Evaluating process safety in the chemical industry [[electronic resource] ] : a user's guide to quantitative risk analysis / / J.S. Arendt, D.K. Lorenzo |
Autore | Arendt J. S (J. Steven), <1952-> |
Pubbl/distr/stampa | Arlington, Va., : American Chemistry Council |
Descrizione fisica | 1 online resource (108 p.) |
Disciplina |
660.2804
660/.2804 |
Altri autori (Persone) | LorenzoD. K <1955-> (Donald K.) |
Collana | CCPS concept book |
Soggetto topico | Chemical plants - Risk assessment |
Soggetto genere / forma | Electronic books. |
ISBN |
1-282-78334-3
9786612783340 0-470-93546-4 1-59124-574-5 0-470-93545-6 |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Evaluating Process Safety in the Chemical Industry: A User's Guide to Quantitative Risk Analysis; CONTENTS; List of Figures; List of Tables; Preface; Acknowledgments; Executive Summary; Advice for the Reader; Acronyms; Glossary; 1 INTRODUCTION; 1.1. BACKGROUND; 1.2. THE PROCESS OF RISK ANALYSIS; 1.3. DEFINITION OF QRA; 1.4. MISCONCEPTIONS ABOUT QRA; 2 DECIDING WHETHER TO USE QRA; 2.1. SOME REASONS FOR CONSIDERING QRA; 2.2. TYPES OF INFORMATION AVAILABLE FROM RISK STUDIES; 2.3. CRITERIA FOR ELECTING TO USE QRA; 3 MANAGEMENT USE OF QRA; 3.1. CHARTERING THE ANALYSIS; 3.1.1. Study Objective
3.1.2. Scope3.1.3. Technical Approach; 3.1.4. Resources; 3.2. SELECTING QRATECHNIQUES; 3.2.1. Hazard Identification; 3.2.2. Consequence Analysis; 3.2.3. Frequency Analysis; 3.2.4. Risk Evaluation and Presentation; 3.3. UNDERSTANDING THE ASSUMPTIONS AND LIMITATIONS; 3.3.1. Completeness; 3.3.2. Model Validity; 3.3.3. Accuracy/Uncertainty; 3.3.4. Reproducibility; 3.3.5. Inscrutability; 4 USING QRA RESULTS; 4.1. COMPARATIVE METHODS FOR ESTABLISHING PERSPECTIVE; 4.2. FACTORS INFLUENCING RISK PERCEPTION; 4.2.1. Type of Hazard; 4.2.2. Voluntary versus lnvoluntary; 4.2.3. Societal versus Individual 4.2.4. Public versus Employee4.2.5. High Consequence/Low Frequency versus Low Consequence/High Frequency; 4.2.6. Acute versus Latent Effects; 4.2.7. Familiarity; 4.2.8. Controllability; 4.2.9. Age of Exposed Population; 4.2.10. Distribution of Risk and Benefit; 4.3. COMMUNICATING RISK; 4.3.1. Accept and lnvolve the Public as a Legitimate Partner; 4.3.2. Plan Carefully and Evaluate Your Efforts; 4.3.3. Listen to People's Specific Concerns; 4.3.4. Be Honest, Frank, and Open; 4.3.5. Coordinate and Collaborate with Other Credible Sources; 4.3.6. Meet the Needs of the Media 4.3.7. Speak Clearly and with Compassion4.4. PITFALLS IN USING QRA RESULTS; 5 CONCLUSIONS; References; Suggested Additional Reading |
Record Nr. | UNINA-9910142522603321 |
Arendt J. S (J. Steven), <1952-> | ||
Arlington, Va., : American Chemistry Council | ||
Materiale a stampa | ||
Lo trovi qui: Univ. Federico II | ||
|
Evaluating process safety in the chemical industry [[electronic resource] ] : a user's guide to quantitative risk analysis / / J.S. Arendt, D.K. Lorenzo |
Autore | Arendt J. S (J. Steven), <1952-> |
Pubbl/distr/stampa | Arlington, Va., : American Chemistry Council |
Descrizione fisica | 1 online resource (108 p.) |
Disciplina |
660.2804
660/.2804 |
Altri autori (Persone) | LorenzoD. K <1955-> (Donald K.) |
Collana | CCPS concept book |
Soggetto topico | Chemical plants - Risk assessment |
ISBN |
1-282-78334-3
9786612783340 0-470-93546-4 1-59124-574-5 0-470-93545-6 |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Evaluating Process Safety in the Chemical Industry: A User's Guide to Quantitative Risk Analysis; CONTENTS; List of Figures; List of Tables; Preface; Acknowledgments; Executive Summary; Advice for the Reader; Acronyms; Glossary; 1 INTRODUCTION; 1.1. BACKGROUND; 1.2. THE PROCESS OF RISK ANALYSIS; 1.3. DEFINITION OF QRA; 1.4. MISCONCEPTIONS ABOUT QRA; 2 DECIDING WHETHER TO USE QRA; 2.1. SOME REASONS FOR CONSIDERING QRA; 2.2. TYPES OF INFORMATION AVAILABLE FROM RISK STUDIES; 2.3. CRITERIA FOR ELECTING TO USE QRA; 3 MANAGEMENT USE OF QRA; 3.1. CHARTERING THE ANALYSIS; 3.1.1. Study Objective
