http://www.loc.gov/mods/v3 http://www.loc.gov/standards/mods/v3/mods-3-2.xsd
According to NACE (National Association of Corrosion Engineers), the total annual cost of corrosion in petroleum refining takes up 3.7 billion in the US alone. Corrosion control is always a challenge for the downstream industry, but as the quality of feedstock is declining due to refineries accepting more of the heavy and shale gas and oil resources that are more readily available today, refinery managers, petroleum and natural gas engineers are unprepared for the new set of corrosion problems that are showing up in their equipment and processing units.
Front Cover; Oil and Gas Corrosion Prevention; Copyright Page; Contents; Preface; 2 Materials of Construction for Refinery Units; 2.1 Introduction; 2.2 Metals and Alloys; 2.2.1 Metals; 2.2.2 Alloys; 2.2.2.1 Ferrous Alloys; 2.2.2.2 Austenitic Alloys; 2.2.2.3 Ferritic Alloys; 2.2.3 Other Alloys; 2.3 Selection of Materials; 2.3.1 Distillation; 2.3.2 Coking; 2.3.3 Fluid Catalytic Cracking; 2.3.4 Hydroprocesses; 2.3.4.1 Hydrotreating and Hydrodesulfurization; 2.3.4.2 Hydrocracking; 2.3.5 Other Processes; 2.3.5.1 Catalytic Reforming; 2.3.5.2 Alkylation; 2.3.5.3 Polymerization.
2.3.5.4 Hydrogen Production2.3.6 Sour Water Strippers; 2.3.7 Cooling Water Systems; 2.3.7.1 Freshwater and Polluted Water; 2.3.7.2 Polluted Saltwater; 2.3.7.3 Cooling Towers; 2.3.8 Gas Processing; 2.3.8.1 General; 2.3.8.2 Amine Plant; 2.4 Pipes and Pipelines; 2.4.1 Low- and High-Temperature Services; 2.4.2 Water-Hydrogen Sulfide Service; 2.4.3 Hydrocarbon-Hydrogen Service; References; 3 Corrosion in Refinery Units; 3.1 Introduction; 3.2 Storage Tanks; 3.3 Desalting; 3.3.1 Conventional Crude Oil; 3.3.2 Heavy Crude Oil; 3.3.3 Opportunity Crude Oil and Oil from Tight Shale; 3.4 Distillation.
3.4.1 Hydrogen Chloride/Hydrogen Sulfide Corrosion3.5 Naphthenic Acid Corrosion; 3.6 Coking; 3.7 Catalytic Cracking; 3.8 Hydroprocesses; 3.9 Product Improvement Processes; 3.9.1 Solvent Processes; 3.9.2 Reforming Processes; 3.9.3 Alkylation Processes; 3.9.4 Polymerization Processes; 3.9.5 Isomerization Processes; 3.9.6 Caustic Treating Processes; References; Further Reading; 4 Corrosion in Gas Processing Plants; 4.1 Introduction; 4.2 Gas Streams; 4.2.1 Natural Gas; 4.2.2 Refinery Gas; 4.3 Corrosion Chemistry; 4.3.1 Hydrogen Sulfide; 4.3.2 Carbon Dioxide; 4.3.3 Other Corrosive Agents.
4.4 Gas Cleaning4.4.1 Acid-Gas Removal; 4.4.2 Sour Water Stripper; 4.4.3 Sulfur Recovery Unit; 4.4.3.1 Claus Process; 4.4.3.2 Other Processes; 4.4.4 Acid-Flare Header; References; Further Reading; 5 Corrosion in Other Systems; 5.1 Introduction; 5.2 Heat Exchangers; 5.3 Pipelines; 5.4 Offshore Corrosion; 5.4.1 Offshore Structures; 5.4.2 Stainless Steel; 5.4.3 Carbon Steel; 5.4.4 Copper Base Alloys; 5.4.5 Corrosion by Polluted Water; References; 6 Corrosion Monitoring and Control; 6.1 Introduction; 6.2 Corrosion Monitoring; 6.2.1 Corrosion Coupons; 6.2.2 Electrical Resistance Methods.
6.2.3 Field Signature Methods6.2.4 Linear Polarization Resistance Monitoring; 6.2.5 Galvanic Monitoring; 6.2.6 Other Methods; 6.2.6.1 Iron Powder Test; 6.2.6.2 Hydrogen Penetration Monitoring; 6.2.6.3 Radiography; 6.2.6.4 Biological Monitoring; 6.2.7 Real-Time Monitoring; 6.3 Corrosion Control and Inhibition; 6.3.1 Cathodic Protection; 6.3.2 Galvanic Cathodic Protection; 6.3.3 Impressed Current Cathodic Protection; 6.3.4 Cathodic Shielding; 6.4 Corrosion Control in Refineries; 6.4.1 Crude Oil Quality; 6.4.2 Acidic Corrosion; 6.4.3 Sulfidic Corrosion; 6.4.4 Carburization.
Plný text je dostupný pouze z IP adres počítačů Univerzity Tomáše Bati ve Zlíně nebo vzdáleným přístupem pro zaměstnance a studenty