Explosion and fire (3 injured, potential offsite consequences) [[electronic resource] ] : First Chemical Corporation, Pascagoula, Mississippi, October 13, 2002 / / U.S. Chemical Safety and Hazard Investigation Board |
Pubbl/distr/stampa | [Washington, D.C.] : , : U.S. Chemical Safety and Hazard Investigation Board, , [2003] |
Descrizione fisica | 77 pages : digital, PDF file |
Collana | Investigation report / U.S. Chemical Safety and Hazard Investigation Board |
Soggetto topico |
Industrial accidents - Investigation - Mississippi - Pascagoula
Chemicals - Fires and fire prevention - Mississippi - Pascagoula Chemicals - Fires and fire prevention Industrial accidents - Investigation |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Altri titoli varianti | Explosion and fire |
Record Nr. | UNINA-9910697413303321 |
[Washington, D.C.] : , : U.S. Chemical Safety and Hazard Investigation Board, , [2003] | ||
Materiale a stampa | ||
Lo trovi qui: Univ. Federico II | ||
|
Guidelines for fire protection in chemical, petrochemical, and hydrocarbon processing facilities [[electronic resource]] |
Pubbl/distr/stampa | New York, NY, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2003 |
Descrizione fisica | 1 online resource (482 p.) |
Disciplina |
660.2804
660/.2804 |
Soggetto topico |
Chemical plants - Fires and fire prevention
Chemicals - Fires and fire prevention |
ISBN |
1-282-77417-4
9786612774171 0-470-92504-3 1-59124-664-4 0-470-92503-5 |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Guidelines for Fire Protection in Chemical, Petrochemical, and Hydrocarbon Processing Facilities; CONTENTS; Preface; Acknowledgments; Acronyms; 1 Introduction; 1.1. Scope; 1.2. Who Will Benefit from This Guideline?; 1.2.1. What Is Fire Protection?; 1.2.2. Examples; 1.3. Relation to Other CCPS Guidelines and Resources; 2 Management Overview; 2.1. Management Commitment; 2.2. Integration with Other Management Systems; 2.3. Balancing Protection; 2.4. Cost-Benefit; 3 Fire Protection Strategy; 3.1. Key Factors in a Fire Protection Strategy; 3.1.1. Acceptable Loss; 3.1.2. Cost of Fires
3.1.3. Insurance Coverage3.1.4. Installed Systems versus Emergency Response; 3.1.5. Prescriptive versus Performance-Based Design; 3.2. Developing a Fire Protection Strategy; 3.3. Integration with Other Management Systems; 3.4. Integration with the Lifecycle of a Facility; 3.4.1. Design; 3.4.2. Construction and Commissioning; 3.4.3. Operations; 3.4.4. Decommissioning; 4 Overview of Fire Prevention Elements; 4.1. Audit Program; 4.1.1. The Audit Process; 4.1.2. Qualifications and Staffing; 4.1.3. Frequency of Audits; 4.1.4. Application to Fire Protection; 4.2. Layout and Spacing 4.3. Control of Ignition Sources4.3.1. Electrical Area Classification; 4.3.2. Personal Ignition Sources; 4.3.3. Hot Work; 4.3.4. Static Electricity; 4.4. Employee Training; 4.5. Housekeeping; 4.5.1. Housekeeping Program; 4.5.2. Process Area Housekeeping; 4.5.3. Dust Control; 4.5.4. Inappropriate Storage and Handling; 4.5.5. Housekeeping and Equipment; 4.5.6. Cleaning Materials; 4.6. Incident Investigation; 4.6.1. Incident Investigation Process; 4.6.2. Application to Fire Prevention; 4.7. Inherently Safer Design; 4.8. Plant Maintenance; 4.8.1. Poor Maintenance 4.8.2. Good Maintenance Program Elements4.9. Management of Change; 4.9.1. Personnel Changes; 4.9.2. Process Changes; 4.9.3. Maintenance Turnarounds; 4.10. Material Hazards; 4.10.1. Materials Hazard Evaluation Program; 4.10.2. Material Safety Data Sheets; 4.11. Alarm and Surveillance; 4.11.1. Security; 5 Fire Hazard Analysis; 5.1. Hazardous Chemicals and Processes; 5.2. Recognize What You Want to Understand; 5.3. Identification of Inventories; 5.4. Define Fire Scenarios; 5.5. Calculate Potential Fire Hazard; 5.5.1. Ignition and Combustion; 5.5.2. Heat Transfer 5.5.3. Fire Growth and Heat Release5.5.4. Solid Materials; 5.5.5. Enclosure Effects; 5.6. Flash Fires; 5.7. Fireballs; 5.8. Liquid or Pool Fires; 5.8.1. Uelease Rate; 5.8.2. Pool Size; 5.8.3. Flame Height; 5.8.4. Duration of Burning Pools; 5.8.5. Heat Transfer; 5.8.6. Convective Heat Transfer above the Plume; 5.9. Gas and Jet Fires; 5.9.1. Estimating Discharge Rates; 5.9.2. Jet Flame Size; 5.9.3. Heat Transfer; 5.9.4. Radiative Exposure; 5.10. Solid Fires; 5.11. Fire Impact to Personnel, Structures, and Equipment; 5.11.1. Impact to Personnel; 5.11.2. Impact to Structures 5.11.3. Thermal and Nonthermal Impact on Electrical and Electronic Equipment |
