Design parameters estimations for bubble column reactors

AIChE Journal

Volumn 28, Issue 3, 1982, Pages 353-379

  Shah, Y T ^a   Kelkar, B G ^a   Godbole, S P ^a   Deckwer, W D ^b  

^a UNIVERSITY OF PITTSBURGH   (United States)

^b UNIVERSITY OF OLDENBURG   (Germany)

Author keywords

[No Author keywords available]

Indexed keywords

GAS-LIQUID;

BUBBLE COLUMN REACTORS;

CHEMICAL EQUIPMENT;

EID: 0020128880     PISSN: 00011541     EISSN: 15475905     Source Type: Journal    
DOI: 10.1002/aic.690280302     Document Type: Review

References (341)

1. Gas Holdup and Volumetric Mass Transfer Coefficient in Bubble Columns
2. Bubble Size, Interfacial Area, and Liquid Phase Mass Transfer Coefficients in Bubble Columns
3. Determination of Mass Transfer Parameters in Gas‐Liquid Reactors Using the Acid Catalyzed Isobutene Hydration
4. Oxygen Mass Transfer in Bubble Columns
5. Oxygen Mass Transfer in Bubble Columns Working at Large Gas and Liquid Flow Rates
6. The Transition to Slug Flow in Bubble Columns
7. The Effect of Solids Wettability on the Characteristics of Three Phase Fluidization
8. Variation of Gas Holdup in Bubble Columns with Physical Properties of Liquids and Operating Parameters of Columns
9. Neuere Entwicklungen bei der Industriellen Katalytischen Hydrierung von Fetten (Fetthärtung)
10. Flow Pattern Characterization in Two Phase Flow by Electrical Conductance Probe
11. Stability of Gas Bubbles Rising in Inviscid Fluids
12. Cyclohexan
13. Gas Holdup in a Bubble Column Containing Organic Liquid Mixtures
14. Effect of Solids Wettability on Expansion of Gas‐Liquid Fluidized Beds
15. The Design of Gas Sparged Devices for Viscous Liquid Systems
16. Longitudinal Mixing in Orifice Plate Gas‐Liquid Reactors
17. The Residence Time Distribution of Solid and Liquid in Multistage Bubble Columns in the Cocurrent Flow of Gas, Liquid and Suspended Solid
18. Cyclohexanol
19. Gas‐Liquid Interfacial Area Determination for a Turbine Agitated Reactor
20. Influence of Column Diameter and High Gas Throughputs on the Operation of a Bubble Column
21. Mass Transfer in Bubble Columns Operating at High Gas Throughputs
22. Modelling of a Slurry Reaction. Hydrogeneration of Glucose on Raney Nickel
23. Mass Transfer in Sparged Contactor: Part I. Physical Mechanisms and Controlling Parameters
24. Effects of Transpiration and Changing Diameter on Heat and Mass Transfer to Spheres
25. Theoretische Grundlagen der Butan‐Oxydation
26. Luftoxydation von n‐Butan zu Essigsäure und Lösungmitteln
27. Bubble Swarm Behavior and Gas Absorption in Non‐Newtonian Fluids in Sparged Columns
28. Messtechniken zur Bestimmung der Eigenschaften von Blasen in Blasensäulen
29. Bubble Column Bioreactors‐I. Methods for Measuring the Bubble Size
30. Methods for Measuring the Bubble Size in Bubble Column Bioreactors II
31. A Comprehensive Study on the Cultivation of Yeast in a Tower Bioreactor
32. Techniques for Determining the Properties of Bubbles in Bubble Columns
33. Bubble Size Distribution and Interfacial Areas of Electrolyte Solutions in Bubble Columns
34. Der Einfluβ der Betriebsbedingungen und die Wirkung von Elektrolytzusätzen auf den Sauerstoffübergang in Blasensäulen
35. The Measurement of Bubble Parameters in Two Phase Dispersion‐I. The Development of an Approved Probe Technique
