توضیحاتی در مورد کتاب Heterogeneous Catalysis: Essentials for Chemical Engineers
نام کتاب : Heterogeneous Catalysis: Essentials for Chemical Engineers
عنوان ترجمه شده به فارسی : کاتالیز ناهمگن: ملزومات برای مهندسان شیمی
سری : De Gruyter Textbook
نویسندگان : Shaikh A.A.
ناشر : Walter de Gruyter
سال نشر : 2020
تعداد صفحات : 162
ISBN (شابک) : 9783110624854
زبان کتاب : English
فرمت کتاب : pdf
حجم کتاب : 3 مگابایت
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فهرست مطالب :
Cover
Half Title
Also of Interest
Heterogeneous Catalysis: Essentials for Chemical Engineers
Copyright
Preface
Acknowledgments
Contents
1. Introduction
1.1 Industrial importance of heterogeneous catalysis
1.2 General characteristics of solid catalysts
1.2.1 Activation energy
1.2.2 Functionality and classification
1.2.3 Selectivity of solid catalysts
1.2.4 The catalytic site
1.2.5 Composition of solid catalysts
1.2.6 Naming of solid catalysts
1.3 The catalytic sequence
References
2. Adsorption
2.1 Types of adsorption
2.2 Comparison between physical and chemical adsorption
2.2.1 Surface coverage
2.2.2 Heat of adsorption
2.2.3 Catalytic cycle
2.2.4 Rate of adsorption
2.3 Adsorption isotherms
2.3.1 Langmuir isotherm
2.3.2 Competitive adsorption
2.3.3 Determination of surface area
2.4 Other isotherms
2.4.1 BET isotherm
2.4.2 Surface area by BET isotherm
References
3. Characterization of solid catalysts
3.1 Physical characterization
3.1.1 Determination of surface area
3.1.2 Measurement of total pore volume
3.1.3 Pore-size distribution
3.1.3.1 Mercury-porosimetry method
3.2 Chemical and structural characterization
3.2.1 Electron microscopy
3.3 Mechanical characterization
References
4. Kinetics of catalytic reactions
4.1 Classification of kinetic models
4.2 Langmuir–Hinshelwood (L-H) model
4.2.1 Irreversible, unimolecular, surface reactions
4.2.2 Irreversible, bimolecular, surface reactions
4.2.3 Inhibition in bimolecular surface reactions
4.2.4 Reversible, unimolecular, reactions
4.2.5 Reversible, bimolecular, reactions
4.2.6 Irreversible, bimolecular, reactions: Different sites
4.3 Eley–Rideal (E-R) model
4.4 Effect of temperature on reaction rate
References
5. Transport effects in catalytic reactions
5.1 External and internal mass transfer
5.2 The effectiveness factor
5.2.1 Isothermal first-order catalytic reactions
5.2.2 Effectiveness factor for first-order reactions
5.2.3 Effectiveness factors for other catalyst shapes
5.2.4 Parameter estimation
5.3 Behavior of observed reaction rate: falsification of kinetic data
5.4 Laboratory reactors
References
6. Deactivation of solid catalysts
6.1 Causes of deactivation
6.2 Deactivation by thermal degradation
6.3 Deactivation by fouling
6.4 Deactivation by poisoning
6.5 Other causes of deactivation
6.6 Kinetics of catalyst deactivation
6.6.1 Catalyst activity
6.6.2 Kinetics of catalyst coking
6.7 Catalyst reactivation
References
7. Industrial catalytic reactors
7.1 Types of reactors and applications
7.1.1 Packed-bed reactor family
7.1.2 Fluidized-bed reactor family
7.2 Design of isothermal packed-bed reactor
7.2.1 Cautionary remarks
7.3 Three-phase catalytic reactors
References
8. Major industrial applications
8.1 Applications in petroleum refining
8.2 Applications in the petrochemicals industry
8.3 Applications in environmental protection
References
9. Computational case studies
9.1 Published models and simulators
9.1.1 Adsorption isotherms of C2H4 in NaX zeolite
9.1.2 Surface kinetics with pore diffusion resistance
9.1.3 Nonisothermal effectiveness factor
9.1.4 Conversion of ethylbenzene to styrene in the presence of steam
9.1.5 Pressure drop in a packed-bed reactor
9.1.6 Slurry reactor with declining catalyst activity
9.2 Applied catalysis design problem
9.3 Open-ended catalysis design problems
9.3.1 Elementary computational thought experiment
9.3.2 Intermediate computational thought experiment
References
Problems
Finale
Index