Record Nr. | UNINA-9910143237903321 |
New York, NY, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2003 | ||
Materiale a stampa | ||
Lo trovi qui: Univ. Federico II | ||
|
Guidelines for fire protection in chemical, petrochemical, and hydrocarbon processing facilities [[electronic resource]] |
Pubbl/distr/stampa | New York, NY, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2003 |
Descrizione fisica | 1 online resource (482 p.) |
Disciplina |
660.2804
660/.2804 |
Soggetto topico |
Chemical plants - Fires and fire prevention
Chemicals - Fires and fire prevention |
ISBN |
1-282-77417-4
9786612774171 0-470-92504-3 1-59124-664-4 0-470-92503-5 |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Guidelines for Fire Protection in Chemical, Petrochemical, and Hydrocarbon Processing Facilities; CONTENTS; Preface; Acknowledgments; Acronyms; 1 Introduction; 1.1. Scope; 1.2. Who Will Benefit from This Guideline?; 1.2.1. What Is Fire Protection?; 1.2.2. Examples; 1.3. Relation to Other CCPS Guidelines and Resources; 2 Management Overview; 2.1. Management Commitment; 2.2. Integration with Other Management Systems; 2.3. Balancing Protection; 2.4. Cost-Benefit; 3 Fire Protection Strategy; 3.1. Key Factors in a Fire Protection Strategy; 3.1.1. Acceptable Loss; 3.1.2. Cost of Fires
3.1.3. Insurance Coverage3.1.4. Installed Systems versus Emergency Response; 3.1.5. Prescriptive versus Performance-Based Design; 3.2. Developing a Fire Protection Strategy; 3.3. Integration with Other Management Systems; 3.4. Integration with the Lifecycle of a Facility; 3.4.1. Design; 3.4.2. Construction and Commissioning; 3.4.3. Operations; 3.4.4. Decommissioning; 4 Overview of Fire Prevention Elements; 4.1. Audit Program; 4.1.1. The Audit Process; 4.1.2. Qualifications and Staffing; 4.1.3. Frequency of Audits; 4.1.4. Application to Fire Protection; 4.2. Layout and Spacing 4.3. Control of Ignition Sources4.3.1. Electrical Area Classification; 4.3.2. Personal Ignition Sources; 4.3.3. Hot Work; 4.3.4. Static Electricity; 4.4. Employee Training; 4.5. Housekeeping; 4.5.1. Housekeeping Program; 4.5.2. Process Area Housekeeping; 4.5.3. Dust Control; 4.5.4. Inappropriate Storage and Handling; 4.5.5. Housekeeping and Equipment; 4.5.6. Cleaning Materials; 4.6. Incident Investigation; 4.6.1. Incident Investigation Process; 4.6.2. Application to Fire Prevention; 4.7. Inherently Safer Design; 4.8. Plant Maintenance; 4.8.1. Poor Maintenance 4.8.2. Good Maintenance Program Elements4.9. Management of Change; 4.9.1. Personnel Changes; 4.9.2. Process Changes; 4.9.3. Maintenance Turnarounds; 4.10. Material Hazards; 4.10.1. Materials Hazard Evaluation Program; 4.10.2. Material Safety Data Sheets; 4.11. Alarm and Surveillance; 4.11.1. Security; 5 Fire Hazard Analysis; 5.1. Hazardous Chemicals and Processes; 5.2. Recognize What You Want to Understand; 5.3. Identification of Inventories; 5.4. Define Fire Scenarios; 5.5. Calculate Potential Fire Hazard; 5.5.1. Ignition and Combustion; 5.5.2. Heat Transfer 5.5.3. Fire Growth and Heat Release5.5.4. Solid Materials; 5.5.5. Enclosure Effects; 5.6. Flash Fires; 5.7. Fireballs; 5.8. Liquid or Pool Fires; 5.8.1. Uelease Rate; 5.8.2. Pool Size; 5.8.3. Flame Height; 5.8.4. Duration of Burning Pools; 5.8.5. Heat Transfer; 5.8.6. Convective Heat Transfer above the Plume; 5.9. Gas and Jet Fires; 5.9.1. Estimating Discharge Rates; 5.9.2. Jet Flame Size; 5.9.3. Heat Transfer; 5.9.4. Radiative Exposure; 5.10. Solid Fires; 5.11. Fire Impact to Personnel, Structures, and Equipment; 5.11.1. Impact to Personnel; 5.11.2. Impact to Structures 5.11.3. Thermal and Nonthermal Impact on Electrical and Electronic Equipment |
Record Nr. | UNISA-996212662303316 |
New York, NY, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2003 | ||
Materiale a stampa | ||
Lo trovi qui: Univ. di Salerno | ||
|
Guidelines for fire protection in chemical, petrochemical, and hydrocarbon processing facilities [[electronic resource]] |
Pubbl/distr/stampa | New York, NY, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2003 |
Descrizione fisica | 1 online resource (482 p.) |
Disciplina |
660.2804
660/.2804 |
Soggetto topico |
Chemical plants - Fires and fire prevention
