Design of Biochemical Reactors Mass Transfer Criteria for Simple and Complex Systems
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[1] T. W. F. Russell,et al. The tubular loop batch fermentor: Basic concepts , 1974 .
[2] G. Batchelor,et al. Pressure fluctuations in isotropic turbulence , 1951, Mathematical Proceedings of the Cambridge Philosophical Society.
[3] W. Deckwer,et al. Mixing and mass transfer in tall bubble columns , 1974 .
[4] C. Tien,et al. Creeping flow of power‐law fluid over newtonian fluid sphere , 1968 .
[5] John Happel,et al. Viscous flow in multiparticle systems: Slow motion of fluids relative to beds of spherical particles , 1958 .
[6] N. Kossen,et al. The growth of molds in the form of pellets–a literature review , 1977 .
[7] L. Kempe,et al. Influence of surface active agents on oxygen absorption to the free interface in a stirred fermentor , 1971 .
[8] L. Fan,et al. Oxygen transfer to mixed cultures in tower systems , 1975 .
[9] M. Alexander,et al. GROWTH CHARACTERISTICS OF FUNGI AND ACTINOMYCETES , 1960, Journal of bacteriology.
[10] L. Fan,et al. Pressure drop, gas hold‐up, and oxygen transfer in tower systems , 1977 .
[11] N. Blakebrough,et al. Mass transfer and mixing rates in fermentation vessels , 1966 .
[12] J. Davidson,et al. The effect of surface active agents on the rate of absorption of carbon dioxide by water , 1956 .
[13] Kazuo Endoh,et al. Power Characteristics of Gas-Liquid Contacting Mixers , 1955 .
[14] F. Yoshida,et al. Performance of gas bubble columns: Volumetric liquid‐phase mass transfer coefficient and gas holdup , 1965 .
[15] M. Moo-young,et al. Generalized expressions for gas absorption rates in bubbles , 1970 .
[16] Charles N. Satterfield,et al. Mass transfer in heterogeneous catalysis , 1969 .
[17] W. Resnick,et al. Mass transfer from gas bubbles in an agitated vessel with and without simultaneous chemical reaction , 1964 .
[18] John Howard Perry,et al. Chemical Engineers' Handbook , 1934 .
[19] G. A. Hughmark,et al. Holdup and Mass Transfer in Bubble Columns , 1967 .
[20] M. L. Wasserman,et al. Upper and lower bounds on the drag coefficient of a sphere in a power‐model fluid , 1964 .
[21] M. J. Johnson. Aerobic Microbial Growth at Low Oxygen Concentrations , 1967, Journal of Bacteriology.
[22] B. Gal-or,et al. Hydrodynamics of an ensemble of drops (or bubbles) in the presence or absence of surfactants , 1968 .
[23] M. Moo-young,et al. The continuous phase heat and mass transfer properties of dispersions , 1961 .
[24] P. Calderbank,et al. Mass transfer coefficients, velocities and shapes of carbon dioxide bubbles in free rise through distilled water , 1964 .
[25] Klaas R. Westerterp,et al. The residence time distribution of the gas in an agitated gas-liquid contactor , 1963 .
[26] J. J. Janssen,et al. The influence of suspended solid material on the gas-liquid mass transfer in stirred gas-liquid contactors , 1977 .
[27] S. Aiba,et al. Comments on oxygen transfer within a mold pellet. , 1971, Biotechnology and bioengineering.
[28] M. Moo-Young,et al. Heat transfer rates to newtonian fluids in aUSn anchor-agitated kettle , 1969 .
[29] M. Moo-Young,et al. Degradation of polysaccharides by endo and exo enzymes: A theoretical analysis , 1975 .
[30] G. Hamer,et al. Turbine impellers as gas‐liquid contacting devices , 1963 .
[31] S. A. Miller,et al. Power requirements of gas‐liquid agitated systems , 1962 .
[32] H. Blanch,et al. Non‐Newtonian fermentation broths: Rheology and mass transfer , 1976, Biotechnology and bioengineering.
[33] L. A. Bromley,et al. COMPUTER ESTIMATION OF HEAT AND FREE ENERGY OF FORMATION FOR SIMPLE INORGANIC COMPOUNDS , 1963 .
[34] Takeshi Kobayashi,et al. Oxygen transfer into mycelial pellets , 1966, Biotechnology and Bioengineering.
[35] S. A. Miller,et al. Performance of Agitated Gas-Liquid Contactors , 1944 .