3.1.2. Scope3.1.3. Technical Approach; 3.1.4. Resources; 3.2. SELECTING QRATECHNIQUES; 3.2.1. Hazard Identification; 3.2.2. Consequence Analysis; 3.2.3. Frequency Analysis; 3.2.4. Risk Evaluation and Presentation; 3.3. UNDERSTANDING THE ASSUMPTIONS AND LIMITATIONS; 3.3.1. Completeness; 3.3.2. Model Validity; 3.3.3. Accuracy/Uncertainty; 3.3.4. Reproducibility; 3.3.5. Inscrutability; 4 USING QRA RESULTS; 4.1. COMPARATIVE METHODS FOR ESTABLISHING PERSPECTIVE; 4.2. FACTORS INFLUENCING RISK PERCEPTION; 4.2.1. Type of Hazard; 4.2.2. Voluntary versus lnvoluntary; 4.2.3. Societal versus Individual 4.2.4. Public versus Employee4.2.5. High Consequence/Low Frequency versus Low Consequence/High Frequency; 4.2.6. Acute versus Latent Effects; 4.2.7. Familiarity; 4.2.8. Controllability; 4.2.9. Age of Exposed Population; 4.2.10. Distribution of Risk and Benefit; 4.3. COMMUNICATING RISK; 4.3.1. Accept and lnvolve the Public as a Legitimate Partner; 4.3.2. Plan Carefully and Evaluate Your Efforts; 4.3.3. Listen to People's Specific Concerns; 4.3.4. Be Honest, Frank, and Open; 4.3.5. Coordinate and Collaborate with Other Credible Sources; 4.3.6. Meet the Needs of the Media 4.3.7. Speak Clearly and with Compassion4.4. PITFALLS IN USING QRA RESULTS; 5 CONCLUSIONS; References; Suggested Additional Reading |
Record Nr. | UNISA-996199267803316 |
Arendt J. S (J. Steven), <1952-> | ||
Arlington, Va., : American Chemistry Council | ||
Materiale a stampa | ||
Lo trovi qui: Univ. di Salerno | ||
|
Evaluating process safety in the chemical industry [[electronic resource] ] : a user's guide to quantitative risk analysis / / J.S. Arendt, D.K. Lorenzo |
Autore | Arendt J. S (J. Steven), <1952-> |
Pubbl/distr/stampa | Arlington, Va., : American Chemistry Council |
Descrizione fisica | 1 online resource (108 p.) |
Disciplina |
660.2804
660/.2804 |
Altri autori (Persone) | LorenzoD. K <1955-> (Donald K.) |
Collana | CCPS concept book |
Soggetto topico | Chemical plants - Risk assessment |
ISBN |
1-282-78334-3
9786612783340 0-470-93546-4 1-59124-574-5 0-470-93545-6 |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Evaluating Process Safety in the Chemical Industry: A User's Guide to Quantitative Risk Analysis; CONTENTS; List of Figures; List of Tables; Preface; Acknowledgments; Executive Summary; Advice for the Reader; Acronyms; Glossary; 1 INTRODUCTION; 1.1. BACKGROUND; 1.2. THE PROCESS OF RISK ANALYSIS; 1.3. DEFINITION OF QRA; 1.4. MISCONCEPTIONS ABOUT QRA; 2 DECIDING WHETHER TO USE QRA; 2.1. SOME REASONS FOR CONSIDERING QRA; 2.2. TYPES OF INFORMATION AVAILABLE FROM RISK STUDIES; 2.3. CRITERIA FOR ELECTING TO USE QRA; 3 MANAGEMENT USE OF QRA; 3.1. CHARTERING THE ANALYSIS; 3.1.1. Study Objective
3.1.2. Scope3.1.3. Technical Approach; 3.1.4. Resources; 3.2. SELECTING QRATECHNIQUES; 3.2.1. Hazard Identification; 3.2.2. Consequence Analysis; 3.2.3. Frequency Analysis; 3.2.4. Risk Evaluation and Presentation; 3.3. UNDERSTANDING THE ASSUMPTIONS AND LIMITATIONS; 3.3.1. Completeness; 3.3.2. Model Validity; 3.3.3. Accuracy/Uncertainty; 3.3.4. Reproducibility; 3.3.5. Inscrutability; 4 USING QRA RESULTS; 4.1. COMPARATIVE METHODS FOR ESTABLISHING PERSPECTIVE; 4.2. FACTORS INFLUENCING RISK PERCEPTION; 4.2.1. Type of Hazard; 4.2.2. Voluntary versus lnvoluntary; 4.2.3. Societal versus Individual 4.2.4. Public versus Employee4.2.5. High Consequence/Low Frequency versus Low Consequence/High Frequency; 4.2.6. Acute versus Latent Effects; 4.2.7. Familiarity; 4.2.8. Controllability; 4.2.9. Age of Exposed Population; 4.2.10. Distribution of Risk and Benefit; 4.3. COMMUNICATING RISK; 4.3.1. Accept and lnvolve the Public as a Legitimate Partner; 4.3.2. Plan Carefully and Evaluate Your Efforts; 4.3.3. Listen to People's Specific Concerns; 4.3.4. Be Honest, Frank, and Open; 4.3.5. Coordinate and Collaborate with Other Credible Sources; 4.3.6. Meet the Needs of the Media 4.3.7. Speak Clearly and with Compassion4.4. PITFALLS IN USING QRA RESULTS; 5 CONCLUSIONS; References; Suggested Additional Reading |
Record Nr. | UNINA-9910829839203321 |
Arendt J. S (J. Steven), <1952-> | ||
