schöny, G., Fuchs, J., & Hofbauer, H. (2018). Experimental study of the adsorber performance in a multi-stage fluidized bed system for continuous CO2 capture by means of temperature swing adsorption. Fuel Processing Technology, 173, 103−111. https://doi.org/10.1016/j.fuproc.2018.01.013
  • 14. Foroughi-Dahr, M., Mostoufi, N., Sotudeh-Gharebagh, R., & Chaouki, J. (2017). Particle coating in fluidized beds. In Reference Module in Chemistry, Molecular Sciences and Chemical Engineering. Elsevier. https://doi.org/10.1016/B978-0-12-409547-2.12206-1
  • 15. Hou, Q. F., Zhou, Z. Y., & Yu, A. B. (2016). Gas–solid flow and heat transfer in fluidized beds with tubes: Effects of material properties and tube array settings. Powder Technology, 296, 59−71. https://doi.org/10.1016/j.powtec.2015.03.028
  • 16. Kim, S. W., Ahn, J. Y., Kim, S. D., & Lee, D. H. (2003). Heat transfer and bubble characteristics in a fluidized bed with immersed horizontal tube bundle. International Journal of Heat and Mass Transfer, 46(3), 399–409. https://doi.org/10.1016/S0017-9310(02)00296-X
  • 17. Kunii, D., & Levenspiel, O. (1991). Fluidization engineering (2nd ed.). Butterworth-Heinemann. https://doi.org/10.1016/C2009-0-24190-0
  • 18. Li, D., Cai, R., Zhang, M., Yang, H., Choi, K., Ahn, S., & Jeon, C. H. (2020). Operation characteristics of a bubbling fluidized bed heat exchanger with internal solid circulation for a 550-MWe ultrasupercritical CFB boiler. Energy, 192, Article 116503. https://doi.org/10.1016/j.energy.2019.116503
  • 19. Miri, R., Mliki, B., Mohamad, B. A., Abbassi, M. A., Oreijah, M., Guedri, K., & Abderafi, S. (2023). Entropy generation and heat transfer rate for MHD forced convection of nanoliquid in the presence of the viscous dissipation term. CFD Letters, 15(12), 77–106. https://doi.org/10.37934/cfdl.15.12.77106
  • 20. Mohammed, F. Z., Hussein, A. M., Danook, S. H., & Mohamad, B. (2023). Characterization of a flat plate solar water heating system using different nano-fluids. AIP Conference Proceedings, 2901(1), Article 100018. https://doi.org/10.1063/5.0178901
  • 21. Mu, L., Buist, K. A., Kuipers, J. A. M., & Deen, N. G. (2020). Hydrodynamic and heat transfer study of a fluidized bed by discrete particle simulations. Processes, 8(4), Article 463. https://doi.org/10.3390/pr8040463
  • 22. Nag, P. K., Ali, M. N., Basu, P. (1995). A mathematical model for the prediction of heat transfer from finned surfaces in a circulating fluidized bed. International Journal of Heat and Mass Transfer, 38(9), 1675–1681. https://doi.org/10.1016/0017-9310(94)00284-3
  • 23. Nag, P. K., & Moral, M. (1990). The influence of rectangular fins on heat transfer in circulating fluidized bed boilers. Journal of the Institute of Energy, 143–147.