[36] M. Moo-young,et al. Kinetics of enzymatic hydrolysis of cellulose: Analytical description of a mechanistic model , 1978, Biotechnology and bioengineering.
[37] M. Moo-young. Microbial reactor design for synthetic protein production , 1975 .
[38] M. Moo-young,et al. The rheological effects of substrate-additives on fermentation yields. , 1969, Biotechnology and bioengineering.
[39] S. Pirt. A theory of the mode of growth of fungi in the form of pellets in submerged culture , 1966, Proceedings of the Royal Society of London. Series B. Biological Sciences.
[40] T. W. F. Russell,et al. REACTOR MODEL PARAMETERS , 1969 .
[41] E. Katchalski,et al. A WATER-INSOLUBLE POLYANIONIC DERIVATIVE OF TRYPSIN. II. EFFECT OF THE POLYELECTROLYTE CARRIER ON THE KINETIC BEHAVIOR OF THE BOUND TRYPSIN. , 1964, Biochemistry.
[42] Larry L. Gasner. Development and application of the thin channel rectangular air lift mass transfer reactor to fermentation and waste‐water treatment systems , 1974 .
[43] Harumi. Kobayashi,et al. Kinetic studies of α‐galactosidase‐containing mold pellets on PNPG hydrolysis , 1976 .
[44] A. H. P. Skelland,et al. Non-Newtonian flow and heat transfer , 1967 .
[45] J. R. Fair,et al. Heat Transfer and Gas Holdup in a Sparged Contactor , 1962 .
[46] W. K. Lewis,et al. Principles of Gas Absorption. , 1924 .
[47] M. Moo‐Young,et al. Enzymatic breakdown of water insoluble substrates , 1975 .
[48] Norman Blakebrough,et al. Biochemical and biological engineering science , 1967 .
[49] A. Acharya,et al. Mechanics of bubble motion and deformation in non-newtonian media , 1977 .
[50] M. Moo-young,et al. Effects of polymer additives on fermentation parameters in a culture of A. niger , 1973 .
[51] F. Yoshida,et al. Gas Absorption in Agitated Gas-Liquid Contactors , 1963 .
[52] J. Schultz,et al. Sulfite Oxidation as a Measure of Aeration Effectiveness , 1956 .
[53] R. Foresti,et al. Agitation of Non-Newtonian Liquids. Power Measurements in the Laminar Region , 1959 .
[54] A. B. Metzner. Agitation of non‐Newtonian fluids , 1957 .
[55] V. Linek. Bestimmung der Phasen-Grenzfläche in einem mit mechanischem Rührwerk versehenen Reaktor bei Gasdurchgang , 1966 .
[56] R. E. Treybal. Mass-Transfer Operations , 1955 .
[57] A. B. Metzner,et al. Agitation of viscous Newtonian and non-Newtonian fluids , 1961 .
[58] C. Wilke,et al. Simultaneous measurement of interfacial area and mass transfer coefficients for a well—mixed gas dispersion in aqueous electrolyte solutions , 1974 .
[59] O. C. Sandall,et al. Gas absorption by non‐Newtonian fluids in agitated vessels , 1974 .
[60] J. Y. Oldshue,et al. Fermentation mixing scale‐up techniques , 1966 .
[61] Kiyomi Akita,et al. Gas Holdup and Volumetric Mass Transfer Coefficient in Bubble Columns. Effects of Liquid Properties , 1973 .
[62] V. Mohan,et al. A theoretical study of pressure drop for non‐Newtonian creeping flow past an assemblage of spheres , 1976 .
[63] C. H. Lin,et al. Oxygen transfer and mixing in a tower cycling fermentor , 1976 .
[64] M. Moo-young,et al. Gas Absorption Rates at the Free Surface of a Flowing Water Stream. Effects of a Surfactant and of Surface Baffles , 1973 .
[65] A. Humphrey,et al. Mass Transfer from Individual Gas Bubbles , 1961 .
[66] B. Kristiansen,et al. The Filamentous fungi , 1975 .
[67] S. Friedlander. A note on transport to spheres in stokes flow , 1961 .
[68] H. Blanch,et al. Bubble motion and mass transfer in non‐Newtonian fluids: Part I. Single bubble in power law and Bingham fluids , 1978 .
[69] G. Marrucci,et al. A theory of coalescence , 1969 .
