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عدد المساهمات : 18996 التقييم : 35494 تاريخ التسجيل : 01/07/2009 الدولة : مصر العمل : مدير منتدى هندسة الإنتاج والتصميم الميكانيكى
| موضوع: كتاب Guidelines for Design Solutions for Process Equipment Failures الأربعاء 25 سبتمبر 2013, 6:38 am | |
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أخوانى فى الله أحضرت لكم كتاب Guidelines for Design Solutions for Process Equipment Failures
ويتناول الموضوعات الأتية :
Foreword xiii Preface xv Acknowledgments xvii 1 Introduction 1 11 Objectives 1 12 Scope 2 13 Background 2 14 Applicability and Audience 3 15 Organization of This Book 3 16 References 4 Suggested AdditionalReading 4 2 Technique for Selecting the Design Bases for Process Safety Systems 5 21 Risk-Based Design Decisions 5 22 The Concept of Risk 7 23 Selection of Design Bases for Safety Systems 9 231 Step 1: Identify Failure Scenarios 9 232 Step 2: Estimate the Consequences 9 233 Step 3: Determine Tolerability of Consequences 11 234 Step 4: Estimate Likelihood and Risk 11 235 Step 5: Determine Tolerability ofRisk 12 236 Step 6: Consider Enhanced and/or Alternative Designs 12 237 Step 7: Evaluate Enhancements and/or Alternatives 13 238 Step 8: Determine Tolerability of Risk and Cost 13 239 Step 9: Document Results 13 24 Guidelines for Risk Tolerability 14 25 Potential Process Safety Systems Design Solutions 20 251 Four Categories of Design Solutions 20 252 Characteristics of Design Solution Categories 24 26 Applying the Risk-Based Design Bases Selection Technique 27 261 Locking Open a Valve (a Simple Design Case) 27 262 Selecting the Relief System Basis for a Reactor (a Complex Design Case) 30 27 References 34 Suggested AdditionalReading 35 3 Vessels 37 31 Introduction 37 32 Past Incidents 37 321 Storage Tank Autopolymerization Incident 37 322 Storage Tank Stratification Incident 38 323 Batch Pharmaceutical Reactor Accident 39 33 Failure Scenarios and Design Solutions 40 34 Discussion 40 341 Use of Potential Design Solutions Table 40 342 Special Considerations 41 35 References 43 Suggested AdditionalReading 44 Table 3 Failure Scenarios for Vessels 45 4 Reactors 61 41 Introduction 61 42 Past Incidents 61 421 Seveso Runaway Reaction 62 422 3,4-Dichloroaniline Autoclave Incident 62 423 Continuous Sulfonation Reaction Explosion 63 43 Failure Scenarios and Design Solutions 63 44 Discussion 64 441 Use of Potential Design Solutions Table 64 442 General Discussion 64 443 Special Considerations 66 45 References 67 Suggested AdditionalReading 68 Table 4 Failure Scenarios for Reactors 69 5 Mass Transfer Equipment 79 51 Introduction 79 52 Past Incidents 79 521 Distillation Column Critical Concentration 80 522 Ethylene Purifier Vessel Rupture 80 523 Ignition of Pyrophoric Materials in Gasoline Fractionator 81 53 Failure Scenarios and Design Solutions 82 54 Discussion 82 541 Use of Potential Design Solutions Table 82 542 Special Considerations 82 55 References 83 Suggested AdditionalReading 83 Table 5 Failure Scenarios for Mass Transfer Equipment 84 6 Heat Transfer Equipment 89 61 Introduction 89 62 Past Incidents 89 621 Ethylene Oxide Redistillation Column Explosion 89 622 Brittle Fracture of a Heat Exchanger 90 623 Cold Box Explosion 91 63 Failure Scenarios and Design Solutions 92 64 Discussion 92 641 Use of Potential Design Solutions Table 92 642 Special Considerations 92 65 References 93 Suggested AdditionalReading 94 Table 6 Failure Scenarios for Heat Transfer Equipment 95 7 Dryers 101 71 Introduction 101 72 Past Incidents 101 721 Drying of Compound Fertilizers 102 722 Fires in CelluloseAcetate Dryer 102 723 Pharmaceutical Powder Dryer Fire and Explosion 102 73 Failure Scenarios and Design Solutions 103 74 Discussion 103 741 Use of Potential Design Solutions Table 103 742 Special Considerations 103 75 References 104 Suggested AdditionalReading 104 Table 7 Failure Scenarios for Dryers 106 8 Fluid Transfer Equipment 117 81 Introduction 117 82 Past Incidents 117 821 Reciprocating Pump Leak 117 822 Pump Leak Fire 118 823 Compressor Fireand Explosion 118 824 Start-up of Parallel Centrifugal Pumps 119 83 Failure Scenarios and Design Solutions 119 84 Discussion 119 841 Use of Potential Design Solutions Table 119 842 Special Considerations 