Arlington, Va., : American Chemistry Council | ||
Materiale a stampa | ||
Lo trovi qui: Univ. Federico II | ||
|
Evaluating process safety in the chemical industry : a user's guide to quantitative risk analysis / / J.S. Arendt, D.K. Lorenzo |
Autore | Arendt J. S (J. Steven), <1952-> |
Pubbl/distr/stampa | Arlington, Va., : American Chemistry Council |
Descrizione fisica | 1 online resource (108 p.) |
Disciplina | 660/.2804 |
Altri autori (Persone) | LorenzoD. K <1955-> (Donald K.) |
Collana | CCPS concept book |
Soggetto topico | Chemical plants - Risk assessment |
ISBN |
1-282-78334-3
9786612783340 0-470-93546-4 1-59124-574-5 0-470-93545-6 |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Evaluating Process Safety in the Chemical Industry: A User's Guide to Quantitative Risk Analysis; CONTENTS; List of Figures; List of Tables; Preface; Acknowledgments; Executive Summary; Advice for the Reader; Acronyms; Glossary; 1 INTRODUCTION; 1.1. BACKGROUND; 1.2. THE PROCESS OF RISK ANALYSIS; 1.3. DEFINITION OF QRA; 1.4. MISCONCEPTIONS ABOUT QRA; 2 DECIDING WHETHER TO USE QRA; 2.1. SOME REASONS FOR CONSIDERING QRA; 2.2. TYPES OF INFORMATION AVAILABLE FROM RISK STUDIES; 2.3. CRITERIA FOR ELECTING TO USE QRA; 3 MANAGEMENT USE OF QRA; 3.1. CHARTERING THE ANALYSIS; 3.1.1. Study Objective
3.1.2. Scope3.1.3. Technical Approach; 3.1.4. Resources; 3.2. SELECTING QRATECHNIQUES; 3.2.1. Hazard Identification; 3.2.2. Consequence Analysis; 3.2.3. Frequency Analysis; 3.2.4. Risk Evaluation and Presentation; 3.3. UNDERSTANDING THE ASSUMPTIONS AND LIMITATIONS; 3.3.1. Completeness; 3.3.2. Model Validity; 3.3.3. Accuracy/Uncertainty; 3.3.4. Reproducibility; 3.3.5. Inscrutability; 4 USING QRA RESULTS; 4.1. COMPARATIVE METHODS FOR ESTABLISHING PERSPECTIVE; 4.2. FACTORS INFLUENCING RISK PERCEPTION; 4.2.1. Type of Hazard; 4.2.2. Voluntary versus lnvoluntary; 4.2.3. Societal versus Individual 4.2.4. Public versus Employee4.2.5. High Consequence/Low Frequency versus Low Consequence/High Frequency; 4.2.6. Acute versus Latent Effects; 4.2.7. Familiarity; 4.2.8. Controllability; 4.2.9. Age of Exposed Population; 4.2.10. Distribution of Risk and Benefit; 4.3. COMMUNICATING RISK; 4.3.1. Accept and lnvolve the Public as a Legitimate Partner; 4.3.2. Plan Carefully and Evaluate Your Efforts; 4.3.3. Listen to People's Specific Concerns; 4.3.4. Be Honest, Frank, and Open; 4.3.5. Coordinate and Collaborate with Other Credible Sources; 4.3.6. Meet the Needs of the Media 4.3.7. Speak Clearly and with Compassion4.4. PITFALLS IN USING QRA RESULTS; 5 CONCLUSIONS; References; Suggested Additional Reading |
Record Nr. | UNINA-9910876974003321 |
Arendt J. S (J. Steven), <1952-> | ||
Arlington, Va., : American Chemistry Council | ||
Materiale a stampa | ||
Lo trovi qui: Univ. Federico II | ||
|
Fires in silos [[electronic resource] ] : hazards, prevention, and fire fighting / / edited by Ulrich Krause |
Pubbl/distr/stampa | Weinheim, : Wiley-VCH, c2009 |
Descrizione fisica | 1 online resource (158 p.) |
Disciplina | 363.379 |
Altri autori (Persone) | KrauseUlrich, Dr. |
Soggetto topico |
Silos - Fires and fire prevention
Fire extinction Chemical plants - Risk assessment |
Soggetto genere / forma | Electronic books. |
ISBN |
1-282-02177-X
9786612021770 3-527-62382-5 3-527-62381-7 |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Fires in Silos: Hazards, Prevention, and Fire Fighting; Contents; Preface; 1 Introduction; 1.1 Problem Description; 1.2 Influence of Material Properties on Fire; 1.2.1 Particle Size Distribution, Particle Shape and Internal Surface Area; 1.2.2 Bulk Porosity and Bulk Density; 1.2.3 Porosity of Individual Particles; 1.2.4 Particle Density; 1.2.5 Humidity; 1.3 Chemical Properties of Bulk Goods; 1.3.1 Chemical Structure; 1.3.2 Heat of Formation and Calorific Value; References; 2 Ignition Sources; 2.1 Introduction; 2.2 External Ignition Sources; 2.2.1 Hot Solids, Liquids or Gases
