- Chemical Engineering Review for PE Examination|Kinetics
417401|1||2| |3||4||5||6||7||8||Symbols and Definitions||Reaction Parameters - Nomenclature||Rate of Reaction|||

417402|1||2| |3||4||5||6||7||8||Symbols and Definitions||Reaction Parameters - Nomenclature||Fractional Conversion|||

417403|1||2| |3||4||5||6||7||8||Symbols and Definitions||Temperature Dependence||Arrhenius Equation|||

417404|1||2| |3||4||5||6||7||8||Symbols and Definitions||Temperature Dependence||Energy of Activation|||

417405|1||2| |3||4||5||6||7||8||Symbols and Definitions||Temperature Dependence||Rate constant at two temperatures|||

417501|1||2| |3||4||5||6||7||8||Symbols and Definitions||Reaction Order||General Rate of Reaction|||

417502|1||2| |3||4||5||6||7||8||Symbols and Definitions||Reaction Order||Overall Order|||

417503|1||2| |3||4||5||6||7||8||Rate Equations in Differential Form for Irreversible Reactio||Zero-Order (A → R)||Conversion functional group||Reaction Rate|

417504|1||2| |3||4||5||6||7||8||Rate Equations in Differential Form for Irreversible Reactio||Zero-Order (A → R)||Conversion functional group||Time for a given conversion|

417505|1||2| |3||4||5||6||7||8||Rate Equations in Differential Form for Irreversible Reactio||First-Order (A → R)||Conversion functional group||Reaction Rate|

417506|1||2| |3||4||5||6||7||8||Rate Equations in Differential Form for Irreversible Reactio||First-Order Reaction (A → R)||Conversion functional group||Time for a given conversion|

417507|1||2| |3||4||5||6||7||8||Rate Equations in Differential Form for Irreversible Reactio||Second-Order Reaction (2A → R)||Bimolecular Reaction||Reaction Rate|

417508|1||2| |3||4||5||6||7||8||Rate Equations in Differential Form for Irreversible Reactio||Second-Order (2A → R)||Bimolecular Reaction||Time for a given conversion|

417509|1||2| |3||4||5||6||7||8||Rate Equations in Differential Form for Irreversible Reactio||Second-Order (A = bB → R)||Reaction Rate||Concentration Form|

417510|1||2| |3||4||5||6||7||8||Chemical Equilibrium from Rate Constants for Reversible Elementary Reactions||Gaseous-Phase Reactions||General Reactions|||

417511|1||2| |3||4||5||6||7||8||Chemical Equilibrium from Rate Constants for Reversible Elementary Reactions||Gaseous-Phase Reactions||General Reactions||Reaction Rate in the Forward Direction|

417512|1||2| |3||4||5||6||7||8||Chemical Equilibrium from Rate Constants for Reversible Elementary Reactions||Gaseous-Phase Reactions||General Reactions||Reaction Rate in the Reverse Direction|

417513|1||2| |3||4||5||6||7||8||Chemical Equilibrium from Rate Constants for Reversible Elementary Reactions||Gaseous-Phase Reactions||Equilibrium Constant||General Reaction|

417601|1||2| |3||4||5||6||7||8||Chemical Equilibrium Constants from Rate Constants for Rever||Liquid-Phase Reactions||General Reaction|||

417602|1||2| |3||4||5||6||7||8||Chemical Equilibrium Constants from Rate Constants for Rever||Liquid-Phase Reactions||Reaction Rate in Forward Direction|||

417603|1||2| |3||4||5||6||7||8||Chemical Equilibrium Constants from Rate Constants for Rever||Liquid-Phase Reactions||Reaction Rate in Reverse Direction|||

417604|1||2| |3||4||5||6||7||8||Chemical Equilibrium Constants from Rate Constants for Rever||Liquid-Phase Reactions||Equilibrium Constant in terms of concentration|||

417605|1||2| |3||4||5||6||7||8||Chemical Equilibrium Constants from Rate Constants for Rever||Liquid-Phase Reactions||Equilibrium Constant in terms of pressure|||

417606|1||2| |3||4||5||6||7||8||Chemical Equilibrium Constants from Rate Constants for Rever||Effect of Temperature on Chemical Equilibrium Constants||Change of the Equilibrium Constant as a function of Heat of Reaction|||

417607|1||2| |3||4||5||6||7||8||Chemical Equilibrium Constants from Rate Constants for Rever||Effect of Temperature on Chemical Equilibrium Constants||Integrated Equation of the Equilibrium Constant|||

417608|1||2| |3||4||5||6||7||8||Chemical Equilibrium Constants from Rate Constants for Rever||Relationship Between Gibbs Free Energy and the Equilibrium Constant||Gibbs Free Energy for a given value of Equilibrium Constant|||