36. Der Wärmeübergang an Heiz‐und Kühlflächen in begasten Flüssigkeiten
37. Gas Absorption from Bubbles
38. The Continuous Phase Heat and Mass Transfer Properties of Dispersions
39. The Prediction of Distillation Plate Efficiencies from Froth Properties
40. Some Properties of Packed Bubble Column
41. Three Phase Slurry Reactors
42. Messung der Phasengrenzfläche in einer Siebbodenkolonne
43. The Absorption of Carbon Dioxide into Solution of Alkalines and Amines (with some notes on hydrogen sulfide and carbonyl sulfide)
44. Gas and Liquid Holdup in Three Phase Fluidization
45. The Behavior of a Continuity Bubbling Fluidized Bed
46. The Influence of Surfactants on the Creeping Motion of Bubbles
47. Oxidation of Glucose to Gluconate
48. Absorption and Reaction of Isobutene in Sulfuric Acid‐II. Consideration on the Scale‐up of Bubble Columns
49. On the Mechanism of Heat Transfer in Bubble Column Reactors
50. Mixing and Mass Transfer in Tall Bubble Columns
51. Absorption and Reaction of Isobutene in Sulfurized Acid‐II. Determination of Parameters and Optimal Conditions in Bubble Columns
52. 2‐Interphase Mass Transfer in Vertical Cocurrent and Countercurrent Gas Flow
53. Effectiveness of Mass Transfer with Chemical Reaction in the Homogeneous and Heterogeneous Regime of Vertical Gas‐Liquid Flow
54. Hydrodynamic Properties of the Fischer‐Tropsch Slurry Process
55. Exclusion of Gas Sparger Influence on Mass Transfer in Bubble Columns
56. On the Relevance of Mass Transfer Limitation in the Fischer‐Tropsch Slurry Process
57. Simultaneous Measurement of Interfacial Area and Mass Transfer Coefficient in Three Phase Fluidized Beds
58. Eine Blasensäule mit Gleichstrom von Wasser und Luft I‐Mischungsvorgänge in der Gasphase
59. High Purity Cyclohexane
60. Designing Gas‐Sparged Reactors
61. Mass Transfer Coefficient and Pressure Drop Data of Two‐Phase Oxygen‐Water Flow in Bubble Column Packed with Static Mixers
62. Solid Concentration Profile in the Bubble Column Slurry Reactor
63. Axial Dispersion in Bubble Columns
64. Process Cuts Methanation Cost
65. Comprehensive Study of the Gas Holdup and Bubble Size Distribution in Highly Viscous Liquids‐I. Glycerol Solutions
66. Comprehensive Study of the Gas Holdup and Bubble Size Distribution in Highly Viscous Liquid‐II. CMC Solutions
67. Holdup and Liquid Circulation in Bubble Columns
68. Mean Gas Holdup in Down‐flow Bubble Columns
69. Mass and Heat Transfer to Single Spheres and Cylinders at Low Reynolds Numbers
70. A Note on Transport to Spheres in Stokes Flow
71. Flow and Oxygen Transfer in Cocurrent Gas‐Liquid Downflow
72. Absorption of Isobutylene in Aqueous Solutions of Sulfuric Acid
73. Alkylation of Phenols with Isobutylene
74. Die spezifische Phasengrenzfläche in Blasenschichten
75. Der relative Gasgehalt von Blasenschichten
76. Der flüssigkeitsseitige Stoffübergangskoeffizient in Blasenschichten
77. On the Dynamics of Bubble Column Slurry Reactors
78. Two Phase Slug Flow
79. Markt‐und Verfahrensübersicht für Phthalsäureanhydrid (PSA)
80. Blasensäulen‐Reaktoren mit suspendiertem Feststoff: Grundlagen—Auslegung—Anwendung
81. Blasengröβen‐Häufigkeits‐Verteilungen und Phasengrenzflächen in Blasensäulen
82. Hydrodynamische Eigenschaften von Blasensäulen: Blasengröβen‐Häufigkeitsverteilungen in mit Stickstoff begasten Gemischen von n‐Butanol und n‐Butanal