2.2.1.1 Ignition of Gases by Hot Solids2.2.1.2 Ignition of Dust Clouds by Hot Solids; 2.2.1.3 Ignition of Solids by Hot Solids; 2.2.2 Flames or Remote Burning Objects; 2.2.3 Electric Current, Static Electricity, Electromagnetic Waves and Particulate Radiation; 2.2.3.1 Electric Current; 2.2.3.2 Static Electricity; 2.3 Self-Heating; 2.4 Physical Characteristics of Self-Ignition Processes and Smoldering Fire Propagation; References; 3 Fire Risk Assessment; 3.1 Introduction; 3.2 Experimental Techniques; 3.2.1 Ignition Sensitivity; 3.2.1.1 Minimum Ignition Temperature (MIT) 3.2.1.2 Minimum Explosible Concentration (Lower Explosion Limit (MEC/LEL))3.2.1.3 Minimum Ignition Energy (MIE); 3.2.2 Explosion Severity; 3.2.2.1 Explosion Pressure (Pmax ); 3.2.2.2 Maximum Rate of Pressure Rise (dp/dt); 3.2.2.3 Kmax Specific Constant; 3.2.3 Thermal Susceptibility; 3.2.3.1 Maciejasz Index (MI); 3.2.3.2 Temperature of Emission of Flammable Volatiles (TEV); 3.2.3.3 Thermogravimetry (TG) Test; 3.2.3.4 Differential Scanning Calorimetry (DSC); 3.2.3.5 Susceptibility Evaluation: Activation Energy (Ea) 3.2.3.6 Susceptibility Evaluation: Characteristic Oxidation Temperature (Tcharac )3.2.4 Thermal Stability; 3.2.4.1 Self-Ignition Temperature (SIT); 3.2.5 Classication of Solid Dangerous Goods; 3.2.5.1 Solids which are Readily Combustible; 3.2.5.2 Substances Liable to Spontaneous Combustion; 3.2.5.3 Substances which, in Contact with Water, Release Flammable Gases; 3.2.5.4 Oxidizing Substances; 3.2.6 Other Tests; 3.2.6.1 Flammability; 3.2.6.2 Burning Behavior; 3.2.6.3 Grewer Oven; 3.2.6.4 Impact Sensitivity; 3.2.6.5 Friction Sensitivity; References; 4 Explosion Risk and Protection 4.1 Essential Conditions for Explosion Occurrence4.2 Parameters of Dust Explosion; Denitions; 4.3 Some Physical and Chemical Properties of Agricultural Dusts; 4.4 Explosion Characteristics; 4.5 Propagation of Explosion; 4.6 Dynamics of Explosions in Long Ducts and Galleries; 4.7 Causes of Fires and Fire-Explosion Protection; 4.7.1 Age of the Facilities, Maintenance and Repair Work; 4.7.2 Nature of Processed Materials; 4.7.3 Ignition Sources; 4.7.4 Plant Operation; 4.7.5 Type of Buildings and Facilities; 4.7.6 Equipment for Dust Collection; 4.7.7 Plant Automation; 4.7.8 Human Factor 4.8 Fire and Explosion Prevention and Protection in the Storage of Agro, Feed and Food Products |
Record Nr. | UNINA-9910146116203321 |
Weinheim, : Wiley-VCH, c2009 | ||
Materiale a stampa | ||
Lo trovi qui: Univ. Federico II | ||
|
Fires in silos [[electronic resource] ] : hazards, prevention, and fire fighting / / edited by Ulrich Krause |
Pubbl/distr/stampa | Weinheim, : Wiley-VCH, c2009 |
Descrizione fisica | 1 online resource (158 p.) |
Disciplina | 363.379 |
Altri autori (Persone) | KrauseUlrich, Dr. |
Soggetto topico |
Silos - Fires and fire prevention
Fire extinction Chemical plants - Risk assessment |
ISBN |
1-282-02177-X
9786612021770 3-527-62382-5 3-527-62381-7 |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Fires in Silos: Hazards, Prevention, and Fire Fighting; Contents; Preface; 1 Introduction; 1.1 Problem Description; 1.2 Influence of Material Properties on Fire; 1.2.1 Particle Size Distribution, Particle Shape and Internal Surface Area; 1.2.2 Bulk Porosity and Bulk Density; 1.2.3 Porosity of Individual Particles; 1.2.4 Particle Density; 1.2.5 Humidity; 1.3 Chemical Properties of Bulk Goods; 1.3.1 Chemical Structure; 1.3.2 Heat of Formation and Calorific Value; References; 2 Ignition Sources; 2.1 Introduction; 2.2 External Ignition Sources; 2.2.1 Hot Solids, Liquids or Gases