Chemicals - Fires and fire prevention |
ISBN |
1-282-77417-4
9786612774171 0-470-92504-3 1-59124-664-4 0-470-92503-5 |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Guidelines for Fire Protection in Chemical, Petrochemical, and Hydrocarbon Processing Facilities; CONTENTS; Preface; Acknowledgments; Acronyms; 1 Introduction; 1.1. Scope; 1.2. Who Will Benefit from This Guideline?; 1.2.1. What Is Fire Protection?; 1.2.2. Examples; 1.3. Relation to Other CCPS Guidelines and Resources; 2 Management Overview; 2.1. Management Commitment; 2.2. Integration with Other Management Systems; 2.3. Balancing Protection; 2.4. Cost-Benefit; 3 Fire Protection Strategy; 3.1. Key Factors in a Fire Protection Strategy; 3.1.1. Acceptable Loss; 3.1.2. Cost of Fires
3.1.3. Insurance Coverage3.1.4. Installed Systems versus Emergency Response; 3.1.5. Prescriptive versus Performance-Based Design; 3.2. Developing a Fire Protection Strategy; 3.3. Integration with Other Management Systems; 3.4. Integration with the Lifecycle of a Facility; 3.4.1. Design; 3.4.2. Construction and Commissioning; 3.4.3. Operations; 3.4.4. Decommissioning; 4 Overview of Fire Prevention Elements; 4.1. Audit Program; 4.1.1. The Audit Process; 4.1.2. Qualifications and Staffing; 4.1.3. Frequency of Audits; 4.1.4. Application to Fire Protection; 4.2. Layout and Spacing 4.3. Control of Ignition Sources4.3.1. Electrical Area Classification; 4.3.2. Personal Ignition Sources; 4.3.3. Hot Work; 4.3.4. Static Electricity; 4.4. Employee Training; 4.5. Housekeeping; 4.5.1. Housekeeping Program; 4.5.2. Process Area Housekeeping; 4.5.3. Dust Control; 4.5.4. Inappropriate Storage and Handling; 4.5.5. Housekeeping and Equipment; 4.5.6. Cleaning Materials; 4.6. Incident Investigation; 4.6.1. Incident Investigation Process; 4.6.2. Application to Fire Prevention; 4.7. Inherently Safer Design; 4.8. Plant Maintenance; 4.8.1. Poor Maintenance 4.8.2. Good Maintenance Program Elements4.9. Management of Change; 4.9.1. Personnel Changes; 4.9.2. Process Changes; 4.9.3. Maintenance Turnarounds; 4.10. Material Hazards; 4.10.1. Materials Hazard Evaluation Program; 4.10.2. Material Safety Data Sheets; 4.11. Alarm and Surveillance; 4.11.1. Security; 5 Fire Hazard Analysis; 5.1. Hazardous Chemicals and Processes; 5.2. Recognize What You Want to Understand; 5.3. Identification of Inventories; 5.4. Define Fire Scenarios; 5.5. Calculate Potential Fire Hazard; 5.5.1. Ignition and Combustion; 5.5.2. Heat Transfer 5.5.3. Fire Growth and Heat Release5.5.4. Solid Materials; 5.5.5. Enclosure Effects; 5.6. Flash Fires; 5.7. Fireballs; 5.8. Liquid or Pool Fires; 5.8.1. Uelease Rate; 5.8.2. Pool Size; 5.8.3. Flame Height; 5.8.4. Duration of Burning Pools; 5.8.5. Heat Transfer; 5.8.6. Convective Heat Transfer above the Plume; 5.9. Gas and Jet Fires; 5.9.1. Estimating Discharge Rates; 5.9.2. Jet Flame Size; 5.9.3. Heat Transfer; 5.9.4. Radiative Exposure; 5.10. Solid Fires; 5.11. Fire Impact to Personnel, Structures, and Equipment; 5.11.1. Impact to Personnel; 5.11.2. Impact to Structures 5.11.3. Thermal and Nonthermal Impact on Electrical and Electronic Equipment |
Record Nr. | UNINA-9910830023703321 |
New York, NY, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2003 | ||
Materiale a stampa | ||
Lo trovi qui: Univ. Federico II | ||
|
Guidelines for fire protection in chemical, petrochemical, and hydrocarbon processing facilities |
Pubbl/distr/stampa | New York, NY, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2003 |
Descrizione fisica | 1 online resource (482 p.) |
Disciplina |
660.2804
660/.2804 |
Soggetto topico |
Chemical plants - Fires and fire prevention
Chemicals - Fires and fire prevention |
ISBN |
1-282-77417-4
9786612774171 0-470-92504-3 1-59124-664-4 0-470-92503-5 |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Guidelines for Fire Protection in Chemical, Petrochemical, and Hydrocarbon Processing Facilities; CONTENTS; Preface; Acknowledgments; Acronyms; 1 Introduction; 1.1. Scope; 1.2. Who Will Benefit from This Guideline?; 1.2.1. What Is Fire Protection?; 1.2.2. Examples; 1.3. Relation to Other CCPS Guidelines and Resources; 2 Management Overview; 2.1. Management Commitment; 2.2. Integration with Other Management Systems; 2.3. Balancing Protection; 2.4. Cost-Benefit; 3 Fire Protection Strategy; 3.1. Key Factors in a Fire Protection Strategy; 3.1.1. Acceptable Loss; 3.1.2. Cost of Fires