83. Mass Transfer to Particles: Part II. Suspended in a Pipeline
84. Heat Transfer in Bubble Agitated Systems—A General Correlation
85. Effect of Mass Transfer on the Selectivity in the Hydrogenation of Fatty Oils
86. Kinetics of Liquid Phase Oxidation of Cumene in Bubble Column
87. A Theoretical Study of the Kinetics of Chlorine Substitution Reaction in Gas‐Liquid Contactors
88. Absorption of Oxygen in Counter‐Current Multistage Bubble Columns—II, Viscoelastic Liquids. Comparison of Systems with High Viscosity
89. Begasen Höherviskoser Flüssigkeiten
90. Untersuchungen an einem Blasensäulen‐Abstromreaktor
91. Relativer Gasgehalt in Blasensäulen‐Abstromreaktoren
92. Liquid Phase Mixing in Bubble Columns. Effect of Liquid Properties
93. Gas Holdup in Bubble Column
94. The Volumetric Liquid‐Phase Mass Transfer Coefficient in Bubble Columns
95. Radial Nonuniformity of Velocity and Voidage in a Bubble Column
96. The Operation of a Bubble Column at High Throughputs I. Gas Holdup Measurements
97. The Rising Velocity of a Large Bubble in a Bubble Swarm
98. The Large Scale Pressure Cycle Fermenter Configuration
99. Rhodium Complex Catalyzed Methanol Carbonylation
100. Die Butan‐Oxydation zur Herstellung von Aliphatischen Säuren und Lösungsmitteln
101. Geschwindigkeitsbestimmende Faktoren bei Reaktionen mit Suspendiertem Kontakt
102. Oxygen Transfer to Mixed Cultures in Tower Systems
103. Holdup and Mass Transfer in Bubble Columns
104. The Behavior of Suspended Solid Particles in the Bubble Column
105. Stochastic Approach to the Hydrodynamics of Gas‐Liquid Dispersions
106. The Rheological Properties of Suspensions of Rigid Particles
107. Kinetics of Absorption of Oxygen in Aqueous Solutions of Cuprous Chloride
108. Absorption of Oxygen in Aqueous Alkaline Solutions of Sodium Dithionite
109. Axial Mixing in Multiphase Contractors—A Unified Correlation
110. Mass Transfer Characteristics of Horizontal Sparged Contractors
111. A Circulation Cell Model for Bubble Columns
112. Heat Transfer in Multiphase Contactors
113. 2 in a Suspension of Lime
114. Oxidation of Toluene and Other Alkylated Aromatic Hydrocarbons to Benzoic Acid and Phenols
115. Determination of the Value of the Specific Surface Area of Phase Contact for an Industrial Absorber with Built‐in Colling Units for Use in Soda Production
116. Liquid‐Solid Transfer in Bubble Column
117. Results of the Second Large‐Scale Test of the Verga Process
118. Untersuchungen zum Wärmeübergang in Blasensäulen
119. The Relation Between Interfacial Area and the Rate of Energy Dissipation in Bubble Column
120. The Volume Mass Transfer Coefficient in a Bubble Bed Column
121. Mass Transfer in Bubble Type Reactors Without Mechanical Mixing
122. Mass Transfer in Large Bubble Column
123. Bubble Column Reactorfor Mass Propagation of Animal Cells in Suspension Culture
124. Longitudinal Dispersion Coefficient of a Liquid in a Bubble Column
125. The Behavior of Suspendend Solid Particles and Liquid in Bubble Columns
126. The Behavior of Suspended Particles and Liquid in Bubble Columns
127. Gas Holdup and Overall Volumetric Absorption Coefficient in Bubble Columns with Suspended Solid Particles: Absorption Rate of Oxygen by an Aqueous Solution of Sodium Sulfite
