Abstract
In this chapter, three case studies are presented: the first case presents computational fluid dynamics (CFD) modeling and simulation of a pharmaceutical bubbling bed drying process. The mathematical model used in Case1 is composed of the continuity, momentum, energy, and species transfer equations to simulate the flow pattern and heat and mass transfer in the pharmaceutical drying processes based on bubbling fluidized beds. Case 2 presents CFD modeling and simulation of a reactive gas–solid system in the riser section of a circulating fluidized bed (CFB) reactor representing a CO2 capture process using solid sorbents. In Case 3, a two-way coupled computational fluid dynamics-population balance equation (CFD-PBE) is presented following the second case where the density distribution of the solid phase is changing due to the chemical reaction (i.e., carbon capture) between the solid and gas phases.
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References
Abbasi E (2013) Computational fluid dynamics and population balance model for simulation of dry sorbent based CO2 capture process. Doctoral dissertation, Illinois Institute of Technology
Abbasi E, Hassanzadeh A, Abbasian J (2013) Regenerable MgO-based sorbent for high temperature CO2 removal from syngas: 2. Two-zone variable diffusivity shrinking core model with expanding product layer. Fuel 105:128–134
Abbasi E, Abbasian J, Arastoopour H (2015) CFD–PBE numerical simulation of CO2 capture using MgO-based sorbent. Powder Technol 286:616–628
Chen YM (2011) Evolution of FCC: past, present, and future-and the challenges of operating a high-temperature CFB system. In: Knowlton TM (ed) Proceeding of the tenth international conference on circulating fluidized beds and fluidization technology, CFB-10, ECI, New York
Extavour M, Bunje P (2016) CCUS: Utilizing CO2 to reduce emissions. Chem Eng Prog 112.6:55–59
Gunn DJ (1978) Transfer of heat or mass transfer to particles in fixed and fluidized beds. Int J Heat Mass Trans 21:467–476
Jang J, Arastoopour H (2014) CFD simulation of a pharmaceutical bubbling bed drying process at three different scales. Powder Technol 263:14–25
Johnson PC, Jackson R (1987) Frictional collisional constitutive relations for antigranulocytes-materials, with application to plane shearing. J Fluid Mech 176:67–93
Khotari KA (1967) M.Sc. Thesis, Chemical Engineering, Illinois Institute of Technology
Palancz B (1983) A mathematical-model for continuous fluidized-bed drying. Chem Eng Sci 38:1045–1059
Shadle L, Spenik J, Monazam E, et al. (2010) Approach to developing the C2U: a bench-scale carbon capture test unit using supported amine sorbents. NETL CO2 capture technology meeting, Pittsburgh, PA, 13–17 September 2010. http://www.netl.doe.gov/publications/proceedings/10/co2capture/presentations/monday/Lawrence%20Shadle-ORD.pdf. Accessed 29 June 2016
Sundaresan S (2011) Reflections on mathematical models and simulation of gas-particle flows. In: Knowlton TM (ed) Proceeding of the tenth international conference on circulating fluidized beds and fluidization technology, CFB-10, ECI, New York
Syamlal M, Rogers WA, O’Brien TJ (1993) MFIX documentation, vol 1. Theory Guide, Springfield, VA
Yi CK, Jo SJ, Seo Y et al (2007) Continuous operation of the potassium-based dry sorbent CO2 capture process with two fluidized-bed reactors. Int J Greenhouse Gas Control 1:31–36
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Arastoopour, H., Gidaspow, D., Abbasi, E. (2017). Case Studies. In: Computational Transport Phenomena of Fluid-Particle Systems. Mechanical Engineering Series. Springer, Cham. https://doi.org/10.1007/978-3-319-45490-0_5
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DOI: https://doi.org/10.1007/978-3-319-45490-0_5
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