417609|1||2| |3||4||5||6||7||8||Chemical Equilibrium Constants from Rate Constants for Rever||Variation of Reaction Property Changes with Temperature||Equilibrium Constant for a given Gibbs Free Energy|||

417701|1||2| |3||4||5||6||7||8||Chemical Equilibrium Constants for Reversible Elementary Reactions||Verification of Reaction Property Changes with Temperature||Gibbs-Helmholtz equation|||

417702|1||2| |3||4||5||6||7||8||Reactor Equations||Batch Reactor||Constant Volume||Reaction Rate - General Expression|

417703|1||2| |3||4||5||6||7||8||Reactor Conditions||Batch Reactor||Constant Volume||Time for a given conversion - General Expression|

417704|1||2| |3||4||5||6||7||8||Reactor Conditions||Batch Reactor||Variable Volume||Reaction Rate - General Expression|

417705|1||2| |3||4||5||6||7||8||Reactor Conditions||Batch Reactor||Variable Volume||Time required to achieve conversion - General Expression|

417706|1||2| |3||4||5||6||7||8||Reactor Conditions||Batch Reactor||Variable Volume||Concentration as function of conversion|

417707|1||2| |3||4||5||6||7||8||Reactor Conditions||Batch Reactor||Variable Volume||Fractional conversion|

417708|1||2| |3||4||5||6||7||8||Reactor Conditions||Half-Life||Rate of Reaction - nth Order|||

417709|1||2| |3||4||5||6||7||8||Reactor Conditions||Half-Life||First Order Reaction|||

417710|1||2| |3||4||5||6||7||8||Reactor Equations||Half-Life||nth Order Reaction|||

417801|1||2| |3||4||5||6||7||8||Reactor Equations||Flow Reactors, Steady State (Space Time, Space Velocity||Space Velocity|||

417802|1||2| |3||4||5||6||7||8||Reactor Equations||Flow Reactors, Steady State (Space Time, Space Velocity||Plug-Flow Reactor||Residence Time - General Design Equation|

417803|1||2| |3||4||5||6||7||8||Reactor Equations||Flow Reactors, Steady State (Space Time, Space Velocity||Plug-Flow Reactor||Residence Time - Design Equation for a Constant Volume Case|

417804|1||2| |3||4||5||6||7||8||Reactor Equations||Flow Reactors, Steady State (Space Time, Space Velocity||Continuous Stirred Tank Reactor||Design Equation for a Continuous Stirred Tank Reactor (CSTR)|

417805|1||2| |3||4||5||6||7||8||Reactor Equations||Flow Reactors, Steady State (Space Time, Space Velocity||Continuous Stirred Tank Reactor (CSTR)||Residence time for a constant volume CSTR|

417806|1||2| |3||4||5||6||7||8||Reactor Equations||Flow Reactors, Steady State (Space Time, Space Velocity||Continuous Stirred Tank Reactors in Series||Residence time for N reactors|

417807|1||2| |3||4||5||6||7||8||Reactor Equations||Flow Reactors, Steady State (Space Time, Space Velocity||Continuous Stirred Tanks Reactors in Series||Residence time for n Reactors|

417808|1||2| |3||4||5||6||7||8||Reactor Equations||Flow Reactors, Steady State (Space Time, Space Velocity||Continuous Stirred Tanks Reactors in Series||Concentration at the end of nth Reactor|

417901|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||Zero-Order Reactions (A → R, -rA = k)||Constant Volume||Batch Reactor|

417902|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||Zero-Order Reactions (A → R, -rA = k)||Constant Volume||Plug-flow reactor or CSTR|

417903|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||Zero-Order Reactions (A → R, -rA = k)||Variable Volume||Volume at any given conversion XA|

417904|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||Zero-Order Reactions (A → R, -rA = k)||Variable Volume||Batch reactor|

417905|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||Zero-Order Reactions (A → R, -rA = k)||Variable Volume||Plug-flow reactor or CSTR|

417906|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||First-Order Reactions (A → R, -rA = kCA)||Constant Volume||Batch Reactor|

417907|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||First-Order Reactions (A → R, -rA = kCA)||Constant Volume||Plug-flow reactor|

417908|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||First-Order Reactions (A → R, -rA = kCA)||Constant Volume||CSTR|

417909|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||First-Order Reactions (A → R, -rA = kCA)||Variable Volume||Batch Reactor|

418001|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||First-Order Reactions (A → R, -rA = kCA)||Variable Volume||Plug-flow reactor|

418002|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions|||||||

418003|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||Second-Order Reaction (2A → R, -rA = kCA2)||Constant Volume||Batch Reactor|