2.2.1.1 Ignition of Gases by Hot Solids2.2.1.2 Ignition of Dust Clouds by Hot Solids; 2.2.1.3 Ignition of Solids by Hot Solids; 2.2.2 Flames or Remote Burning Objects; 2.2.3 Electric Current, Static Electricity, Electromagnetic Waves and Particulate Radiation; 2.2.3.1 Electric Current; 2.2.3.2 Static Electricity; 2.3 Self-Heating; 2.4 Physical Characteristics of Self-Ignition Processes and Smoldering Fire Propagation; References; 3 Fire Risk Assessment; 3.1 Introduction; 3.2 Experimental Techniques; 3.2.1 Ignition Sensitivity; 3.2.1.1 Minimum Ignition Temperature (MIT) 3.2.1.2 Minimum Explosible Concentration (Lower Explosion Limit (MEC/LEL))3.2.1.3 Minimum Ignition Energy (MIE); 3.2.2 Explosion Severity; 3.2.2.1 Explosion Pressure (Pmax ); 3.2.2.2 Maximum Rate of Pressure Rise (dp/dt); 3.2.2.3 Kmax Specific Constant; 3.2.3 Thermal Susceptibility; 3.2.3.1 Maciejasz Index (MI); 3.2.3.2 Temperature of Emission of Flammable Volatiles (TEV); 3.2.3.3 Thermogravimetry (TG) Test; 3.2.3.4 Differential Scanning Calorimetry (DSC); 3.2.3.5 Susceptibility Evaluation: Activation Energy (Ea) 3.2.3.6 Susceptibility Evaluation: Characteristic Oxidation Temperature (Tcharac )3.2.4 Thermal Stability; 3.2.4.1 Self-Ignition Temperature (SIT); 3.2.5 Classication of Solid Dangerous Goods; 3.2.5.1 Solids which are Readily Combustible; 3.2.5.2 Substances Liable to Spontaneous Combustion; 3.2.5.3 Substances which, in Contact with Water, Release Flammable Gases; 3.2.5.4 Oxidizing Substances; 3.2.6 Other Tests; 3.2.6.1 Flammability; 3.2.6.2 Burning Behavior; 3.2.6.3 Grewer Oven; 3.2.6.4 Impact Sensitivity; 3.2.6.5 Friction Sensitivity; References; 4 Explosion Risk and Protection 4.1 Essential Conditions for Explosion Occurrence4.2 Parameters of Dust Explosion; Denitions; 4.3 Some Physical and Chemical Properties of Agricultural Dusts; 4.4 Explosion Characteristics; 4.5 Propagation of Explosion; 4.6 Dynamics of Explosions in Long Ducts and Galleries; 4.7 Causes of Fires and Fire-Explosion Protection; 4.7.1 Age of the Facilities, Maintenance and Repair Work; 4.7.2 Nature of Processed Materials; 4.7.3 Ignition Sources; 4.7.4 Plant Operation; 4.7.5 Type of Buildings and Facilities; 4.7.6 Equipment for Dust Collection; 4.7.7 Plant Automation; 4.7.8 Human Factor 4.8 Fire and Explosion Prevention and Protection in the Storage of Agro, Feed and Food Products |
Record Nr. | UNINA-9910829811103321 |
Weinheim, : Wiley-VCH, c2009 | ||
Materiale a stampa | ||
Lo trovi qui: Univ. Federico II | ||
|
Fires in silos : hazards, prevention, and fire fighting / / edited by Ulrich Krause |
Pubbl/distr/stampa | Weinheim, : Wiley-VCH, c2009 |
Descrizione fisica | 1 online resource (158 p.) |
Disciplina | 363.379 |
Altri autori (Persone) | KrauseUlrich, Dr. |
Soggetto topico |
Silos - Fires and fire prevention
Fire extinction Chemical plants - Risk assessment |
ISBN |
1-282-02177-X
9786612021770 3-527-62382-5 3-527-62381-7 |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Fires in Silos: Hazards, Prevention, and Fire Fighting; Contents; Preface; 1 Introduction; 1.1 Problem Description; 1.2 Influence of Material Properties on Fire; 1.2.1 Particle Size Distribution, Particle Shape and Internal Surface Area; 1.2.2 Bulk Porosity and Bulk Density; 1.2.3 Porosity of Individual Particles; 1.2.4 Particle Density; 1.2.5 Humidity; 1.3 Chemical Properties of Bulk Goods; 1.3.1 Chemical Structure; 1.3.2 Heat of Formation and Calorific Value; References; 2 Ignition Sources; 2.1 Introduction; 2.2 External Ignition Sources; 2.2.1 Hot Solids, Liquids or Gases
2.2.1.1 Ignition of Gases by Hot Solids2.2.1.2 Ignition of Dust Clouds by Hot Solids; 2.2.1.3 Ignition of Solids by Hot Solids; 2.2.2 Flames or Remote Burning Objects; 2.2.3 Electric Current, Static Electricity, Electromagnetic Waves and Particulate Radiation; 2.2.3.1 Electric Current; 2.2.3.2 Static Electricity; 2.3 Self-Heating; 2.4 Physical Characteristics of Self-Ignition Processes and Smoldering Fire Propagation; References; 3 Fire Risk Assessment; 3.1 Introduction; 3.2 Experimental Techniques; 3.2.1 Ignition Sensitivity; 3.2.1.1 Minimum Ignition Temperature (MIT) 3.2.1.2 Minimum Explosible Concentration (Lower Explosion Limit (MEC/LEL))3.2.1.3 Minimum Ignition Energy (MIE); 3.2.2 Explosion Severity; 3.2.2.1 Explosion Pressure (Pmax ); 3.2.2.2 Maximum Rate of Pressure Rise (dp/dt); 3.2.2.3 Kmax Specific Constant; 3.2.3 Thermal Susceptibility; 3.2.3.1 Maciejasz Index (MI); 3.2.3.2 Temperature of Emission of Flammable Volatiles (TEV); 3.2.3.3 Thermogravimetry (TG) Test; 3.2.3.4 Differential Scanning Calorimetry (DSC); 3.2.3.5 Susceptibility Evaluation: Activation Energy (Ea) 3.2.3.6 Susceptibility Evaluation: Characteristic Oxidation Temperature (Tcharac )3.2.4 Thermal Stability; 3.2.4.1 Self-Ignition Temperature (SIT); 3.2.5 Classication of Solid Dangerous Goods; 3.2.5.1 Solids which are Readily Combustible; 3.2.5.2 Substances Liable to Spontaneous Combustion; 3.2.5.3 Substances which, in Contact with Water, Release Flammable Gases; 3.2.5.4 Oxidizing Substances; 3.2.6 Other Tests; 3.2.6.1 Flammability; 3.2.6.2 Burning Behavior; 3.2.6.3 Grewer Oven; 3.2.6.4 Impact Sensitivity; 3.2.6.5 Friction Sensitivity; References; 4 Explosion Risk and Protection 4.1 Essential Conditions for Explosion Occurrence4.2 Parameters of Dust Explosion; Denitions; 4.3 Some Physical and Chemical Properties of Agricultural Dusts; 4.4 Explosion Characteristics; 4.5 Propagation of Explosion; 4.6 Dynamics of Explosions in Long Ducts and Galleries; 4.7 Causes of Fires and Fire-Explosion Protection; 4.7.1 Age of the Facilities, Maintenance and Repair Work; 4.7.2 Nature of Processed Materials; 4.7.3 Ignition Sources; 4.7.4 Plant Operation; 4.7.5 Type of Buildings and Facilities; 4.7.6 Equipment for Dust Collection; 4.7.7 Plant Automation; 4.7.8 Human Factor 4.8 Fire and Explosion Prevention and Protection in the Storage of Agro, Feed and Food Products |
Record Nr. | UNINA-9910876552303321 |
Weinheim, : Wiley-VCH, c2009 | ||
Materiale a stampa | ||
Lo trovi qui: Univ. Federico II | ||
|
Guidelines for chemical process quantitative risk analysis [[electronic resource]] |
Edizione | [2nd ed.] |
Pubbl/distr/stampa | New York, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2000 |
Descrizione fisica | 1 online resource (786 p.) |
Disciplina |
660.2804
660.281 |
Soggetto topico | Chemical plants - Risk assessment |
ISBN |
1-282-78332-7
9786612783326 0-470-93542-1 1-59124-456-0 0-470-93541-3 |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Guidelines for Chemical Process Quantitative Risk Analysis; Contents; Preface; Preface to the First Edition; Acknowledgments; Acknowledgments to the First Edition; Management Overview; Organization of the Guidelines; Acronyms; 1 Chemical Process Quantitative Risk Analysis; 1.1. CPQRA Definitions; 1.2. Component Techniques of CPQRA; 1.2.1. Complete CPQRA Procedure; 1.2.2. Prioritized CPQRA Procedure; 1.3. Scope of CPQRA Studies; 1.3.1. The Study Cube; 1.3.2. Typical Goals of CPQRAs; 1.4. Management of Incident Lists; 1.4.1. Enumeration; 1.4.2. Selection; 1.4.3. Tracking
1.5. Applications of CPQRA1.5.1. Screening Techniques; 1.5.2. Applications within Existing Facilities; 1.5.3. Applications within New Projects; 1.6. Limitations of CPQRA; 1.7. Current Practices; 1.8. Utilization of CPQRA Results; 1.9. Project Management; 1.9.1. Study Goals; 1.9.2. Study Objectives; 1.9.3. Depth of Study; 1.9.4. Special User Requirements; 1.9.5. Construction of a Project Plan; 1.9.6. Project Execution; 1.10. Maintenance of Study Results; 1.11. References; 2 Consequence Analysis; 2.1. Source Models; 2.1.1. Discharge Rate Models; 2.1.2. Flash and Evaporation 2.1.3. Dispersion Models2.2. Explosions and Fires; 2.2.1. Vapor Cloud Explosions (VCE); 2.2.2. Flash Fires; 2.2.3. Physical Explosion; 2.2.4. BLEVE and Fireball; 2.2.5. Confined Explosions; 2.2.6. Pool Fires; 2.2.7. Jet Fires; 2.3. Effect Models; 2.3.1. Toxic Gas Effects; 2.3.2. Thermal Effects; 2.3.3. Explosion Effects; 2.4. Evasive Actions; 2.4.1. Background; 2.4.2. Description; 2.4.3. Example Problem; 2.4.4. Discussion; 2.5. Modeling Systems; 2.6. References; 3 Event Probability and Failure Frequency Analysis; 3.1. Incident Frequencies from the Historical Record; 3.1.1. Background 3.1.2. Description3.1.3. Sample Problem; 3.1.4. Discussion; 3.2. Frequency Modeling Techniques; 3.2.1. Fault Tree Analysis; 3.2.2. Event Tree Analysis; 3.3. Complementary Plant-Modeling Techniques; 3.3.1. Common Cause Failure Analysis; 3.3.2. Human Reliability Analysis; 3.3.3. External Events Analysis; 3.4. References; 4 Measurement, Calculation, and Presentation of Risk Estimates; 4.1. Risk Measures; 4.1.1. Risk Indices; 