128. Liquid Holdup and Heat Transfer Coefficient Between Bed and Wall in Liquid‐Solid and Gas‐Liquid‐Solid Fluidized Beds
129. Flow Pattern and Gas Holdup Conditions in Gas‐Sparged Contactors
130. Holdup and Axial Mixing Characteristics of Two Phase and Three Phase Fluidized Beds
131. Phase Holdup Characteristics of Three Phase Fluidized Beds
132. Distribution of Local Void Fraction of Air‐Water Two Phase Flow in a Vertical Channel
133. Behavior of Bubbles in Large Scale Bubble Columns
134. Synthese von Kohlenwasserstoffen und sauerstoffhaltigen Verbindungen aus Wasser and Kohlenoxyd
135. Groβtechnische Versuche zur Fischer‐Tropsch Synthese im flüssigen Medium
136. Neue Entwicklungen zur Kohlenwasserstoff‐Synthese
137. Wärmeübergang an Blasensäulen‐II. Messungen an viscosen Suspensionen
138. Warmeübergang an Blasensäulen‐III. Messungen an gasdurchströmten Suspensionen
139. Gröβenverteilung der Gasblasen in Blasensäulen
140. Dynamische Messung des Relativen Gasgehaltes in Blasensäulen mittels Absorption von Rontgenstrahlen
141. The Fischer‐Tropsch Synthesis in the Liquid Phase
142. Continuous Oxidation of Butyraldehyde to Butyricanhydride by Air in Bubble Column
143. Vinylacetat auf Basis Äthylen in der Flüssigphase mit Palladiumsalz‐Katalysatoren
144. Size Reduction of Bubbles by Orifice Mixers
145. Dispersion of Solid Particles in a Multistage Three Phase Fluidized Bed
146. Bubble Swarm Characteristics in Bubble Columns
147. On Interfacial Area in Aerated Vessels Fitted with a Flat‐Blade Turbine
148. Mechanics of Vertical Moving Fluidized Systems
149. Der Bio‐Hochreaktor—eine Biologische Abwasserreinigungsanlage in Hochbauweise
150. Adipinsaure
151. Application of Kolmogoroff's Theory to Particle‐Liquid Mass Transfer in Agitated Vessels
152. Oxygen Transfer and Mixing in a Tower Cycling Fermentor
153. Ideal Bubbly Flow and Actual Flow in Bubble Columns
154. Oxygen Transfer and Axial Dispersion in an Aeration Tower Containing Static Mixers
155. Axial Mixing of Liquid in Packed Bubble Columns and Perforated Plate Columns of Large Diameter
156. Untersuchungen zur Gasphasendispersion in Blasensäulenreaktoren
157. Interpretation of Mass Transfer Measurements in Bubble Columns Considering Dispersion of Both Phases
158. Rising Velocity of a Swarm of Spherical Bubbles
159. Wärmeübergang an gasdurchströmten Suspensionen
160. Bubble Columns
161. Mass Transfer in Bubble and Packed Bubble Columns
162. Longitudinal Dispersion in Circulation Dominated Bubble Columns
163. Zum Wärmeübergang in Blasensäulen
164. Design and Scale‐up of Bubble and Spray Columns
165. Gas Holdup and Pressure Drop in Bubble Column Reactor
166. Flow of Fluids in Gas‐Liquid Columns
167. Microbial Reactor Design of Synthetic Protein Production
168. Der Wärmeübergang an viscosen Suspensionen in Blasensäulen
169. Stoffaustauschfläche und Energiedissipationsdichte als Auswahlkriterien für Gas/Flüssigkeits‐Reaktoren—Teil I: Die Stoffaustauschfläche in Verschiedenen Gas/Flüssigkeits‐Reaktoren als Funktion der Betriebsparameter
170. Stoffaustauschfläche und Energiedissipationsdichte als Auswahlkriterien für Gas/Flüssikeits‐Reacktoren—Teil II: Korrelation der Stoffaustauschfläche als Funktion der Energiedissipationsdichte mit Hilfe einer Modellvorstellung
171. Die Stoffaustauschfläche in Gas/Flüssigkeitskontaktapparaten—Auswahlkriterien und Unterlagen zur Vergröβerung