3.1.3. Insurance Coverage3.1.4. Installed Systems versus Emergency Response; 3.1.5. Prescriptive versus Performance-Based Design; 3.2. Developing a Fire Protection Strategy; 3.3. Integration with Other Management Systems; 3.4. Integration with the Lifecycle of a Facility; 3.4.1. Design; 3.4.2. Construction and Commissioning; 3.4.3. Operations; 3.4.4. Decommissioning; 4 Overview of Fire Prevention Elements; 4.1. Audit Program; 4.1.1. The Audit Process; 4.1.2. Qualifications and Staffing; 4.1.3. Frequency of Audits; 4.1.4. Application to Fire Protection; 4.2. Layout and Spacing 4.3. Control of Ignition Sources4.3.1. Electrical Area Classification; 4.3.2. Personal Ignition Sources; 4.3.3. Hot Work; 4.3.4. Static Electricity; 4.4. Employee Training; 4.5. Housekeeping; 4.5.1. Housekeeping Program; 4.5.2. Process Area Housekeeping; 4.5.3. Dust Control; 4.5.4. Inappropriate Storage and Handling; 4.5.5. Housekeeping and Equipment; 4.5.6. Cleaning Materials; 4.6. Incident Investigation; 4.6.1. Incident Investigation Process; 4.6.2. Application to Fire Prevention; 4.7. Inherently Safer Design; 4.8. Plant Maintenance; 4.8.1. Poor Maintenance 4.8.2. Good Maintenance Program Elements4.9. Management of Change; 4.9.1. Personnel Changes; 4.9.2. Process Changes; 4.9.3. Maintenance Turnarounds; 4.10. Material Hazards; 4.10.1. Materials Hazard Evaluation Program; 4.10.2. Material Safety Data Sheets; 4.11. Alarm and Surveillance; 4.11.1. Security; 5 Fire Hazard Analysis; 5.1. Hazardous Chemicals and Processes; 5.2. Recognize What You Want to Understand; 5.3. Identification of Inventories; 5.4. Define Fire Scenarios; 5.5. Calculate Potential Fire Hazard; 5.5.1. Ignition and Combustion; 5.5.2. Heat Transfer 5.5.3. Fire Growth and Heat Release5.5.4. Solid Materials; 5.5.5. Enclosure Effects; 5.6. Flash Fires; 5.7. Fireballs; 5.8. Liquid or Pool Fires; 5.8.1. Uelease Rate; 5.8.2. Pool Size; 5.8.3. Flame Height; 5.8.4. Duration of Burning Pools; 5.8.5. Heat Transfer; 5.8.6. Convective Heat Transfer above the Plume; 5.9. Gas and Jet Fires; 5.9.1. Estimating Discharge Rates; 5.9.2. Jet Flame Size; 5.9.3. Heat Transfer; 5.9.4. Radiative Exposure; 5.10. Solid Fires; 5.11. Fire Impact to Personnel, Structures, and Equipment; 5.11.1. Impact to Personnel; 5.11.2. Impact to Structures 5.11.3. Thermal and Nonthermal Impact on Electrical and Electronic Equipment |
Record Nr. | UNINA-9910876775003321 |
New York, NY, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2003 | ||
Materiale a stampa | ||
Lo trovi qui: Univ. Federico II | ||
|
Guidelines for vapor cloud explosion, pressure vessel burst, BLEVE, and flash fire hazards |
Edizione | [2nd ed.] |
Pubbl/distr/stampa | Hoboken, New Jersey : , : Wiley, , 2010 |
Descrizione fisica | 1 online resource (458 p.) |
Disciplina |
660.2804
660/.2804 |
Collana | CCPS concept book Guidelines for vapor cloud explosion, pressure vessel burst, BLEVE, and flash fire hazards. |
Soggetto topico |
Chemical plants - Fires and fire prevention
Chemical plants - Safety measures Pressure vessels - Safety measures Chemicals - Fires and fire prevention Explosions - Prevention |
Soggetto genere / forma | Electronic books. |
ISBN |
1-118-20987-7
1-283-37163-4 9786613371638 0-470-64043-X 1-61583-627-6 0-470-64044-8 |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Guidelines for Vapor Cloud Explosion, Pressure Vessel Burst, BLEVE, and Flash Fire Hazards; CONTENTS; List of Tables; List of Figures; Glossary; Acknowledgements; 1. INTRODUCTION; 2. MANAGEMENT OVERVIEW; 2.1. Flash Fires; 2.2. Vapor Cloud Explosions; 2.3. Pressure Vessel Bursts; 2.4. BLEVEs; 2.5. Prediction methodologies; 3. CASE HISTORIES; 3.1. Historical experience; 3.2. Flash fires; 3.2.1. Donnellson, Iowa, USA: Propane Fire; 3.2.2. Lynchburg, Virginia, USA: Propane Fire; 3.2.3. Quantum Chemicals, Morris, Illinois, USA: Olefins Unit Flash Fire; 3.3. Vapor Cloud Explosions