120 85 References 121 Suggested AdditionalReading 121 Table 8 Failure Scenarios for Fluid Transfer Equipment 122 9 Solid-Fluid Separators 127 91 Introduction 127 92 Past Incidents 127 921 Batch Centrifuge Explosion 128 922 Filter Explosion 128 923 Dust CollectorExplosion 129 93 Failure Scenarios and Design Solutions 129 94 Discussion 130 941 Use of Potential Design Solutions Table 130 942 Special Considerations 130 95 References 131 Suggested AdditionalReading 131 Table 9 Failure Scenarios for Solid-Fluid Separators 132 10 Solids Handling and Processing Equipment 137 101 Introduction 137 102 Past Incidents 138 1021 Silicon Grinder Fireand Explosion 138 1022 Blowing Agent Blender Operation Explosion Incident 138 1023 Screw ConveyorExplosion 139 1024 Bucket Elevator Explosion 139 103 Failure Scenarios and Design Solutions 139 104 Discussion 140 1041 Use of Potential Design Solutions Table 140 1042 General Discussion 140 1043 Special Considerations 140 105 References 142 Suggested AdditionalReading 143 Table 10 Failure Scenarios for Solids Handling and Processing Equipment 144 11 Fired Equipment 149 111 Introduction 149 112 Past Incidents 149 1121 Light-off Error 149 1122 Ethylene Cracking Furnace Overfiring 150 1123 Furnace TubeFailure 150 113 Failure Scenarios and Design Solutions 151 114 Discussion 151 1141 Use of Potential Design Solutions Table 151 1142 Special Considerations 151 115 References 152 Suggested AdditionalReading 153 Table 11 Failure Scenarios for Fired Equipment 154 12 Piping and Piping Components 161 121 Introduction 161 122 Past Incidents 161 1221 Flixborough Expansion Joint Failure 161 1222 Chemical Storage Terminal Fire 162 1223 Line Pluggage 163 1224 External Corrosion 163 123 Failure Scenarios and Design Solutions 163 124 Discussion 164 1241 Use of Potential Design Solutions Table 164 1242 Special Considerations 164 125 References 166 Suggested AdditionalReading 166 Table 12 Failure Scenario for Piping and Piping Components 168 Appendix A Example Problem: Batch Chemical Reactor 179 A1 System Description 179 A2 General Information Requirements 181 A3 PSS Discussion for Batch Reactors 182 A31 Vessel Design and Primary Containment 182 A32 Control Systems and Safe Automation 183 A33 Pressure and Vacuum Relief 186 A34 Fixed Fire Protection and Passive Mitigation 187 A4 Selection of Design Bases for Safety Systems 187 A5 Ignition of Flammable Atmosphere in the Reactor Vapor Space Caused by Static Discharge Spark (Failure ScenarioA) 193 A6 Cooling System Control Failure (Failure Scenario B) 194 A7 External Fire (Failure Scenario C) 196 A8 Loss of Sealing Fluid to Reactor Agitator Mechanical Seal (Failure Scenario D) 197 A9 Ignition of Flammable Atmosphere in Reactor Vapor Space Caused by Hot Mechanical Seal (Failure Scenario E) 199 A10 Documentation 200 References 201 Suggested AdditionalReading 201 Appendix B Example Problem: Distillation System 203 B1 System Description 204 B2 General Information Requirements 204 B3 PSS Discussion for Distillation Operations 206 B31 Vessel Design and Primary Containment 206 B32 Control Systems and Safe Automation 207 B33 Pressure and Vacuum Relief 209 B34 Fixed Fire Protection, Passive Mitigation and System-Wide Concerns 210 B4 Design Basis Selection Process 210 B5 Uncontrolled Energy Input (Failure ScenarioA) 215 B6 External Fire (Failure Scenario B) 220 B7 Internal Deflagration (Failure ScenarioC) 225 B8 Vacuum Collapse of the Column (Failure Scenario D)226 B9 Blocked-in Liquids in Heat Transfer Equipment (Failure ScenarioE) 230 B10 Documentation 230 References 233 Suggested AdditionalReading 234 Glossary 235 Acronyms and Abbreviations 245 Index
أتمنى أن تستفيدوا منه وأن ينال إعجابكم رابط تنزيل كتاب Guidelines for Design Solutions for Process Equipment Failures
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محمد محمد أحمد مهندس فعال جدا جدا
عدد المساهمات : 654 التقييم : 694 تاريخ التسجيل : 14/11/2012 العمر : 32 الدولة : EGYPT العمل : Student الجامعة : Menoufia
| موضوع: رد: كتاب Guidelines for Design Solutions for Process Equipment Failures الأربعاء 25 سبتمبر 2013, 4:56 pm | |
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جزاك الله كل خير يا بش مهندس |
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