1991
DOI: 10.1016/0009-2509(91)80130-q
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Crystallization and precipitation engineering—III. A discrete formulation of the agglomeration rate of crystals in a crystallization process

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Cited by 104 publications
(86 citation statements)
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“…These effects and the universal hydrodynamic functions which describe the disturbance of the ambient fluid velocity by the presence of particles are calculated for particles of unequal size. Because not every collision leads to agglomeration the concept of probability of agglomeration is used in agreement with the concepts of David et al [4], Hounslow et al [5] and Baødyga et al [2,6]. However, in the present paper the probability of agglomeration is related to the fine scale structure of turbulence and expressed using multifractal formalism.…”
Section: Introductionmentioning
confidence: 79%
“…These effects and the universal hydrodynamic functions which describe the disturbance of the ambient fluid velocity by the presence of particles are calculated for particles of unequal size. Because not every collision leads to agglomeration the concept of probability of agglomeration is used in agreement with the concepts of David et al [4], Hounslow et al [5] and Baødyga et al [2,6]. However, in the present paper the probability of agglomeration is related to the fine scale structure of turbulence and expressed using multifractal formalism.…”
Section: Introductionmentioning
confidence: 79%
“…where f (k) is the shape function proposed by David et al [2]. Presented approach requires some discussion.…”
Section: ±3mentioning
confidence: 97%
“…In present investigations the experiments for BaSO 4 precipitation are carried out at high reactant concentrations with the aim to observe agglomeration process. In the theoretical part of this paper agglomeration rate is expressed using adequate collision kernels and expressions for the probability of agglomeration in agreement with the concepts of David et al [2], Hounslow et al [3], and Baødyga et al [4].…”
Section: Introductionmentioning
confidence: 98%
“…England primary and secondary nucleation, chemical-and diffusioncontrolled growth and agglomeration of crystals. David et al (1991a) developed a discrete formulation of the agglomeration rate of adipic acid crystals during crystallization in mechanically stirred crystallizer. The expression relied on fluid mechanics and phenomenological considerations, and accounted for the influence of particle concentration, supersaturation, specific power dissipation, size of crystallizer and size of agglomerating crystals.…”
Section: Introductionmentioning
confidence: 99%