| Acknowledgement | 
    v | 
  
  
    | Abstract | 
    vii | 
  
  
    | 
	 1  | 
      Introduction
      403kb | 
    1 | 
  
  
    |   | 
    
	 1.1  | 
     Motivation for the Thesis | 
    1 | 
  
  
    |   | 
    1.1.1 | 
     Importance of bubble column reactors | 
    1 | 
  
  
    | 1.1.2 | 
     The importance of reactor modeling | 
    6 | 
  
  
    | 1.1.3 | 
     The need for determining model parameters | 
    7 | 
  
  
    | 
	 1.2  | 
     Problem Formulation | 
    9 | 
  
  
    |   | 
    1.2.1 | 
     Overview | 
    9 | 
  
  
    | 1.2.2 | 
     Coalescence and breakup rates | 
    10 | 
  
  
    | 1.2.3 | 
     Liquid circulation | 
    12 | 
  
  
    | 1.2.4 | 
     Dynamic gas disengagement | 
    13 | 
  
  
    | 
	 2  | 
      Experimental
      479kb | 
    15 | 
  
  
    |   | 
    
	 2.1  | 
     Experimental Apparatus | 
    15 | 
  
  
    | 
	 2.2  | 
     Measurement Principle | 
    17 | 
  
  
    |   | 
    
	 2.2.1  | 
     The five-point probe of Burgess and Calderbank | 
    17 | 
  
  
    | 
	 2.2.2  | 
     The five-point probe of Steinemann and Buchholz | 
    19 | 
  
  
    | 
	 2.3  | 
     Estimation of the Bubble Parameters | 
    20 | 
  
  
    |   | 
    
	 2.3.1  | 
     Technique of Burgess and Calderbank | 
    20 | 
  
  
    | 
	 2.3.2  | 
     Technique of Steinemann and Buchholz | 
    22 | 
  
  
    | 
	 2.4  | 
     Experimental Results | 
    23 | 
  
  
    | 
	 2.5  | 
     Conclusion  | 
    31 | 
  
  
    | 
	 3  | 
      Coalescence and Breakup
      962kb | 
    33 | 
  
  
    |   | 
    
	 3.1  | 
     Introduction | 
    33 | 
  
  
    | 
	 3.2  | 
     Binary Bubble Coalescence | 
    37 | 
  
  
    |   | 
    
	 3.2.1  | 
     Binary bubble collision frequency | 
    38 | 
  
  
    | 
	 3.2.2  | 
     Coalescence efficiency | 
    40 | 
  
  
    | 
	 3.3  | 
     Model for Bubble Breakup | 
    43 | 
  
  
    |   | 
    
	 3.3.1  | 
     Arrival or bombarding frequency of eddies | 
    44 | 
  
  
    | 
	 3.3.2  | 
     Breakage probability (efficiency) | 
    46 | 
  
  
    | 
	 3.3.3  | 
     The expression for breakage rate | 
    49 | 
  
  
    | 
	 3.3.4  | 
     Breakage kernel or breakage size distribution | 
    50 | 
  
  
    | 
	 3.4  | 
     Results and Discussion | 
    52 | 
  
  
    |   | 
    
	 3.4.1  | 
     Coalescence efficiency | 
    52 | 
  
  
    | 
	 3.4.2  | 
     Specific coalescence rate | 
    54 | 
  
  
    | 
	 3.4.3  | 
     Breakage kernel | 
    58 | 
  
  
    | 
	 3.4.4  | 
     Specific breakage rate | 
    61 | 
  
  
    | 
	 3.5  | 
     Conclusion | 
    62 | 
  
  
    | 
	 4  | 
      Approach of Two Fluid Particles
      824kb | 
    65 | 
  
  
    |   | 
    
	 4.1  | 
     Introduction | 
    66 | 
  
  
    | 
	 4.2  | 
     Simple Parallel-Film Model | 
    67 | 
  
  
    |   | 
    
	 4.2.1  | 
     Expression of film area | 
    67 | 
  
  
    | 
	 4.2.2  | 
     Expression for interaction time | 
