References
- J. M. Matsen, Scale-up of fluidized bed processes: Principle and practice, Powder Technol., 88, 237-244 (1996). https://doi.org/10.1016/S0032-5910(96)03126-9
- M. Perrut and J.-Y. Clavier, Supercritical fluid formulation: Process choice and scale-up, Ind. Eng. Chem. Res., 42, 6375-6383 (2003). https://doi.org/10.1021/ie030144x
- D. Weuster-Botz, D. Hekmat, R. Puskeiler, and E. Franco-Lara, Enabling technologies: fermentation and downstream processing, Adv. Biochem. Eng. Biotechnol., 105, 205-247 (2007).
- L. Z. He and Y. Sun, Purification of lysozyme by multistage affinity filtration. Bioprocess Biosyst. Eng., 25, 155-164 (2002). https://doi.org/10.1007/s00449-002-0288-7
- B. K. Lonsane, G. Saucedo-Castaneda, M. Raimbault, S. Roussos, G. Viniegra-Gonzalez, N. P. Ghildyal, M. Ramakrishna, and M. M. Krishnaiah, Scale-up strategies for solid state fermentation systems, Process Biochem., 27, 259-273 (1992). https://doi.org/10.1016/0032-9592(92)85011-P
- T. Kamiya, M. Kiminoyama, K. Nishi, and R. Misumi, Scale-up factor for mean drop diameter in batch rotor-stator mixers, J. Chem. Eng. Jpn., 43, 326-332 (2010). https://doi.org/10.1252/jcej.09we142
- V. A. Atiemo-Obeng and R. V. Calabrese, Handbook of Industrial Mixing: Science and Practice, John Wiley & Sons, Hoboken, USA, 470-505 (2004).
- J. T. Davies, Drop sizes of emulsions related to turbulent energy dissipation rates, Chem. Eng. Sci., 40, 839-842 (1985). https://doi.org/10.1016/0009-2509(85)85036-3
- J. T. Davies, A physical interpretation of drop sizes in homogenizers and agitated tanks, including the dispersion of viscous oils, Chem. Eng. Sci., 42, 1671-1676 (1987). https://doi.org/10.1016/0009-2509(87)80172-0
- Y. Sumi and M. Kamiwano, Production method for objective size of suspension droplet in different scale of mixing devices, Japanese Patent 066284 (2002).
- Y. F. Maa and C. Hsu, Liquid-liquid emulsification by rotor/stator homogenization, J. Control. Release, 38, 219-228 (1996). https://doi.org/10.1016/0168-3659(95)00123-9
- F. Barailler, M. Heniche, and P. A. Tanguy, CFD analysis of a rotor-stator mixer with viscous fluids, Chem. Eng. Sci., 61, 2888-2894 (2006). https://doi.org/10.1016/j.ces.2005.10.064
- R. V. Calabrese, M. K. Francis, V. P. Mishra, and S. Phongikaroon, Measurement and analysis of drop size in batch rotor-stator mixer, Proceedings of 10th European Conference on Mixing, July 2-5, Delft, Netherlands (2000).
- T. Hielscher, Ultrasonic production of nano-size dispersions and emulsions, Dans European Nano Systems Worshop - ENS 2005, Dec. 14-16, Paris, France (2005).
- I. Sole, C. M. Pey, A. Maestro, C. Gonzalez, M. Porras, C. Solans, and J. M. Gutierrez, Nano-emulsions prepared by the phase inversion composition method: preparation variables and scale up, J. Colloid Interface Sci., 344, 417-423 (2010). https://doi.org/10.1016/j.jcis.2009.11.046
- E. Paul and R. E. Treybal, Mixing and product distribution for a liquid-phase, second-order, competitive-consecutive reaction, AIChE J., 17, 718-724 (1971). https://doi.org/10.1002/aic.690170340
- J. C. Ogbonna, H. Mashima, and H. Tanaka, Scale up of fuel ethanol production from sugar beet juice using loofa sponge immobilized bioreactor, Bioresour. Technol., 76, 1-8 (2001). https://doi.org/10.1016/S0960-8524(00)00084-5
- R. Philippe, P. Serp, P. Kalck, Y. Kihn, S. Bordere, D. Plee, P. Gaillard, D. Bernard, and B. Caussat, Kinetic study of carbon nanotubes synthesis by fluidized bed chemical vapor deposition, AIChE J., 55, 450-464 (2009). https://doi.org/10.1002/aic.11676
- J. B. Romero and L. N. Johanson, Factors affecting fluidized bed quality, Chem. Eng. Prog. Symp. Ser., 58, 28-37 (1962).
- T. M. Knowlton, S. B. R. Karri, and A. Issangya, Scale-up of fluidized-bed hydrodynamics, Powder Technol., 150, 72-77 (2005). https://doi.org/10.1016/j.powtec.2004.11.036
- T. E. Broadhurst and H. A. Becker, Onset of fluidization and slugging in beds of uniform particles, AIChE J., 21, 238-247 (1975). https://doi.org/10.1002/aic.690210204
- L. R. Glicksman, Scaling relationships for fluidized beds, Chem. Eng. Sci., 39, 1373-1379 (1984). https://doi.org/10.1016/0009-2509(84)80070-6
- J. R. Ommen, M. Teuling, J. Nijenhuis, and B. G. M. Wachem, Computational validation of the scaling rules for fluidized beds, Powder Technol., 163, 32-40 (2006). https://doi.org/10.1016/j.powtec.2006.01.010
- C. Sierra, F. Bonniol, R. Occelli, and L. Tadrist, Practical scaling consideration for dense gas fluidized beds interacting with the air-supply system, Chem. Eng. Sci., 64, 3717-3720 (2009). https://doi.org/10.1016/j.ces.2009.04.042
- J. Sanderson and M. Rhodes, Bubbling fluidized bed scaling laws: evaluation at large scales, AIChE J., 51, 2686-2694 (2005). https://doi.org/10.1002/aic.10511
- D. L. Marchisio, L. Rivautell, and A. A. Barresi, Design and scale-up of chemical reactors for nanoparticle precipitation, AIChE J., 52, 1877-1887 (2006). https://doi.org/10.1002/aic.10786
- S. Tissot, M. Farhat, D. L. Hacker, T. Anderlei, M. Kuhner, C. Comninellis, and F. Wurm, Determination of a scale-up factor from mixing time studies in orbitally shaken bioreactors, Biochem. Eng. J., 52, 181-186 (2010). https://doi.org/10.1016/j.bej.2010.08.005
- F. Garcia-Ochoa and E. Gomez, Bioreactor Scale-up and oxygen transfer rate in microbial processes: An overview, Biotechnol. Adv., 27, 153-176 (2009). https://doi.org/10.1016/j.biotechadv.2008.10.006
- R. Gamboa-Suasnavart, L. Marin-Palacio, J. A. Marinez-Sotelo, C. Espitia, L. Servin-Gonzalez, N. A. Valdez-Cruz, and M. A. Trujillo-Roldan, Scale-up from shake flasks to bioreactor, based on power input and Streptomyceslividans morphology, for the production of recombinant APA (45/47 kDa protein) from Mycobacterium tuberculosis, World J. Microbiol. Biotechnol., 29, 1421-1429 (2013). https://doi.org/10.1007/s11274-013-1305-5