  • 24. Ngoh, J., & Lim, E. W. C. (2016). Effects of particle size and bubbling behavior on heat transfer in gas fluidized beds. Applied Thermal Engineering, 105, 225–242. https://doi.org/10.1016/j.applthermaleng.2016.05.165
  • 25. Ozkaynak, T. F., & Chen, J. C. (1980). Emulsion phase residence time and its use in heat transfer models in fluidized beds. AIChE Journal, 26(4), 544–550. https://doi.org/10.1002/aic.690260404
  • 26. Papadikis, K., Gu, S., & Bridgwater, A. V. (2010). Computational modelling of the impact of particle size to the heat transfer coefficient between biomass particles and a fluidised bed. Fuel Processing Technology, 91(1), 68–79. https://doi.org/10.1016/j.fuproc.2009.08.016
  • 27. Park, S. H., Yeo, C. E., Lee, M. J., & Kim, S. W. (2020). Effect of bed particle size on thermal performance of a directly-irradiated fluidized bed gas heater. Processes, 8(8), Article 967. https://doi.org/10.3390/pr8080967
  • 28. Pence, D. V., Beasley, D. E., & Figliola, R. S. (1994). Heat transfer and surface renewal dynamics in gas-fluidized beds. ASME Journal of Heat and Mass Transfer, 116(4), 929–937. https://doi.org/10.1115/1.2911468
  • 29. Pröll, T., Schöny, G., Sprachmann, G., & Hofbauer, H. (2016). Introduction and evaluation of a double loop staged fluidized bed system for post-combustion CO2 capture using solid sorbents in a continuous temperature swing adsorption process. Chemical Engineering Science, 141, 166−174. https://doi.org/10.1016/j.ces.2015.11.005
  • 30. Qader, F. F., Mohamad, B., Hussein, A. M., & Danook, S. H. (2023). Numerical study of heat transfer in a circular pipe filled with porous medium. Pollack Periodica. Online first: https://doi.org/10.1556/606.2023.00869
  • 31. Rasouli, S., Golriz, M. R., & Hamidi, A. A. (2005). Effect of annular fins on heat transfer of horizontal immersed tube in bubbling fluidized beds. Powder Technology, 154(1), 9–13. https://doi.org/10.1016/j.powtec.2005.02.008
  • 32. Samanta, A., Zhao, A., Shimizu, G. K. H., Sarkar, P., & Gupta, R. (2012). Post-combustion CO2 capture using solid sorbents: A review. Industrial & Engineering Chemistry Research, 51(4), 1438−1463. https://doi.org/10.1021/ie200686q
  • 33. Saxena, S. C. (1989). Heat transfer between immersed surfaces and gas-fluidized beds. Advances in Heat Transfer, 19, 97–190. https://doi.org/10.1016/S0065-2717(08)70212-0
  • 34. Schöny, G., Zehetner, E., Fuchs, J., Pröll, T., Sprachmann, G., & Hofbauer, H. (2016). Design of a bench scale unit for continuous CO2 capture via temperature swing adsorption—Fluid-dynamic feasibility study. Chemical Engineering Research and Design, 106, 155−167. https://doi.org/10.1016/j.cherd.2015.12.018
  • 35. Sjösten, J., Golriz, M. R., Nordin, A., & Grace, J. R. (2004). Effect of particle coating on fluidized-bed heat transfer. Industrial & Engineering Chemistry Research, 43(18), 5763−5769. https://doi.org/10.1021/ie034317u
  • 36. Wormsbecker, M., Pugsley, T., & Tanfara, H. (2009). Interpretation of the hydrodynamic behaviour in a conical fluidized bed dryer. Chemical Engineering Science, 64(8), 1739−1746. https://doi.org/10.1016/j.ces.2008.11.025
  • 37. Yusuf, R., Melaaen, M. C., & Mathiesen, V. (2005). Convective heat and mass transfer modeling in gas-fluidized beds. Chemical Engineering Technology, 28(1), 13–24. https://doi.org/10.1002/ceat.200407014
  • 38. Zerobin, F., & Pröll, T. (2020). Concentrated carbon dioxide (CO2) from diluted sources through continuous temperature swing adsorption (TSA). Industrial & Engineering Chemistry Research, 59(19), 9207−9214. https://doi.org/10.1021/acs.iecr.9b06177
Uwagi
PL
Opracowanie rekordu ze środków MNiSW, umowa nr SONP/SP/546092/2022 w ramach programu "Społeczna odpowiedzialność nauki" - moduł: Popularyzacja nauki i promocja sportu (2024).
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-faeaba1e-ab18-4009-975c-8f1b31d7e758
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