Search engine for discovering works of Art, research articles, and books related to Art and Culture
Javascript must be enabled to continue!
Principles of Chemical Reaction Engineering
View through CrossRef
Abstract
The article contains sections titled:
1.
Introduction
2.
Fundamentals
2.1.
Chemical Rates
2.2.
Relative Degree of Conversion
2.3.
Selectivity and Yield
3.
Microkinetics
3.1.
Elementary Reactions
3.1.1.
Fundamentals
3.1.2.
Influence of Temperature
3.1.3.
Influence of Concentration
3.2.
Chemical Equilibria
3.3.
Complex Reaction Schemes
3.3.1.
Fundamentals
3.3.2.
Polymerization Reactions
3.3.2.1.
Conversion ‐ Time Curve
3.3.2.2.
Radical Intermediates Concentration
3.3.3.
Heterogeneous Catalytic Reactions
3.3.3.1.
Monomolecular Reactions
3.3.3.2.
Bimolecular Reactions
3.3.4.
Biochemical Reactions
4.
Macrokinetics: Single‐Phase Systems
4.1.
Introduction
4.2.
Macromixing
4.2.1.
Residence‐Time Distribution (RTD)
4.2.2.
Batch Reactor (BR)
4.2.3.
Plug‐Flow Reactor (PFR)
4.2.4.
Continuous, Ideally Stirred Tank Reactor (CISTR)
4.3.
Micromixing
4.4.
Sequence of Mixing
5.
Macrokinetics: Multiphase Systems‐Part I: Mass Transfer without Reaction
5.1.
Introduction
5.2.
Penetration Models
5.3.
Stagnant Film Model
5.4.
Mass‐Transfer Coefficients
6.
Macrokinetics: Multi‐phase Systems‐Part II: Mass Transfer with Reaction
6.1.
Mass Transfer with Reaction in Series
6.1.1.
Introduction
6.1.2.
Monomolecular First‐Order Kinetics
6.1.3.
Arbitrary Monomolecular Kinetics
6.1.4.
Multiple Phases
6.1.5.
Bimolecular Reactions
6.1.6.
Case Study: Shrinking Core Model
6.1.7.
Selectivities of Multiple Reactions
6.1.7.1.
Introduction
6.1.7.2.
Parallel Reactions
6.1.7.3.
Consecutive Reactions
6.1.7.4.
Complex Reaction Schemes
6.2.
Mass Transfer with Simultaneous Reaction
6.2.1.
Introduction
6.2.2.
Reaction of Gases in Porous Solids
6.2.2.1.
Introduction
6.2.2.2.
Monomolecular First‐Order Kinetics
6.2.2.3.
Monomolecular Arbitrary Kinetics
6.2.2.4.
Bimolecular Reactions
6.2.2.5.
Anisotropic Catalyst Pellets
6.2.3.
Reactions of Gases in Liquids‐Part I: Gaseous Reactants Only
6.2.3.1.
Introduction
6.2.3.2.
Higbie Penetration Model
6.2.3.3.
Surface Renewal Model
6.2.3.4.
Stagnant Film Model
6.2.3.5.
Comparison of Models for First‐Order Kinetics
6.2.3.6.
Comparison of Hatta Numbers with Thiele Moduli
6.2.3.7.
Hatta Numbers for Arbitrary Kinetics
6.2.3.8.
Case Study: Ideally Mixed Gas ‐ Liquid Reactors
6.2.3.9.
Selectivities of Multiple Reactions
6.2.4.
Reactions of Gases in Liquids‐Part II:Reactants from both the Gas and the Liquid
6.2.4.1.
Introduction
6.2.4.2.
Slow Reaction
6.2.4.3.
Fast Reaction
6.2.4.4.
Instantaneous Reaction
6.2.4.5.
Van Krevelen ‐ Hoftijzer Approximation
6.2.4.6.
Arbitrary Kinetics
6.2.4.7.