3.3.1. Flixborough, UK: Vapor Cloud Explosion in Chemical Plant3.3.2. Port Hudson, Missouri, USA: Vapor Cloud Explosion after Propane Pipeline Failure; 3.3.3. Jackass Flats, Nevada, USA: Hydrogen-Air Explosion during Experiment; 3.3.4. Ufa, West-Siberia, USSR: Pipeline Rupture Resulting In a VCE; 3.3.5. Phillips, Pasadena, Texas USA: Propylene HDPE Unit VCE and BLEVEs; 3.3.6. BP, Texas City, Texas USA: Discharge from Atmospheric Vent Resulting in a VCE; 3.4. Pressure Vessel Burst; 3.4.1. Kaiser Aluminum, Gramercy, Louisiana USA: Alumina Process Pressure Vessel Burst 3.4.2. Union Carbide Seadrift, Texas USA: Ethylene Oxide Distillation Column Pressure Vessel Burst3.4.3. Dana Corporation, Paris, Tennessee USA: Boiler Pressure Vessel Burst; 3.5. BLEVE; 3.5.1. Procter and Gamble, Worms, Germany: Liquid CO2 Storage Vessel Explosion; 3.5.2. San Juan Ixhuatepec, Mexico City, Mexico: Series of BLEVEs at LPG Storage Facility; 3.5.3. San Carlos de la Rapita, Spain: Propylene Tank Truck Failure; 3.5.4. Crescent City, Illinois, USA: LPG Rail Car Derailment; 3.5.5. Kingman, Arizona USA: LPG Railroad Tank Car BLEVE; 4. BASIC CONCEPTS 4.1. Atmospheric Vapor Cloud Dispersion4.2. Ignition; 4.3. Thermal Radiation; 4.3.1. Point-Source Model; 4.3.2. Solid-Flame Model; 4.4. Explosions - VCE; 4.4.1. Deflagration; 4.4.2. Detonation; 4.5. Blast Effects; 4.5.1. Manifestation; 4.5.2. Blast Loading; 4.5.3. Ground Reflection; 4.5.4. Blast Scaling; 5. FLASH FIRES; 5.1. Overview of Experimental Research; 5.1.1. China Lake and Frenchmen Flats cryogenic liquid tests; 5.1.2. Maplin Sands Tests; 5.1.3. Musselbanks Propane Tests; 5.1.4. HSE LPG Tests of Flash Fires and Jet Fires; 5.2. Flash-Fire Radiation Models; 5.3. Sample Calculations 6. VAPOR CLOUD EXPLOSIONS6.1. Introduction; 6.1.1. Organization of Chapter; 6.1.2. VCE Phenomena; 6.1.3. Definition of VCE; 6.1.4. Confinement and Congestion; 6.2. Vapor Cloud Deflagration Theory and Research; 6.2.1. Laminar Burning Velocity and Flame Speed; 6.2.2. Mechanisms of Flame Acceleration; 6.2.3. Effect of Fuel Reactivity; 6.2.4. Effect of Confinement; 6.2.5. Effect of Congestion; 6.2.6. Effects of Other Factors; 6.2.7. University of Leeds Correlation; 6.2.8. TOO GAME Correlation; 6.2.9. Shell CAM Correlation; 6.3. Vapor Cloud Detonation Theory and Research 6.3.1. Direct Initiation of Vapor Cloud Detonations |
Record Nr. | UNINA-9910139403303321 |
Hoboken, New Jersey : , : Wiley, , 2010 | ||
Materiale a stampa | ||
Lo trovi qui: Univ. Federico II | ||
|
Guidelines for vapor cloud explosion, pressure vessel burst, BLEVE, and flash fire hazards |
Edizione | [2nd ed.] |
Pubbl/distr/stampa | Hoboken, New Jersey : , : Wiley, , 2010 |
Descrizione fisica | 1 online resource (458 p.) |
Disciplina |
660.2804
660/.2804 |
Collana | CCPS concept book Guidelines for vapor cloud explosion, pressure vessel burst, BLEVE, and flash fire hazards. |
Soggetto topico |
Chemical plants - Fires and fire prevention
Chemical plants - Safety measures Pressure vessels - Safety measures Chemicals - Fires and fire prevention Explosions - Prevention |
ISBN |
1-118-20987-7
1-283-37163-4 9786613371638 0-470-64043-X 1-61583-627-6 0-470-64044-8 |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Guidelines for Vapor Cloud Explosion, Pressure Vessel Burst, BLEVE, and Flash Fire Hazards; CONTENTS; List of Tables; List of Figures; Glossary; Acknowledgements; 1. INTRODUCTION; 2. MANAGEMENT OVERVIEW; 2.1. Flash Fires; 2.2. Vapor Cloud Explosions; 2.3. Pressure Vessel Bursts; 2.4. BLEVEs; 2.5. Prediction methodologies; 3. CASE HISTORIES; 3.1. Historical experience; 3.2. Flash fires; 3.2.1. Donnellson, Iowa, USA: Propane Fire; 3.2.2. Lynchburg, Virginia, USA: Propane Fire; 3.2.3. Quantum Chemicals, Morris, Illinois, USA: Olefins Unit Flash Fire; 3.3. Vapor Cloud Explosions
3.3.1. Flixborough, UK: Vapor Cloud Explosion in Chemical Plant3.3.2. Port Hudson, Missouri, USA: Vapor Cloud Explosion after Propane Pipeline Failure; 3.3.3. Jackass Flats, Nevada, USA: Hydrogen-Air Explosion during Experiment; 3.3.4. Ufa, West-Siberia, USSR: Pipeline Rupture Resulting In a VCE; 3.3.5. Phillips, Pasadena, Texas USA: Propylene HDPE Unit VCE and BLEVEs; 3.3.6. BP, Texas City, Texas USA: Discharge from Atmospheric Vent Resulting in a VCE; 3.4. Pressure Vessel Burst; 3.4.1. Kaiser Aluminum, Gramercy, Louisiana USA: Alumina Process Pressure Vessel Burst 3.4.2. Union Carbide Seadrift, Texas USA: Ethylene Oxide Distillation Column Pressure Vessel Burst3.4.3. Dana Corporation, Paris, Tennessee USA: Boiler Pressure Vessel Burst; 3.5. BLEVE; 3.5.1. Procter and Gamble, Worms, Germany: Liquid CO2 Storage Vessel Explosion; 3.5.2. San Juan Ixhuatepec, Mexico City, Mexico: Series of BLEVEs at LPG