Mass transfer and hydrodynamic characteristics of unbaffled stirred bio-reactors: Influence of impeller design
Tài liệu tham khảo
Mazzarotta, 1993, Communication phenomena in stirred sugar suspensions, AIChE Symp. Ser., 89, 112
Hekmat, 2007, Crystallization of lysozyme: from vapor diffusion experiments to batch crystallization in agitated ml-scale vessels, Process Biochem., 42, 1649, 10.1016/j.procbio.2007.10.001
Rousseaux, 2001, Mixing and micromixing times in the forced vortex region of unbaffled mixing devices, Can. J. Chem. Eng., 79, 697, 10.1002/cjce.5450790501
Assirelli, 2008, Macro- and micromixing studies in an unbaffled vessel agitated by a Rushton turbine, Chem. Eng. Sci., 63, 35, 10.1016/j.ces.2007.07.074
Lamberto, 1996, Using time dependent RPM to enhance mixing in stirred vessels, Chem. Eng. Sci., 51, 733, 10.1016/0009-2509(95)00203-0
Grisafi, 1994, Solid–liquid mass transfer coefficient in mixing tanks: influence of side wall roughness, IChemE Symp. Ser., 136, 571
Yoshida, 2008, Movement of solid particles on and off bottom of an unbaffled vessel agitated by unsteadily forward-reverse rotating impeller, J. Fluid Sci. Technol., 3, 282, 10.1299/jfst.3.282
Brucato, 2010, Particle suspension in top-covered unbaffled tanks, Chem. Eng. Sci., 65, 3001, 10.1016/j.ces.2010.01.026
Wang, 2012, Energy efficient solids suspension in an agitated vessel-water slurry, Chem. Eng. Sci., 74, 233, 10.1016/j.ces.2012.02.035
Chisti, 2000, Animal-cell damage in sparged bioreactors, Tibtech Rev., 18, 420, 10.1016/S0167-7799(00)01474-8
Barrett, 2010, Microwell engineering characterization for mammalian cell culture process development, Biotechnol. Bioeng., 105, 260, 10.1002/bit.22531
Nienow, 1996, Homogenisation and oxygen transfer rates in large agitated and sparged animal cell bioreactors: some applications for growth and production, Cytotecnology, 22, 87, 10.1007/BF00353927
Scargiali, 2012, Oxygen transfer performance of unbaffled stirred vessels in view of their use as biochemical reactors for animal cell growth, Chem. Eng. Trans., 27, 205
Doig, 2005, Modelling surface aeration rates in shaken microtitre plates using dimensionless groups, Chem. Eng. Sci., 60, 2741, 10.1016/j.ces.2004.12.025
Conway, 2002, Gas–liquid–solid operation of a vortex-ingesting stirred tank reactor, Chem. Eng. Res. Des., 80, 839, 10.1205/026387602321143372
Scargiali, 2007, Mass transfer and hydro-dynamic characteristics of a high aspect ratio self-ingesting reactor for gas–liquid operations, Chem. Eng. Sci., 62, 1376, 10.1016/j.ces.2006.11.040
Scargiali, 2012, Gas–liquid–solid operation of a high aspect ratio self-ingesting reactor, Int. J. Chem. React. Eng., 10, A-27
Cabaret, 2008, Gas–liquid mass transfer in unbaffled dual-impeller mixers, Chem. Eng. Sci., 63, 1636, 10.1016/j.ces.2007.11.028
Scargiali, 2010, Simplified dynamic pressure method for kLa measurement in aerated bioreactors, Biochem. Eng. J., 49, 165, 10.1016/j.bej.2009.12.008
Scargiali, 2010, kLa measurement in bioreactors, Chem. Eng. Trans., 20, 229
Linek, 1989, Dynamic pressure method for kLa measurement in large scale bioreactors, Biotech. Bioeng., 33, 1406, 10.1002/bit.260331107
Linek, 1993, Non-ideal pressure step method for kLa measurement, Chem. Eng. Sci., 48, 1593, 10.1016/0009-2509(93)80119-B
Carbajal, 2004, On the applicability of the dynamic pressure step method for kLa determination in stirred Newtonian and non Newtonian fluids, culture media and fermentation broths, Biochem. Eng. J., 18, 185, 10.1016/j.bej.2003.08.008
Moucha, 2012, Mass transfer characteristics of multiple-impeller fermenters for their design and scale-up, Biochem. Eng. J., 69, 17, 10.1016/j.bej.2012.08.007
Busciglio, 2013, Free-surface shape in unbaffled stirred vessels: experimental study via digital image analysis, Chem. Eng. Sci., 104, 868, 10.1016/j.ces.2013.10.019
Nienow, 1985, On the flooding/loading transition and the complete dispersal condition in aerated vessels agitated by a Rushton turbine, 143
1985
Paul, 2004
Scargiali, 2013, Power consumption in uncovered-unbaffled stirred tanks: influence of viscosity and flow regime, Ind. Eng. Chem. Res., 52, 14998, 10.1021/ie402466w
Rushton, 1950, Power characteristics of mixing impellers – part II, Chem. Eng. Prog., 46, 467