Selectivities of Multiple Reactions
6.3.
Combination of Simultaneous and Series Mass Transfer and Reaction
7.
Macrokinetics: Multiphase Systems‐Part III: Mass and Heat Transfer with Reaction
7.1.
Introduction
7.2.
Mass and Heat Transfer with Reaction in Series
7.2.1.
Particle Mass and Heat Balances
7.2.2.
Particle Multiplicity
7.3.
Mass and Heat Transfer with Simultaneous Reaction
7.3.1.
Frank ‐ Kamenetzki Approximation
7.3.2.
Thiele Moduli and Hatta Numbers
Title: Principles of Chemical Reaction Engineering
Description:
Abstract
The article contains sections titled:
1.
Introduction
2.
Fundamentals
2.
1.
Chemical Rates
2.
2.
Relative Degree of Conversion
2.
3.
Selectivity and Yield
3.
Microkinetics
3.
1.
Elementary Reactions
3.
1.
1.
Fundamentals
3.
1.
2.
Influence of Temperature
3.
1.
3.
Influence of Concentration
3.
2.
Chemical Equilibria
3.
3.
Complex Reaction Schemes
3.
3.
1.
Fundamentals
3.
3.
2.
Polymerization Reactions
3.
3.
2.
1.
Conversion ‐ Time Curve
3.
3.
2.
2.
Radical Intermediates Concentration
3.
3.
3.
Heterogeneous Catalytic Reactions
3.
3.
3.
1.
Monomolecular Reactions
3.
3.
3.
2.
Bimolecular Reactions
3.
3.
4.
Biochemical Reactions
4.
Macrokinetics: Single‐Phase Systems
4.
1.
Introduction
4.
2.
Macromixing
4.
2.
1.
Residence‐Time Distribution (RTD)
4.
2.
2.
Batch Reactor (BR)
4.
2.
3.
Plug‐Flow Reactor (PFR)
4.
2.
4.
Continuous, Ideally Stirred Tank Reactor (CISTR)
4.
3.
Micromixing
4.
4.
Sequence of Mixing
5.
Macrokinetics: Multiphase Systems‐Part I: Mass Transfer without Reaction
5.
1.
Introduction
5.
2.
Penetration Models
5.
3.
Stagnant Film Model
5.
4.
Mass‐Transfer Coefficients
6.
Macrokinetics: Multi‐phase Systems‐Part II: Mass Transfer with Reaction
6.
1.
Mass Transfer with Reaction in Series
6.
1.
1.
Introduction
6.
1.
2.
Monomolecular First‐Order Kinetics
6.
1.
3.
Arbitrary Monomolecular Kinetics
6.
1.
4.
Multiple Phases
6.
1.
5.
Bimolecular Reactions
6.
1.
6.
Case Study: Shrinking Core Model
6.
1.
7.
Selectivities of Multiple Reactions
6.
1.
7.
1.
Introduction
6.
1.
7.
2.
Parallel Reactions
6.
1.
7.
3.
Consecutive Reactions
6.
1.
7.
4.
Complex Reaction Schemes
6.
2.
Mass Transfer with Simultaneous Reaction
6.
2.
1.
Introduction
6.
2.
2.
Reaction of Gases in Porous Solids
6.
2.
2.
1.
Introduction
6.
2.
2.
2.
Monomolecular First‐Order Kinetics
6.
2.
2.
3.
Monomolecular Arbitrary Kinetics
6.
2.
2.
4.
Bimolecular Reactions
6.
2.
2.
5.
Anisotropic Catalyst Pellets
6.
2.
3.
Reactions of Gases in Liquids‐Part I: Gaseous Reactants Only
6.
2.
3.
1.
Introduction
6.
2.
3.
2.
Higbie Penetration Model
6.
2.
3.
3.
Surface Renewal Model
6.
2.
3.
4.
Stagnant Film Model
6.
2.
3.
5.
Comparison of Models for First‐Order Kinetics
6.