Storage Facility; 3.5.3. San Carlos de la Rapita, Spain: Propylene Tank Truck Failure; 3.5.4. Crescent City, Illinois, USA: LPG Rail Car Derailment; 3.5.5. Kingman, Arizona USA: LPG Railroad Tank Car BLEVE; 4. BASIC CONCEPTS 4.1. Atmospheric Vapor Cloud Dispersion4.2. Ignition; 4.3. Thermal Radiation; 4.3.1. Point-Source Model; 4.3.2. Solid-Flame Model; 4.4. Explosions - VCE; 4.4.1. Deflagration; 4.4.2. Detonation; 4.5. Blast Effects; 4.5.1. Manifestation; 4.5.2. Blast Loading; 4.5.3. Ground Reflection; 4.5.4. Blast Scaling; 5. FLASH FIRES; 5.1. Overview of Experimental Research; 5.1.1. China Lake and Frenchmen Flats cryogenic liquid tests; 5.1.2. Maplin Sands Tests; 5.1.3. Musselbanks Propane Tests; 5.1.4. HSE LPG Tests of Flash Fires and Jet Fires; 5.2. Flash-Fire Radiation Models; 5.3. Sample Calculations 6. VAPOR CLOUD EXPLOSIONS6.1. Introduction; 6.1.1. Organization of Chapter; 6.1.2. VCE Phenomena; 6.1.3. Definition of VCE; 6.1.4. Confinement and Congestion; 6.2. Vapor Cloud Deflagration Theory and Research; 6.2.1. Laminar Burning Velocity and Flame Speed; 6.2.2. Mechanisms of Flame Acceleration; 6.2.3. Effect of Fuel Reactivity; 6.2.4. Effect of Confinement; 6.2.5. Effect of Congestion; 6.2.6. Effects of Other Factors; 6.2.7. University of Leeds Correlation; 6.2.8. TOO GAME Correlation; 6.2.9. Shell CAM Correlation; 6.3. Vapor Cloud Detonation Theory and Research 6.3.1. Direct Initiation of Vapor Cloud Detonations |
Record Nr. | UNINA-9910830788803321 |
Hoboken, New Jersey : , : Wiley, , 2010 | ||
Materiale a stampa | ||
Lo trovi qui: Univ. Federico II | ||
|
LNG risk based safety [[electronic resource] ] : modeling and consequence analysis / / John L Woodward and Robin Pitblado |
Autore | Woodward John Lowell |
Pubbl/distr/stampa | Hoboken, N.J., : Wiley, c2010 |
Descrizione fisica | 1 online resource (392 p.) |
Disciplina |
665.7/730289
665.7730289 |
Altri autori (Persone) | PitbladoRobin |
Soggetto topico |
Liquefied natural gas - Safety measures
Flammable gases - Accidents - Risk assessment Flammable liquids - Accidents - Risk assessment Chemicals - Fires and fire prevention Chemical plants - Accidents - Simulation methods |
Soggetto genere / forma | Electronic books. |
ISBN |
1-282-54984-7
9786612549847 0-470-59023-8 0-470-59022-X |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
LNG RISK BASED SAFETY; CONTENTS; Preface; 1 LNG Properties and Overview of Hazards; 1.1 LNG Properties; 1.2 Hazards of LNG with Respect to Public Risk; 1.2.1 Flash Fire, Pool Fire, or Jet Fire; 1.2.2 Outdoor Vapor Cloud Explosions; 1.2.3 Enclosed Vapor Cloud Explosions; 1.2.4 Asphyxiation; 1.2.5 Freeze Burns; 1.2.6 RPT Explosions; 1.2.7 Roll Over; 1.3 Risk Analysis Requires Adequate Modeling; 1.4 Flammability; 1.5 Regulations in Siting Onshore LNG Import Terminals; 1.5.1 U.S. Marine LNG Risk and Security Regulation; 1.5.2 U.S. Land-Based LNG Risk and Security Regulation
1.5.3 European and International Regulations1.6 Regulation for Siting Offshore LNG Import Terminals; 1.7 Controversial Claims of LNG Opponents; 2 LNG Incidents and Marine History; 2.1 LNG Ship Design History; 2.1.1 Initial Design Attempts; 2.1.2 Tank Materials; 2.1.3 Insulation Materials; 2.1.4 Tank Design; 2.2 Designs and Issues-First Commercial LNG Ships; 2.2.1 Membrane Technology; 2.2.2 Gaztransport Solution; 2.2.3 Spheres; 2.2.4 LNG Carriers for the Asian Trade; 2.2.5 Current State of LNG Tankers; 2.3 LNG Trade History; 2.3.1 European Trade; 2.3.2 Asian Trade; 2.3.3 Temporary Setbacks 2.3.4 Revival of LNG with Worldwide Supply-Demand Pinch of Petroleum2.3.5 Supply History; 2.3.6 Some Economic Factors; 2.4 LNG Accident History; 2.5 Summary of LNG History and Relevant Technical Developments; 3 Current LNG Carriers; 3.1 Design Requirements; 3.2 Membrane Tanks; 3.2.1 Tank Design and Insulation; 3.2.2 Dimensions and Capacity; 3.2.3 Tank Materials and Insulation; 3.2.4 Pressure and Vacuum Relief; 3.2.5 Design Issues; 3.3 Moss Spheres; 3.3.1 Typical Dimensions and Capacity; 3.3.2 Insulation and Tank Materials; 3.3.3 Pressure and Vacuum Relief; 3.3.4 Design Issues 4 Risk Analysis and Risk Reduction4.1 Background; 4.2 Risk Analysis Process; 4.2.1 Hazard Identification; 4.3 Frequency: Data Sources and Analysis; 4.3.1 Generic Data Approach; 4.4 Frequency: Predictive Methods; 4.4.1 FTA; 4.4.2 Event Tree Analysis; 