论文信息 - Optimization Design for DTB Industrial Crystallizer of Potassium Chloride - 字舞流文

Optimization Design for DTB Industrial Crystallizer of Potassium Chloride

A computational fluid dynamics (CFD) model was developed for the simulation and optimization of an existing continuous DTB crystallizer with KCl productivity of 0.1 million tons per year. The multi...

Ping Li | Xingfu Song | Jianguo Yu | Menghua Zhang | Xingfu Song | Jianguo Yu | Ping Li | Jin Wang | Jin Wang | Meng Zhang

[1] Manabu Kano,et al. Influence of the incomplete dissolution of fines in the fines dissolver on the optimal operation of industrial continuous DTB crystallizers , 2001 .

[2] H. Kramer,et al. Modelling the cyclic behaviour in a DTB crystallizer—a two-population balance model approach , 2005 .

[3] M. Vakili,et al. CFD analysis of turbulence in a baffled stirred tank, a three-compartment model , 2009 .

[4] Allan S. Myerson,et al. CFD simulations for analysis and scale‐up of anti‐solvent crystallization , 2006 .

[5] M. Bravi,et al. The effect of scaling on the performances of a DTB crystallizer by means of a compartmental simulation model , 2005 .

[6] D. Pinelli,et al. Dispersion coefficients and settling velocities of solids in slurry vessels stirred with different types of multiple impellers , 2004 .