418004|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||Second-Order Reaction (2A → R, -rA = kCA2)||Constant Volume||Plug-flow reactor|

418005|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||Second-Order Reaction (2A → R, -rA = kCA2)||Constant Volume||CSTR|

418006|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||Second-Order Reaction (2A → R, -rA = kCA2)||Variable Volume||Batch reactor|

418007|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||Second-Order Reaction (2A → R, -rA = kCA2)||Variable Volume||Plug-flow reactor|

418008|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||Second-Order Reaction (2A → R, -rA = kCA2)||Variable Volume||CSTR|

418101|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||Second-Order Reaction (A + bB → R, -rA = kCACB)||Constant Volume||Batch reactor|

418102|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||Second-Order Reaction (A + bB → R, -rA = kCACB)||Constant Volume||Batch reactor|

418103|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||Second-Order Reaction (A + bB → R, -rA = kCACB)||Constant Volume||Plug-flow reactor|

418104|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||Second-Order Reaction (A + bB → R, -rA = kCACB)||Constant Volume||Plug-flow reactor|

418105|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||Second-Order Reaction (A + bB → R, -rA = kCACB)||Constant Volume||CSTR|

418106|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||Second-Order Reaction (A + bB → R, -rA = kCACB)||Constant Volume||CSTR|

418107|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||First-Order Reversible Reactions||Reaction Rate|||

418108|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||First-Order Reversible Reactions||Equilibrium constant, concentration based|||

418109|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||First-Order Reversible Reactions||Concentration ratio|||

418110|1||2| |3||4||5||6||7||8||Integrated Reactor Equations for Irreversible Reactions||First-Order Reversible Reactions||Conversion-time relationship|||

418201|1||2| |3||4||5||6||7||8||Complex Reactions||Reactions of Shifting Order||Reaction Rate|||

418202|1||2| |3||4||5||6||7||8||Complex Reactions||Reactions of Shifting Order||Concentration as a function of time|||

418203|1||2| |3||4||5||6||7||8||Complex Reactions||Plug-Flow Reactions With Recycle||First Order (εA = 0)|||

418204|1||2| |3||4||5||6||7||8||Complex Reactions||Plug-Flow Reactors With Recycle||Second Order (εA = 0)|||

418205|1||2| |3||4||5||6||7||8||Complex Reactions||Plug-Flow Reactors With Recycle||Relationship Between Overall Conversion and Single-Pass Conversion||Equilibrium Conversion in Single-Pass|

418301|1||2| |3||4||5||6||7||8||Yield and Selectivity||Two Irreversible Reactions in Parallel||Reaction Rate|||

418302|1||2| |3||4||5||6||7||8||Yield and Selectivity||Two Irreversible Reactions in Parallel||Reaction Rate|||

418303|1||2| |3||4||5||6||7||8||Yield and Selectivity||Two Irreversible Reactions in Parallel||Reaction Rate|||

418304|1||2| |3||4||5||6||7||8||Yield and Selectivity||Two Irreversible Reactions in Parallel||Instantaneous fractional yield|||

418305|1||2| |3||4||5||6||7||8||Yield and Selectivity||Two Irreversible Reactions in Parallel||Overall fractional yield|||

418306|1||2| |3||4||5||6||7||8||Yield and Selectivity||Two Irreversible Reactions in Parallel||Overall selectivity|||

418307|1||2| |3||4||5||6||7||8||Yield and Selectivity||Two First-Order Irreversible Reactions in Series||Reaction Rate|||

418308|1||2| |3||4||5||6||7||8||Yield and Selectivity||Two First-Order Irreversible Reactions in Series||Reaction Rate|||

418309|1||2| |3||4||5||6||7||8||Yield and Selectivity||Two First-Order Irreversible Reactions in Series||Reaction Rate|||

418310|1||2| |3||4||5||6||7||8||Yield and Selectivity||Two First-Order Irreversible Reactions in Series||Plug-flow reactor||Maximum concentration|

418311|1||2| |3||4||5||6||7||8||Yield and Selectivity||Two First-Order Irreversible Reactions in Series||Plug-flow reactor||Residence time for maximum concentration|

418312|1||2| |3||4||5||6||7||8||Yield and Selectivity||Two First-Order Irreversible Reactions in Series||CSTR||Maximum concentration|

418313|1||2| |3||4||5||6||7||8||Yield and Selectivity||Two First-Order Irreversible Reactions in Series||CSTR||Residence time for maximum concentration|

418401|1||2| |3||4||5||6||7||8||Catalytic and Surface Reactions||Surface Reaction Steps||Unimolecular surface reaction|||

418402|1||2| |3||4||5||6||7||8||Catalytic and Surface Reactions||Surface Reaction Steps||Bimolecular surface reaction|||

