Читать книгу Petroleum Refining Design and Applications Handbook - A. Kayode Coker - Страница 2
Table of Contents
Оглавление1 Cover
5 Preface
7 13 Rules of Thumb—Summary 13.0 Introduction
8 14 Process Planning, Scheduling, and Flowsheet Design 14.1 Introduction 14.2 Organizational Structure 14.3 Role of the Process Design Engineer 14.4 Computer-Aided Flowsheeting 14.5 Flowsheets—Types 14.6 Flowsheet Presentation 14.7 General Arrangements Guide 14.8 Computer-Aided Flowsheet Design/Drafting 14.9 Flowsheet Symbols 14.10 Line Symbols and Designations 14.11 Materials of Construction for Lines 14.12 Test Pressure for Lines 14.13 Working Schedules 14.14 Information Checklists 14.15 Basic Engineering and Front End Engineering Design (FEED) References
9 15 Fluid Flow 15.1 Introduction 15.2 Flow of Fluids in Pipes 15.3 Scope 15.4 Basis 15.5 Incompressible Flow 15.6 Compressible Flow: Vapors and Gases [4] 15.7 Important Pressure Level References 15.8 Factors of “Safety” for Design Basis 15.9 Pipe, Fittings, and Valves 15.10 Pipe 15.11 Total Line Pressure Drop 15.12 Reynolds Number, Re (Sometimes Used NRe) 15.13 Pipe Relative Roughness 15.14 Darcy Friction Factor, f 15.15 Friction Head Loss (Resistance) in Pipe, Fittings, and Connections 15.16 Oil System Piping 15.17 Pressure Drop in Fittings, Valves, and Connections 15.18 Resistance of Valves 15.19 Flow Coefficients for Valves, Cv 15.20 Flow Meters Conclusion 15.21 Estimation of Pressure Loss Across Control Valves 15.22 The Direct Design of a Control Valve 15.23 Water Hammer 15.24 Friction Pressure Drop for Compressible Fluid Flow 15.25 Darcy Rational Relation for Compressible Vapors and Gases 15.26 Velocity of Compressible Fluids in Pipe 15.27 Procedure 15.28 Friction Drop for Compressible Natural Gas in Long Pipe Lines 15.29 Panhandle-A Gas Flow Formula 15.30 Modified Panhandle Flow Formula 15.31 American Gas Association (AGA) Dry Gas Method 15.32 Complex Pipe Systems Handling Natural (or Similar) Gas 15.33 Two-Phase Liquid and Gas Flow in Process Piping 15.34 UniSim Design PIPESYS 15.35 Pipe Line Safety 15.36 Mitigating Pipeline Hazards 15.37 Examples of Safety Design Concerns 15.38 Safety Incidents Related With Pipeworks and Materials of Construction 15.39 Lessons Learned From Piping Designs 15.40 Design of Safer Piping Nomenclature Greek Symbols Subscripts References
10 16 Pumps 16.1 Pumping of Liquids 16.2 Pump Design Standardization 16.3 Basic Parts of a Centrifugal Pump 16.4 Centrifugal Pump Selection 16.5 Hydraulic Characteristics for Centrifugal Pumps 16.6 Suction Head or Suction Lift, hs 16.7 Discharge Head, hd 16.8 Velocity Head 16.9 Friction 16.10 Net Positive Suction Head (NPSH) and Pump Suction 16.11 General Suction System 16.12 Reductions in NPSHR 16.13 Charting NPSHR Values of Pumps 16.14 Net Positive Suction Head (NPSH) 16.15 NPSH Requirement for Liquids Saturation With Dissolved Gases 16.16 Specific Speed 16.17 Rotative Speed 16.18 Pumping Systems and Performance 16.19 Power Requirements for Pumping Through Process Lines 16.20 Affinity Laws 16.21 Centrifugal Pump Efficiency 16.22 Effects of Viscosity 16.23 Temperature Rise and Minimum Flow 16.24 Centrifugal Pump Specifications 16.25 Number of Pumping Units 16.26 Rotary Pumps 16.27 Reciprocating Pumps 16.28 Pump Selection 16.29 Selection Rules-of-Thumb 16.30 Case Studies 16.31 Pump Cavitations 16.32 Pump Fundamentals 16.33 Operating Philosophy 16.34 Piping 16.35 Troubleshooting Checklist for Centrifugal Pumps Nomenclature Subscripts Greek Symbols References
11 17 Compression Equipment 17.1 Introduction 17.2 General Application Guide 17.3 Specification Guides 17.4 General Considerations for Any Type of Compressor Flow Conditions 17.5 Reciprocating Compression 17.6 Suction and Discharge Valves 17.7 Specification Sheet 17.8 Performance Considerations 17.9 Compressor Performance Characteristics 17.10 Hydrogen Use in the Refinery Nomenclature Greek Symbols Subscripts References
12 Glossary of Petroleum and Technical Terminology
13 Appendix D
14 Appendix E
15 Index
