Tracer studies of high-shear granulation: II. Population balance modeling

被引:134
作者
Hounslow, MJ [1 ]
Pearson, JMK
Instone, T
机构
[1] Univ Sheffield, Dept Chem & Proc Engn, Particle Prod Grp, Sheffield, S Yorkshire, England
[2] Univ Cambridge, Dept Chem Engn, Cambridge, England
关键词
D O I
10.1002/aic.690470910
中图分类号
TQ [化学工业];
学科分类号
0817 [化学工程与技术];
摘要
A population balance framework developed describes the tracer studies in Pail I A two internal coordinate population balance equation (PBE) links the evolution with time of granule-size and tracer-mass distributions to underlying rate processes. A new analytical PBE was developed for the tracer distribution and novel numerical techniques, including a new discretized population balance equation for breakage or grinding. Also developed is a general differential technique for extracting rate constants from measurements of particle-size distributions. Granulation in a high-shear mixer proceeds after nucleation, not studied here, with very high initial breakage rates but a relatively unchanging aggregation rate constant. The breakage function is bimodal on a mass basis and the selection rate decays exponentially, over about 20 s. A heterogeneous strength hypothesis was used to account for this time dependence. Aggregation rates are the highest for interactions between small and large granules and may be quantitatively given by, the Equipartition of kinetic energy kernel developed from the theory of collisions between gas molecules. The model can describe granule-size and tracer-mass distributions simultaneously, with great accuracy. The need to replace time as a driving force variable in the kinetics for these systems is identified.
引用
收藏
页码:1984 / 1999
页数:16
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