2.
3.
6.
Comparison of Hatta Numbers with Thiele Moduli
6.
2.
3.
7.
Hatta Numbers for Arbitrary Kinetics
6.
2.
3.
8.
Case Study: Ideally Mixed Gas ‐ Liquid Reactors
6.
2.
3.
9.
Selectivities of Multiple Reactions
6.
2.
4.
Reactions of Gases in Liquids‐Part II:Reactants from both the Gas and the Liquid
6.
2.
4.
1.
Introduction
6.
2.
4.
2.
Slow Reaction
6.
2.
4.
3.
Fast Reaction
6.
2.
4.
4.
Instantaneous Reaction
6.
2.
4.
5.
Van Krevelen ‐ Hoftijzer Approximation
6.
2.
4.
6.
Arbitrary Kinetics
6.
2.
4.
7.
Selectivities of Multiple Reactions
6.
3.
Combination of Simultaneous and Series Mass Transfer and Reaction
7.
Macrokinetics: Multiphase Systems‐Part III: Mass and Heat Transfer with Reaction
7.
1.
Introduction
7.
2.
Mass and Heat Transfer with Reaction in Series
7.
2.
1.
Particle Mass and Heat Balances
7.
2.
2.
Particle Multiplicity
7.
3.
Mass and Heat Transfer with Simultaneous Reaction
7.
3.
1.
Frank ‐ Kamenetzki Approximation
7.
3.
2.
Thiele Moduli and Hatta Numbers.
Related Results
Isolation, characterization and semi-synthesis of natural products dimeric amide alkaloids
Isolation, characterization and semi-synthesis of natural products dimeric amide alkaloids
Isolation, characterization of natural products dimeric amide alkaloids from roots of the Piper chaba Hunter. The synthesis of these products using intermolecular [4+2] cycloaddit...
Chemical Kinetics of the Microwave Effect on the Base Hydrolysis Reaction Rate of Benzyl Isobutyrate
Chemical Kinetics of the Microwave Effect on the Base Hydrolysis Reaction Rate of Benzyl Isobutyrate
Many experimental results regarding Arrhenius plot on various chemical reactions under microwave irradiation have been reported. According to these results, it can be confirmed in ...
Absolute value of enthalpy in chemical reaction
Absolute value of enthalpy in chemical reaction
Abstract
Enthalpy is a very ancient topic, and there has been almost no one discussion on its right and wrong in recent years. However, an absolu...
(Invited) Chemical Sensing in the Big Data Era: How and Where Does the Chemical World Store Its Information?
(Invited) Chemical Sensing in the Big Data Era: How and Where Does the Chemical World Store Its Information?
Introduction
In recent years, data analytics have emerged as an important tool for understanding many business and societal trends, and this has bee...
Market Demand versus Technological Development: the Future of Chemical Engineering
Market Demand versus Technological Development: the Future of Chemical Engineering
Abstract
In today’s economy, Chemical Engineering must respond to the changing needs of the chemical process industry in order to meet market demands. The evoluti...
Embedded Education Model for Postgraduate Chemical Engineering Ethics Based on Educational Community
Embedded Education Model for Postgraduate Chemical Engineering Ethics Based on Educational Community
As engineering exerts an increasingly profound impact on human society and the natural world, large scale, comprehensiveness, complexity, and growing engineering influence have bec...
Comparative study of Ziegler-Natta catalyst synthesis for ethylene polymerization
Comparative study of Ziegler-Natta catalyst synthesis for ethylene polymerization
Nowadays, polyethylene becomes more usage in olefin industries. Ziegler-Natta catalyst was used to synthesize polyethylene Therefore, it is important to develop this catalyst effic...
Wittig Reaction
Wittig Reaction
AbstractThe synthesis of an olefin from the reaction between a carbonyl compound (aldehyde or ketone) and a phosphonium ylide, via either a betaine and/or oxaphosphetane intermedia...