418403|1||2| |3||4||5||6||7||8||Catalytic and Surface Reactions||Surface Reaction Steps||Eley-Rideal reaction|||

418404|1||2| |3||4||5||6||7||8||Catalytic and Surface Reactions||Langmuir Adsorption Isotherm (Adsorption without Reaction)||Adsorption of Undissociated Single Species||Rate of adsorption of A|

418405|1||2| |3||4||5||6||7||8||Catalytic and Surface Reactions||Langmuir Adsorption Isotherm (Adsorption without Reaction)||Adsorption of Undissociated Single Species||Rate of desorption of A|

418406|1||2| |3||4||5||6||7||8||Catalytic and Surface Reactions||Langmuir Adsorption Isotherm (Adsorption without Reaction)||Adsorption of Undissociated Single Species||Langmuir adsorption isotherm|

418407|1||2| |3||4||5||6||7||8||Catalytic and Surface Reactions||Langmuir Adsorption Isotherm (Adsorption without Reaction)||Adsorption of Undissociated Single Species||Equilibrium Constant|

418501|1||2| |3||4||5||6||7||8||Caralytic and Surface Reactions||Langmuir Adsorption Isotherm (Adsorption without Reaction)||Adsorption of Disocciated Single Species||Adsorption of a dissociating diatomic molecule|

418502|1||2| |3||4||5||6||7||8||Catalytic and Surface Reactions||Langmuir Adsorption Isotherm (Adsorption without Reaction)||Adsorption of Disocciated Single Species||Adsorption of a dissociating diatomic molecule|

418503|1||2| |3||4||5||6||7||8||Catalytic and Surface Reactions||Langmuir Adsorption Isotherm (Adsorption without Reaction)||Adsorption of Dissociated Single Species||Adsorption of a dissociating diatomic molecule|

418504|1||2| |3||4||5||6||7||8||Catalytic and Surface Reactions||Langmuir Adsorption Isotherm (Adsorption without Reaction)||Adsorption of Dissociated Single Species||Equilibrium Constant|

418505|1||2| |3||4||5||6||7||8||Enzyme Kinetics: Michaelis-Menten||Michaelis-Menten Model||Material balance on total enyme|||

418506|1||2| |3||4||5||6||7||8||Enzyme Kinetics: Michaelis-Menten||Michaelis-Menten Model||Concentration of complex|||

418507|1||2| |3||4||5||6||7||8||Enzyme Kinetics: Michaelis-Menten||Michaelis-Menten Model||Define Michaelis constant|||

418508|1||2| |3||4||5||6||7||8||Enzyme Kinetics: Michaelis-Menten||Michaelis-Menten Model||Rate of production of product P|||

418509|1||2| |3||4||5||6||7||8||Enzyme Kinetics: Michaelis-Menten||Michaelis-Menten Model||Initial Rate|||

418510|1||2| |3||4||5||6||7||8||Enzyme Kinetics: Michaelis-Menten||Michaelis-Menten Model||Limiting Cases||Low CS0|

418511|1||2| |3||4||5||6||7||8||Enzyme Kinetics: Michaelis-Menten||Micaelis-Menten Model||Limiting Cases||High CS0|

418512|1||2| |3||4||5||6||7||8||Enzyme Kinetics: Michaelis-Menten||Michaelis-Menten Model||Limiting Cases||Intermediate|

418601|1||2| |3||4||5||6||7||8||Enzyme Kinetics: Michaelis-Menten||Michaelis-Menten Model||Michaelis-Menten Equation||Standard Form|

418602|1||2| |3||4||5||6||7||8||Enzyme Kinetics: Michaelis-Menten||Michaelis-Menten Model||Michaelis-Menten Equation||Initial Rate|

418603|1||2| |3||4||5||6||7||8||Enzyme Kinetics: Michaelis-Menten||Estimation of KM and Vmax||Linearized Form||Lineaweaver-Burk Plot|

418604|1||2| |3||4||5||6||7||8||Enzyme Kinetics: Michaelis-Menten||Estimation of KM and Vmax||Linearized Form of Integrated Michaelis-Menten Equation||Constant-volume batch reactor|

418605|1||2| |3||4||5||6||7||8||Enzyme Kinetics: Michaelis-Menten||Single-Substrate Inhibition||Rate Law||Reaction Rate|

418606|1||2| |3||4||5||6||7||8||Enzyme Kinetics: Michaelis-Menten||Single-Substrate Inhibition||Rate Law||Equilibrium Constant|

418607|1||2| |3||4||5||6||7||8||Enzyme Kinetics: Michaelis-Menten||Single-Substrate Inhibition||Maximum Rate|||