4.1.2. lndividual Risk; 4.1.3. Societal Risk; 4.1.4. lnjury Risk Measures; 4.2. Risk Presentation; 4.2.1. Risk Indices; 4.2.2. lndividual Risk; 4.2.3. Societal Risk 4.3. Selection of Risk Measures and Presentation Format4.3.1. Selection of Risk Measures; 4.3.2. Selection of Presentation Format; 4.4. Risk Calculations; 4.4.1. lndividual Risk; 4.4.2. Societal Risk; 4.4.3. Risk Indices; 4.4.4. General Comments; 4.4.5. Example Risk Calculation Problem; 4.4.6. Sample Problem Illustrating That F-N Curves Cannot Be Calculated from lndividual Risk Contours; 4.5. Risk Uncertainty, Sensitivity, and Importance; 4.5.1. Uncertainty; 4.5.2. Sensitivity; 4.5.3. Importance; 4.6. References; 5 Creation of CPQRA Data Base; 5.1. Historical incident Data 5.1.1. Types of Data |
Record Nr. | UNISA-996212666303316 |
New York, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2000 | ||
Materiale a stampa | ||
Lo trovi qui: Univ. di Salerno | ||
|
Guidelines for chemical process quantitative risk analysis [[electronic resource]] |
Edizione | [2nd ed.] |
Pubbl/distr/stampa | New York, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2000 |
Descrizione fisica | 1 online resource (786 p.) |
Disciplina |
660.2804
660.281 |
Soggetto topico | Chemical plants - Risk assessment |
ISBN |
1-282-78332-7
9786612783326 0-470-93542-1 1-59124-456-0 0-470-93541-3 |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Guidelines for Chemical Process Quantitative Risk Analysis; Contents; Preface; Preface to the First Edition; Acknowledgments; Acknowledgments to the First Edition; Management Overview; Organization of the Guidelines; Acronyms; 1 Chemical Process Quantitative Risk Analysis; 1.1. CPQRA Definitions; 1.2. Component Techniques of CPQRA; 1.2.1. Complete CPQRA Procedure; 1.2.2. Prioritized CPQRA Procedure; 1.3. Scope of CPQRA Studies; 1.3.1. The Study Cube; 1.3.2. Typical Goals of CPQRAs; 1.4. Management of Incident Lists; 1.4.1. Enumeration; 1.4.2. Selection; 1.4.3. Tracking
1.5. Applications of CPQRA1.5.1. Screening Techniques; 1.5.2. Applications within Existing Facilities; 1.5.3. Applications within New Projects; 1.6. Limitations of CPQRA; 1.7. Current Practices; 1.8. Utilization of CPQRA Results; 1.9. Project Management; 1.9.1. Study Goals; 1.9.2. Study Objectives; 1.9.3. Depth of Study; 1.9.4. Special User Requirements; 1.9.5. Construction of a Project Plan; 1.9.6. Project Execution; 1.10. Maintenance of Study Results; 1.11. References; 2 Consequence Analysis; 2.1. Source Models; 2.1.1. Discharge Rate Models; 2.1.2. Flash and Evaporation 2.1.3. Dispersion Models2.2. Explosions and Fires; 2.2.1. Vapor Cloud Explosions (VCE); 2.2.2. Flash Fires; 2.2.3. Physical Explosion; 2.2.4. BLEVE and Fireball; 2.2.5. Confined Explosions; 2.2.6. Pool Fires; 2.2.7. Jet Fires; 2.3. Effect Models; 2.3.1. Toxic Gas Effects; 2.3.2. Thermal Effects; 2.3.3. Explosion Effects; 2.4. Evasive Actions; 2.4.1. Background; 2.4.2. Description; 2.4.3. Example Problem; 2.4.4. Discussion; 2.5. Modeling Systems; 2.6. References; 3 Event Probability and Failure Frequency Analysis; 3.1. Incident Frequencies from the Historical Record; 3.1.1. Background 3.1.2. Description3.1.3. Sample Problem; 3.1.4. Discussion; 3.2. Frequency Modeling Techniques; 3.2.1. Fault Tree Analysis; 3.2.2. Event Tree Analysis; 3.3. Complementary Plant-Modeling Techniques; 3.3.1. Common Cause Failure Analysis; 3.3.2. Human Reliability Analysis; 3.3.3. External Events Analysis; 3.4. References; 4 Measurement, Calculation, and Presentation of Risk Estimates; 4.1. Risk Measures; 4.1.1. Risk Indices; 4.1.2. lndividual Risk; 4.1.3. Societal Risk; 4.1.4. lnjury Risk Measures; 4.2. Risk Presentation; 4.2.1. Risk Indices; 4.2.2. lndividual Risk; 4.2.3. Societal Risk 4.3. Selection of Risk Measures and Presentation Format4.3.1. Selection of Risk Measures; 4.3.2. Selection of Presentation Format; 4.4. Risk Calculations; 4.4.1. lndividual Risk; 4.4.2. Societal Risk; 4.4.3. Risk Indices; 4.4.4. General Comments; 4.4.5. Example Risk Calculation Problem; 4.4.6. Sample Problem Illustrating That F-N Curves Cannot Be Calculated from lndividual Risk Contours; 4.5. Risk Uncertainty, Sensitivity, and Importance; 4.5.1. Uncertainty; 4.5.2. Sensitivity; 4.5.3. Importance; 4.6. References; 5 Creation of CPQRA Data Base; 5.1. Historical incident Data 5.1.1. Types of Data |
