Deactivation of Heavy Oil Hydroprocessing Catalysts (eBook)

Jorge Ancheyta is Manager of Products for the Transformation of Crude Oil at the Mexican Institute of Petroleum (IMP), where he has worked since 1989. His work centers on the development and application of petroleum refining catalysts, kinetic and reactor models, and process technologies mainly in catalytic cracking, catalytic reforming, middle distillate hydrotreating and heavy oils upgrading. He has been awarded the National Researcher Highest Distinction by the Mexican government and is a member of the Mexican Academy of Science. He is the author of five other books, incuding Modeling and Simulation of Catalytic Reactors for Petroleum Refining (Wiley, 2011). He has also been guest editor of various international journals.

Preface

Nomenclature

Chapter 1: PROPERTIES OF HEAVY OILS

1.1. Introduction

1.2. Refining of petroleum

1.3. Properties of heavy petroleum

1.4. Assay of petroleum

Chapter 2: PROPERTIES OF CATALYSTS FOR HEAVY OIL HYDROPROCESSING

2.1. Introduction

2.2. Hydroprocessing catalyst

2.3. Characterization of catalysts

2.4. General aspects for developing catalyst for hydro processing of heavy crude

2.5. Catalyst for Maya crude oil hydroprocessing

2.6. Concluding remarks

References

Chapter 3: DEACTIVATION OF HYDROPROCESSING CATALYSTS

3.1. Introduction

3.2. Hydroprocessing of heavy oils

3.3. Mechanisms of catalyst deactivation

3.4. Asphaltenes and their effect on catalyst deactivation

References

Chapter 4: CHARACTERIZATION OF SPENT HYDROPROCESSING CATALYST

4.1. Introduction

4.2. Characterization techniques

4.3. Early deactivation of different supported como catalysts

4.4. Carbon and metal deposition during the hydro processing of Maya crude oil

4.5. Characterization study of NiMo/SiO2-Al2O3 spent hydro processing catalysts for heavy oils

4.6. Characterization of spent catalysts along a bench-scale reactor

4.7. Hydrodesulfurization activity of used hydrotreating catalysts

References

Chapter 5: MODELING CATALYST DEACTIVATION

5.1. Introduction

5.2. Effect of reactor configuration on the cycle length of heavy oil fixed-bed hydro processing

5.3. Effect of different heavy feedstocks on the deactivation of a commercial catalyst

5.4. Modeling the deactivation by metal deposition of heavy oil hydrotreating catalyst

5.5. Kinetic model for hydrocracking of heavy oil in a CSTR involving short term catalyst deactivation

5.6. Modeling the kinetics of parallel thermal and catalytic hydrotreating of heavy oil

5.7. Modeling catalyst deactivation during hydrocracking of atmospheric residue by using the continuous kinetic lumping model

5.8. Application of a three-stage approach for modeling the complete period of catalyst deactivation during hydrotreating of heavy oil

References

Index