172. Untersuchungen zum Dispergieren im turbulenten Scherfeld
173. Kriterien für die auswahl und die Auslegung von Gas/Flüssigkeits‐Reaktoren
174. Design of Gas/Liquid Reactors: Mass Transfer Area and Input of Energy
175. Gas Absorption by Newtonian and Non‐Newtonian Liquids in a Bubble Column
176. Suspension of Solids by Bubble Agitation
177. Two Phase Bubble Flow
178. Heat Transfer in Aerated Tower Filled with Non‐Newtonian Liquid
179. Influence of Gas Distributor Type and Composition of Liquid on the Behavior of a Bubble Column Bioreactor
180. Make Aldehydes by New Oxo Process
181. Oxygen Transfer Rates and Efficiencies in One‐ and Two‐Stage Airlift Towers
182. Vertical Two Phase Flow—Part I. Flow Pattern Correlations
183. Gas‐Liquid‐Particle Operations in Chemical Reaction Engineering
184. The Effect of Particle Size and Bed Height on the Expansion of Mixed Phase (Gas‐Liquid) Fluidized Beds
185. Naβoxidation—Ein Beitrag zum Stand der Technik
186. Photoelektrische Meβmethode zur Bestimmung der Gröβenverteilung Mitteldisperser Tropfen in einem Nicht Mischbaren Flüssigen Zweistoff‐System
187. Determination of Fluid Dynamic Parameters in Bubble Column Design
188. Naβoxidation von Abwasserschlamm—Teil I: Oxidation von Glucose als Modellsubstanz
189. Wet‐Air Oxidation of Sewage Sludge—Part II: The Oxidation of Real Sludges
190. Gasgehalt und Phasengrenzfläche in Begasten Kohlenwasserstoffen
191. A Further Note on Mass Transfer Limitations in the Fischer‐Tropsch Slurry Process
192. Evaporation from Drops
193. Chlorkohlenwasserstoffe, Aromatische, Kernchlorierte
194. Chlorkohlenwasserstoffe, Aliphatische
195. Fortschritte auf dem Gebiet der Olefinpolymerisation mit Ziegler‐Katalysatoren
196. Gas Holdup and Axial Mixing in the Fluid Phase of Bubble Columns
197. Sedimentation and Fluidization: Part I
198. A Physical Model for Axial Mixing of the Liquid Phase for Heterogeneous Flow Regime in Bubble Columns
199. Ein Beitrag zur Hydrodynamik Ablaufbarer Siebböden
200. Removal of Dilute Sulfur Dioxide by Aqueous Slurries of Magnesium Hydroxide Particles
201. Liquid‐Solid Mass Transfer in Aerated Suspension
202. Mass Transfer Coefficients for Suspended Particles in Agitated Vessels and Bubble Columns
203. Liquid‐Phase Oxidation Hydrocarbons to Petrochemicals
204. Analysis of Chemical Methods for Determination of Interfacial Areas in Gas‐in‐Liquid Dispersions with Nonuniform Bubble Sizes
205. Vergleich der fotografischen und der Sulfit‐oxidation‐Methode zur Phasengrenzflächen‐Bestimmung in Blasensäulen
206. Effective Use of Bubble Column Reactors
207. Application of Tower Bioreactors in Cell Mass Production
208. Liquid Mixing in Multistage Bubble Columns
209. Turbulence Structure of Air‐Water Flow—I. Measuring Techniques
210. Kinetics of Catalytic Liquefaction of Big Horn Coal in Segmented Bed Reactor
211. Backmixing in Gas‐Liquid Reactors
212. Scale Up Aspects of Fluid‐Fluid Reaction
213. Absorption with Reaction in Bubble columns
214. Chemical Methods of Measuring Interfacial Area and Mass Transfer Coefficients in Two Fluid Systems
215. Determination and Mathematical Correlation of Heat Transfer Coefficients Under Conditions of Bubble Flow, Cellular and Turbulent Foam
216. Make Methanol by Three Phase Reaction
217. Dynamic Oxygen Mass Transfer CoefficientMeasurement Method for Column‐Reactors