    72 | 
  
  
    | 
	 4.2.3  | 
     Virtual mass coefficient | 
    73 | 
  
  
    | 
	 4.3  | 
     General Parallel-Film Model | 
    75 | 
  
  
    | 
	 4.4  | 
     Results and Discussion | 
    80 | 
  
  
    |   | 
    
	 4.4.1  | 
     Zero external force | 
    80 | 
  
  
    | 
	 4.4.2  | 
     Effect of external forces | 
    85 | 
  
  
    | 
	 4.4.3  | 
     Effect of virtual mass | 
    87 | 
  
  
    | 
	 4.4.4  | 
     Comparison with experimental data | 
    88 | 
  
  
    | 
	 4.5  | 
     Conclusion | 
    92 | 
  
  
    | 
	 5  | 
      Local Bubble Size Distribution
      521kb | 
    95 | 
  
  
    |   | 
    
	 5.1  | 
     Introduction | 
    95 | 
  
  
    | 
	 5.2  | 
     Population Balance Model | 
    97 | 
  
  
    |    | 
    5.2.1 | 
     Equations of balance  | 
    97 | 
  
  
    | 5.2.2 | 
     Viscous and buoyancy coalescence  | 
    101 | 
  
  
    | 5.2.3 | 
     Energy dissipation rate | 
    103 | 
  
  
    | 5.2.4 | 
     Boundary conditions | 
    104 | 
  
  
    | 
	 5.3  | 
     Results and Discussion | 
    105 | 
  
  
    | 
	 5.4  | 
     Conclusion | 
    110 | 
  
  
    | 
	 6  | 
      Liquid Circulation
      1157kb | 
    113 | 
  
  
    |   | 
    
	 6.1  | 
     Introduction | 
    113 | 
  
  
    | 
	 6.2  | 
     Pseudo-Homogeneous Fluid Model  | 
    117 | 
  
  
    |    | 
    
	 6.2.1  | 
     Equation of motion  | 
    124 | 
  
  
    | 
	 6.2.2  | 
     Expression of liquid velocity  | 
    121 | 
  
  
    | 
	 6.3  | 
     Two-Fluid Model | 
    124 | 
  
  
    |   | 
    
	 6.3.1  | 
     Equation of motion | 
    124 | 
  
  
    | 
	 6.3.2  | 
     Expression of liquid velocity | 
    127 | 
  
  
    | 
	 6.4  | 
     Results and Discussion | 
    129 | 
  
  
    |   | 
    6.4.1 | 
     Pseudo-homogeneous model | 
    129 | 
  
  
    | 6.4.2 | 
     Two-fluid model | 
    138 | 
  
  
    | 
	 6.5  | 
     Conclusion | 
    144 | 
  
  
    | 
	 7  | 
      Dynamic Gas Disengagement
      1078kb | 
    147 | 
  
  
    |   | 
    
	 7.1  | 
     Introduction | 
    147 | 
  
  
    | 
	 7.2  | 
     Experimental Technique and Data Treatment | 
    151 | 
  
  
    | 
	 7.3  | 
     Holdup Structure and Rise Velocities | 
    154 | 
  
  
    | 
	 7.4  | 
     Non-Uniform Distribution | 
    159 | 
  
  
    | 
	 7.5  | 
     Bubble Size and Specific Interfacial Area | 
    160 | 
  
  
    | 
	 7.6  | 
     Results and Discussion | 
    162 | 
  
  
    |   | 
    
	 7.6.1  | 
     Bubble size and interfacial area | 
    162 | 
  
  
    | 
	 7.6.2  | 
     Non-uniform distribution | 
    169 | 
  
  
    | 
	 7.7  | 
     Conclusion | 
    171 | 
  
  
    | 
	 8  | 
    Conclusions and Recommendations
      422kb | 
    173 | 
  
  
     | 
    
	 8.1  | 
     Conclusions | 
    173 | 
  
  
    | 
	 8.2  | 
     Recommendations | 
    175 | 
  
  
    | Nomenclature | 
    177 | 
  
  
    | Bibliography
      380kb | 
    185 |