Bed expansion characteristics and transition velocity in turbulent fluidized beds
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In-situ gas flow separation between biochar and the heat carrier in a circulating fluidized bed reactor for biomass pyrolysis
2023, Chemical Engineering JournalA state-of-the-art review on transition between the fast fluidization and pneumatic transport of Geldart group B particles
2023, ParticuologyCitation Excerpt :As can be seen, the correlations of Adanez (Adanez et al., 1993) and Monazam and Shadle (Monazam & Shadle, 2011) overestimate the values of utr in the whole range of Ar possibly due to the high Re of the experimental data points obtained in these two studies. Contrarily, the correlations of Lee and Kim (Lee & Kim, 1990) and Seo (Seo et al., 2014) underestimate the values of utr in a certain range of Ar (Ar > 1000) for the scarcity of experimental data points used for fitting in the corresponding Ar range. Generally speaking, the correlations of Perales (Perales et al., 1991), Bi and Fan (Bi & Fan, 1992), Bi and Grace (Bi & Grace, 1995), and Smolders and Baeyens (Smolders & Baeyens, 2001) can give relatively good prediction results for Geldart group B particles.
Saturation carrying capacity Group B particles in a circulating fluidized bed
2021, Powder TechnologyCitation Excerpt :Eqs. (2), (3) and (4) have been shown to be true experimentally by numerous researchers [3–7], [14–16] and generates the curve shown in Fig. 2 of Gs* vs Ug. Likewise, Eq. (5) has been shown to be true by numerous researchers [7–13]. Eqs. (3) and (4), reported by numerous researchers [3–7], define the point (Uck, Gs⁎,ck) as shown in Fig. 2 when Ug = Utr1 = Uck.
Regimes of large-scale fluidized beds for solid fuel conversion
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