4.5 Consequence Modeling; 4.6 Ignition Probability; 4.7 Risk Results; 4.7.1 Risk Presentation; 4.7.2 Risk Decision Making; 4.8 Special Issues-Terrorism; 4.9 Risk Reduction and Mitigation Measures for LNG; 5 LNG Discharge on Water; 5.1 Type 1-Above Water Breaches at Sea; 5.1.1 Ship-to-Ship Collisions; 5.1.2 Weapons Attack 5.2 Type 2-At Waterline Breaches at Sea5.2.1 Grounding or Collision; 5.2.2 Explosive-Laden Boat Attack; 5.3 Type 3-Below Waterline Breaches at Sea; 5.4 Discharges from Ship's Pipework; 5.5 Cascading Failures at Sea; 5.5.1 Sloshing Forces; 5.5.2 Explosion in Hull Chambers; 5.5.3 RPT in Hull Chambers; 5.5.4 Cryogenic Temperature Stresses on Decks and Hull; 5.5.5 Cascading Events Caused by Fire; 5.6 Initial Discharge Rate; 5.7 Time-Dependent Discharge (Blowdown); 5.7.1 Blowdown for Type 2 Breach (at Waterline); 5.7.2 Blowdown for Type 1 Breach (above Waterline) 5.7.3 Blowdown of Type 3 Breach (Underwater Level) |
Record Nr. | UNINA-9910140606103321 |
Woodward John Lowell | ||
Hoboken, N.J., : Wiley, c2010 | ||
Materiale a stampa | ||
Lo trovi qui: Univ. Federico II | ||
|
LNG risk based safety [[electronic resource] ] : modeling and consequence analysis / / John L Woodward and Robin Pitblado |
Autore | Woodward John Lowell |
Pubbl/distr/stampa | Hoboken, N.J., : Wiley, c2010 |
Descrizione fisica | 1 online resource (392 p.) |
Disciplina |
665.7/730289
665.7730289 |
Altri autori (Persone) | PitbladoRobin |
Soggetto topico |
Liquefied natural gas - Safety measures
Flammable gases - Accidents - Risk assessment Flammable liquids - Accidents - Risk assessment Chemicals - Fires and fire prevention Chemical plants - Accidents - Simulation methods |
ISBN |
1-282-54984-7
9786612549847 0-470-59023-8 0-470-59022-X |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
LNG RISK BASED SAFETY; CONTENTS; Preface; 1 LNG Properties and Overview of Hazards; 1.1 LNG Properties; 1.2 Hazards of LNG with Respect to Public Risk; 1.2.1 Flash Fire, Pool Fire, or Jet Fire; 1.2.2 Outdoor Vapor Cloud Explosions; 1.2.3 Enclosed Vapor Cloud Explosions; 1.2.4 Asphyxiation; 1.2.5 Freeze Burns; 1.2.6 RPT Explosions; 1.2.7 Roll Over; 1.3 Risk Analysis Requires Adequate Modeling; 1.4 Flammability; 1.5 Regulations in Siting Onshore LNG Import Terminals; 1.5.1 U.S. Marine LNG Risk and Security Regulation; 1.5.2 U.S. Land-Based LNG Risk and Security Regulation
1.5.3 European and International Regulations1.6 Regulation for Siting Offshore LNG Import Terminals; 1.7 Controversial Claims of LNG Opponents; 2 LNG Incidents and Marine History; 2.1 LNG Ship Design History; 2.1.1 Initial Design Attempts; 2.1.2 Tank Materials; 2.1.3 Insulation Materials; 2.1.4 Tank Design; 2.2 Designs and Issues-First Commercial LNG Ships; 2.2.1 Membrane Technology; 2.2.2 Gaztransport Solution; 2.2.3 Spheres; 2.2.4 LNG Carriers for the Asian Trade; 2.2.5 Current State of LNG Tankers; 2.3 LNG Trade History; 2.3.1 European Trade; 2.3.2 Asian Trade; 2.3.3 Temporary Setbacks 2.3.4 Revival of LNG with Worldwide Supply-Demand Pinch of Petroleum2.3.5 Supply History; 2.3.6 Some Economic Factors; 2.4 LNG Accident History; 2.5 Summary of LNG History and Relevant Technical Developments; 3 Current LNG Carriers; 3.1 Design Requirements; 3.2 Membrane Tanks; 3.2.1 Tank Design and Insulation; 3.2.2 Dimensions and Capacity; 3.2.3 Tank Materials and Insulation; 3.2.4 Pressure and Vacuum Relief; 3.2.5 Design Issues; 3.3 Moss Spheres; 3.3.1 Typical Dimensions and Capacity; 3.3.2 Insulation and Tank Materials; 3.3.3 Pressure and Vacuum Relief; 3.3.4 Design Issues 4 Risk Analysis and Risk Reduction4.1 Background; 4.2 Risk Analysis Process; 4.2.1 Hazard Identification; 4.3 Frequency: Data Sources and Analysis; 4.3.1 Generic Data Approach; 4.4 Frequency: Predictive Methods; 4.4.1 FTA; 4.4.2 Event Tree Analysis; 4.5 Consequence Modeling; 4.6 Ignition Probability; 4.7 Risk Results; 4.7.1 Risk Presentation; 4.7.2 Risk Decision Making; 4.8 Special Issues-Terrorism; 4.9 Risk Reduction and Mitigation Measures for LNG; 5 LNG Discharge on Water; 5.1 Type 1-Above Water Breaches at Sea; 5.1.1 Ship-to-Ship Collisions; 5.1.2 Weapons Attack 5.2 Type 2-At Waterline Breaches at Sea5.2.1 Grounding or Collision; 5.2.2 Explosive-Laden Boat Attack; 5.3 Type 3-Below Waterline Breaches at Sea; 5.4 Discharges from Ship's Pipework; 5.5 Cascading Failures at Sea; 5.5.1 Sloshing Forces; 5.5.2 Explosion in Hull Chambers; 5.5.3 RPT in Hull Chambers; 5.5.4 Cryogenic Temperature Stresses on Decks and Hull; 5.5.5 Cascading Events Caused by Fire; 5.6 Initial Discharge Rate; 5.7 Time-Dependent Discharge (Blowdown); 5.7.1 Blowdown for Type 2 Breach (at Waterline); 5.7.2 Blowdown for Type 1 Breach (above Waterline) 5.7.3 Blowdown of Type 3 Breach (Underwater Level) |