[70] D. Meister,et al. The tubular loop fermentor: Oxygen transfer, growth kinetics and design , 1977, Biotechnology and bioengineering.
[71] Irving Leibson,et al. Rate of flow and mechanics of bubble formation from single submerged orifices. I. Rate of flow studies , 1956 .
[72] M. Moo‐Young,et al. The blending efficiencies of some impellers in batch mixing , 1972 .
[73] V. R. Ranade,et al. Influence of polymer additives on the gas‐liquid mass transfer in stirred tanks , 1978 .
[74] J. M. Marchello,et al. Film-penetration model for mass and heat transfer , 1958 .
[75] Campbell W. Robinson,et al. Stirred‐tank mechanical power requirement and gas holdup in aerated aqueous phases , 1977 .
[76] Manish Sharma,et al. Mass transfer in mechanically agitated gas—liquid contactors , 1971 .
[77] David F. Ollis,et al. Biochemical Engineering Fundamentals , 1976 .
[78] Kenneth B. Bischoff,et al. Effectiveness factors for general reaction rate forms , 1965 .
[79] W. J. McManamey,et al. Mass transfer into simulated fermentation media , 1973 .
[80] E. L. Gaden,et al. A continuous, multistage tower fermentor. I. Design and performance tests , 1969 .
[81] Donald Nelson Miller,et al. Scale‐up of agitated vessels gas‐liquid mass transfer , 1974 .
[82] M. Moo-Young,et al. Bubble drag and mass transfer in non‐newtonian fluids: Creeping flow with power‐law fluids , 1969 .
[83] E. W. Thiele. Relation between Catalytic Activity and Size of Particle , 1939 .
[84] H. Taguchi,et al. Power requirement in non‐newtonian fermentation broth , 1966 .
[85] Y. Tomita. On the Fundamental Formula of Non-Newtonian Flow , 1959 .
[86] P. V. Danckwerts. Significance of Liquid-Film Coefficients in Gas Absorption , 1951 .
[87] Takeshi Kobayashi,et al. Backmixing and mass transfer in the design of immobilized‐enzyme reactors , 1971 .
[88] C. Wilke,et al. Oxygen absorption in stirred tanks: A correlation for ionic strength effects , 1973 .
[89] J. Lloyd,et al. Natural Convection Adjacent to Horizontal Surface of Various Planforms , 1974 .
[90] Kiyomi Akita,et al. Bubble Size, Interfacial Area, and Liquid-Phase Mass Transfer Coefficient in Bubble Columns , 1974 .
[91] P. Calderbank,et al. Mass transfer in the continuous phase around axisymmetric bodies of revolution , 1964 .
[92] L. Erickson,et al. Growth models of cultures with two liquid phases. V. Substrate dissolved in dispersed phase—experimental observations , 1971, Biotechnology and bioengineering.
[93] S. Sideman,et al. MASS TRANSFER IN GAS-LIQUID CONTACTING SYSTEMS , 1966 .
[94] T. W. F. Russell. Secondary sewage treatment in pipeline contactors , 1972 .
[95] J. Happel,et al. Low Reynolds number hydrodynamics , 1965 .
[96] Richards Jw. Studies in aeration and agitation. , 1961 .
[97] Fumitake Yoshida,et al. Gas Absorption by Newtonian and Non-Newtonian Fluids in Sparged Agitated Vessels , 1975 .
[98] T. W. F. Russell,et al. The design of gas sparged devices for viscous liquid systems , 1978 .
[99] Campbell W. Robinson,et al. Mass-transfer-effective bubble coalescence frequency and specific interfacial area in a mechanically agitated gas-liquid contactor , 1980 .
[100] M. Moo-Young,et al. Effectiveness factors for immobilized‐enzyme reactions , 1972 .
[101] R. Dale,et al. Polarographic measurement of dissolved oxygen in yeast fermentations. , 1959, Applied microbiology.
[102] H. Taguchi. The nature of fermentation fluids , 1971 .
[103] M. Moo-young,et al. Mass transfer from a single bubble in turbulent counter‐current liquid flow , 1973 .
[104] F. Yoshida,et al. Oxygen Absorption Rates in Stirred Gas-Liquid Contactors Condensed—complete copy for sale , 1960 .
[105] S. Narayanan,et al. Coalescence of two bubbles rising in line at low reynolds numbers , 1974 .
[106] Takeshi Kobayashi,et al. The kinetic and mass transfer behavior of immobilized invertase on ion‐exchange resin beads , 1973 .