218. Umbersuchungen zur Verbesserung des Stoffaustauchs in Fermentern
219. Erfahrungen mit groβtechnisch eingesetzten Bioreaktoren
220. Technologische und Wirtschaftliche Aspekte der Einzeller‐Proteingewinnung
221. A Dynamic Oxygen Transfer Coefficient Measurement Method for Column Reactors
222. Katalytische Umsetzungen von Olefinen an Platinmetall‐Verbindungen
223. Olefinoxydation mit Palladiumchlorid‐Katalysatoren
224. Tower Bioreactors
225. New Systems and Methods for the Measurement of Effective Interfacial Area and Mass Transfer Coefficients in Gas‐Liquid Contactors
226. Dynamic Gas Disengagement: A New Technique for Assessing the Behavior of Bubble Columns
227. Heat Transfer in Stirred and Non‐stirred Gas‐Liquid Reactors
228. Three Phase Fluidization: Water‐Particle‐Air
229. Separation of Oily Water by Bubble Columns
230. Blasengröβenverteilung in techischen Begasung‐sapparaten
231. On Bubble Flow in Liquids and Fluidized Beds
232. Properties of Recirculating Turbulent Two Phase Flow in Gas Bubble Columns
233. Behavior of Gas Bubbles in Bubble Columns
234. Size Reduction of Bubbles by Orifice Mixer
235. Pressure Aeration in a 55‐ft Bubble Column
236. The Distribution of Gas‐Side and Liquid‐Side Resistance in the Absorption of Chlorine into Benzene in a Wetted Wall Column
237. Hydrogenation in a Stirred Gas‐Liquid Reactor
238. Quantitative Evaluation of Interparticle Mass Transport Effects in the Hydrogenation of Fatty Oils
239. Experimental Techniques For Studying Fluid Dynamics of H‐COAL Reactor
240. Hydrodynamics and Mass Transfer in Bubble Columns Operating in the Churn Turbulent Regime
241. Effects of Dispersing Bubbles into Liquid Fluidized Beds on Heat Transfer and Holdup at Constant Bed Expansion
242. Absorption of Oxygen in Countercurrent Multistage Bubble Columns—I. Aqueous Solution with Low Viscosity
243. Absorption of Oxygen in Countercurrent Multistage Bubble Columns—II. Aqeous Solutions with High Viscosity
244. Three Phase Fluidized Bed Reactors: An Application to the Production of Calciu Bisulfite Acid Solutions
245. Die Synthese von Essigsäure aus Methanol und Kohlenoxyd
246. Improved Gas‐Liquid Contacting in Cocurrent Flow
247. Mass Transfer in Bubble Columns Packed with Motionless Mixers
248. Interfacial Area and Bubble Size Distribution in Gas/Liquid Jet Reactor
249. Age Distribution of Suspended Solid Particles in a Bubble Column
250. Sizes and Size Distribution of Bubbles in a Bubble Column‐Comparison between the Two Point Electric Probe Method and the Photographic Method
251. Gas Holdup in Gas‐Liquid and Gas‐Liquid‐Solid Flow Reactors
252. Performance of Gas Bubble Columns: Volumetric Liquid‐Phase Mass Transfer Coefficient and Gas Holdup
253. The Effect of Plates on Some Parameters of a Heterogeneous Bed in Bubble‐Type Flow Reactors
254. Porosity of the Heterogeneous Bed and Liquid Circulation in Multistage Bubble‐Type Column Reactors
255. Gas Holdup in Uniformly Aerated Bubble Column Reactors
256. Eignung von Einlochboden als Gasverteiler in Blasensäulen
257. Sorption Characteristics for Gas‐Liquid Contacting in Mixing Vessels
258. Sorption Characteristics of Slot Injectors and Their Dependence of the Coalescence Behavior of the System
259. Average Volumetric Concentration in Two Phase Systems