Record Nr. | UNINA-9910830217303321 |
Woodward John Lowell | ||
Hoboken, N.J., : Wiley, c2010 | ||
Materiale a stampa | ||
Lo trovi qui: Univ. Federico II | ||
|
LNG risk based safety : modeling and consequence analysis / / John L Woodward and Robin Pitblado |
Autore | Woodward John Lowell |
Pubbl/distr/stampa | Hoboken, N.J., : Wiley, c2010 |
Descrizione fisica | 1 online resource (392 p.) |
Disciplina | 665.7/730289 |
Altri autori (Persone) | PitbladoRobin |
Soggetto topico |
Liquefied natural gas - Safety measures
Flammable gases - Accidents - Risk assessment Flammable liquids - Accidents - Risk assessment Chemicals - Fires and fire prevention Chemical plants - Accidents - Simulation methods |
ISBN |
1-282-54984-7
9786612549847 0-470-59023-8 0-470-59022-X |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
LNG RISK BASED SAFETY; CONTENTS; Preface; 1 LNG Properties and Overview of Hazards; 1.1 LNG Properties; 1.2 Hazards of LNG with Respect to Public Risk; 1.2.1 Flash Fire, Pool Fire, or Jet Fire; 1.2.2 Outdoor Vapor Cloud Explosions; 1.2.3 Enclosed Vapor Cloud Explosions; 1.2.4 Asphyxiation; 1.2.5 Freeze Burns; 1.2.6 RPT Explosions; 1.2.7 Roll Over; 1.3 Risk Analysis Requires Adequate Modeling; 1.4 Flammability; 1.5 Regulations in Siting Onshore LNG Import Terminals; 1.5.1 U.S. Marine LNG Risk and Security Regulation; 1.5.2 U.S. Land-Based LNG Risk and Security Regulation
1.5.3 European and International Regulations1.6 Regulation for Siting Offshore LNG Import Terminals; 1.7 Controversial Claims of LNG Opponents; 2 LNG Incidents and Marine History; 2.1 LNG Ship Design History; 2.1.1 Initial Design Attempts; 2.1.2 Tank Materials; 2.1.3 Insulation Materials; 2.1.4 Tank Design; 2.2 Designs and Issues-First Commercial LNG Ships; 2.2.1 Membrane Technology; 2.2.2 Gaztransport Solution; 2.2.3 Spheres; 2.2.4 LNG Carriers for the Asian Trade; 2.2.5 Current State of LNG Tankers; 2.3 LNG Trade History; 2.3.1 European Trade; 2.3.2 Asian Trade; 2.3.3 Temporary Setbacks 2.3.4 Revival of LNG with Worldwide Supply-Demand Pinch of Petroleum2.3.5 Supply History; 2.3.6 Some Economic Factors; 2.4 LNG Accident History; 2.5 Summary of LNG History and Relevant Technical Developments; 3 Current LNG Carriers; 3.1 Design Requirements; 3.2 Membrane Tanks; 3.2.1 Tank Design and Insulation; 3.2.2 Dimensions and Capacity; 3.2.3 Tank Materials and Insulation; 3.2.4 Pressure and Vacuum Relief; 3.2.5 Design Issues; 3.3 Moss Spheres; 3.3.1 Typical Dimensions and Capacity; 3.3.2 Insulation and Tank Materials; 3.3.3 Pressure and Vacuum Relief; 3.3.4 Design Issues 4 Risk Analysis and Risk Reduction4.1 Background; 4.2 Risk Analysis Process; 4.2.1 Hazard Identification; 4.3 Frequency: Data Sources and Analysis; 4.3.1 Generic Data Approach; 4.4 Frequency: Predictive Methods; 4.4.1 FTA; 4.4.2 Event Tree Analysis; 4.5 Consequence Modeling; 4.6 Ignition Probability; 4.7 Risk Results; 4.7.1 Risk Presentation; 4.7.2 Risk Decision Making; 4.8 Special Issues-Terrorism; 4.9 Risk Reduction and Mitigation Measures for LNG; 5 LNG Discharge on Water; 5.1 Type 1-Above Water Breaches at Sea; 5.1.1 Ship-to-Ship Collisions; 5.1.2 Weapons Attack 5.2 Type 2-At Waterline Breaches at Sea5.2.1 Grounding or Collision; 5.2.2 Explosive-Laden Boat Attack; 5.3 Type 3-Below Waterline Breaches at Sea; 5.4 Discharges from Ship's Pipework; 5.5 Cascading Failures at Sea; 5.5.1 Sloshing Forces; 5.5.2 Explosion in Hull Chambers; 5.5.3 RPT in Hull Chambers; 5.5.4 Cryogenic Temperature Stresses on Decks and Hull; 5.5.5 Cascading Events Caused by Fire; 5.6 Initial Discharge Rate; 5.7 Time-Dependent Discharge (Blowdown); 5.7.1 Blowdown for Type 2 Breach (at Waterline); 5.7.2 Blowdown for Type 1 Breach (above Waterline) 5.7.3 Blowdown of Type 3 Breach (Underwater Level) |
Record Nr. | UNINA-9910876948703321 |
Woodward John Lowell | ||
Hoboken, N.J., : Wiley, c2010 | ||
Materiale a stampa | ||
Lo trovi qui: Univ. Federico II | ||
|