Record Nr. | UNINA-9910830665503321 |
New York, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2000 | ||
Materiale a stampa | ||
Lo trovi qui: Univ. Federico II | ||
|
Guidelines for chemical process quantitative risk analysis |
Edizione | [2nd ed.] |
Pubbl/distr/stampa | New York, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2000 |
Descrizione fisica | 1 online resource (786 p.) |
Disciplina | 660/.2804 |
Soggetto topico | Chemical plants - Risk assessment |
ISBN |
1-282-78332-7
9786612783326 0-470-93542-1 1-59124-456-0 0-470-93541-3 |
Formato | Materiale a stampa |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Guidelines for Chemical Process Quantitative Risk Analysis; Contents; Preface; Preface to the First Edition; Acknowledgments; Acknowledgments to the First Edition; Management Overview; Organization of the Guidelines; Acronyms; 1 Chemical Process Quantitative Risk Analysis; 1.1. CPQRA Definitions; 1.2. Component Techniques of CPQRA; 1.2.1. Complete CPQRA Procedure; 1.2.2. Prioritized CPQRA Procedure; 1.3. Scope of CPQRA Studies; 1.3.1. The Study Cube; 1.3.2. Typical Goals of CPQRAs; 1.4. Management of Incident Lists; 1.4.1. Enumeration; 1.4.2. Selection; 1.4.3. Tracking
1.5. Applications of CPQRA1.5.1. Screening Techniques; 1.5.2. Applications within Existing Facilities; 1.5.3. Applications within New Projects; 1.6. Limitations of CPQRA; 1.7. Current Practices; 1.8. Utilization of CPQRA Results; 1.9. Project Management; 1.9.1. Study Goals; 1.9.2. Study Objectives; 1.9.3. Depth of Study; 1.9.4. Special User Requirements; 1.9.5. Construction of a Project Plan; 1.9.6. Project Execution; 1.10. Maintenance of Study Results; 1.11. References; 2 Consequence Analysis; 2.1. Source Models; 2.1.1. Discharge Rate Models; 2.1.2. Flash and Evaporation 2.1.3. Dispersion Models2.2. Explosions and Fires; 2.2.1. Vapor Cloud Explosions (VCE); 2.2.2. Flash Fires; 2.2.3. Physical Explosion; 2.2.4. BLEVE and Fireball; 2.2.5. Confined Explosions; 2.2.6. Pool Fires; 2.2.7. Jet Fires; 2.3. Effect Models; 2.3.1. Toxic Gas Effects; 2.3.2. Thermal Effects; 2.3.3. Explosion Effects; 2.4. Evasive Actions; 2.4.1. Background; 2.4.2. Description; 2.4.3. Example Problem; 2.4.4. Discussion; 2.5. Modeling Systems; 2.6. References; 3 Event Probability and Failure Frequency Analysis; 3.1. Incident Frequencies from the Historical Record; 3.1.1. Background 3.1.2. Description3.1.3. Sample Problem; 3.1.4. Discussion; 3.2. Frequency Modeling Techniques; 3.2.1. Fault Tree Analysis; 3.2.2. Event Tree Analysis; 3.3. Complementary Plant-Modeling Techniques; 3.3.1. Common Cause Failure Analysis; 3.3.2. Human Reliability Analysis; 3.3.3. External Events Analysis; 3.4. References; 4 Measurement, Calculation, and Presentation of Risk Estimates; 4.1. Risk Measures; 4.1.1. Risk Indices; 4.1.2. lndividual Risk; 4.1.3. Societal Risk; 4.1.4. lnjury Risk Measures; 4.2. Risk Presentation; 4.2.1. Risk Indices; 4.2.2. lndividual Risk; 4.2.3. Societal Risk 4.3. Selection of Risk Measures and Presentation Format4.3.1. Selection of Risk Measures; 4.3.2. Selection of Presentation Format; 4.4. Risk Calculations; 4.4.1. lndividual Risk; 4.4.2. Societal Risk; 4.4.3. Risk Indices; 4.4.4. General Comments; 4.4.5. Example Risk Calculation Problem; 4.4.6. Sample Problem Illustrating That F-N Curves Cannot Be Calculated from lndividual Risk Contours; 4.5. Risk Uncertainty, Sensitivity, and Importance; 4.5.1. Uncertainty; 4.5.2. Sensitivity; 4.5.3. Importance; 4.6. References; 5 Creation of CPQRA Data Base; 5.1. Historical incident Data 5.1.1. Types of Data |
Record Nr. | UNINA-9910877368603321 |
New York, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2000 | ||
Materiale a stampa | ||
Lo trovi qui: Univ. Federico II | ||
|