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|a Inherently safer design.
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|a [S.l.] :
|b Academic Press,
|c 2023.
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|a 1 online resource.
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|a text
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|a Methods in chemical process safety ;
|v 7
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|a Intro -- Inherently Safer Design -- Copyright -- Contents -- Contributors -- Preface -- Chapter One: Introduction to inherently safer design -- 1. Hierarchy of controls -- 2. Inherently safer design -- 3. Advantages, limitations, and implications of ISD -- 3.1. Improved safety -- 3.2. Reduced costs -- 3.3. Improved sustainability -- 3.4. Improved public perception and stakeholder confidence -- 4. Applications of inherently safer design -- 5. Overview and development of this volume -- References -- Chapter Two: Fundamentals of inherently safer design -- 1. Inherently safer design strategies -- 1.1. The elimination/minimization strategy of ISD -- 1.1.1. Reducing the volume of hazardous materials -- 1.1.2. Reducing inventory levels -- 1.1.3. Minimization using process intensification -- 1.1.4. Minimization by reducing the number and size of critical process equipment -- 1.1.5. Minimization using reduced energy requirements -- 1.1.6. Minimization using reducing waste and emissions -- 1.1.7. Minimization by reducing formation of dust layers and dust clouds -- 1.2. Substitution strategy of ISD -- 1.2.1. Substitution of materials -- 1.2.2. Substitution using alternative chemistry -- 1.2.3. Substitution of process steps -- 1.2.4. Substitution of equipment -- 1.3. Moderation strategy of ISD -- 1.3.1. Moderation using process conditions -- 1.3.2. Moderation by dilution and refrigeration -- 1.3.3. Moderation by inerting -- 1.3.4. Moderation through control of the specific surface area -- 1.4. Simplification strategy of ISD -- 1.4.1. Simplifying system design -- 1.4.2. Using simple, robust, and modular designs -- 1.4.3. Using simpler equipment or materials -- 1.4.4. Simplification of SOP -- 1.4.5. Simplification of model or algorithm -- 2. ISD implementation at various stages of the process design life cycle -- 3. Practical considerations in ISD.
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|a 4. Conclusion -- References -- Chapter Three: The history of inherently safer design (ISrD) -- 1. Introduction -- 2. Early days -- 3. Trevor Kletz -- 4. Two disasters incentivize IS -- 5. Measurement of (inherent) safety -- 6. Extending the index concept to environmental and occupational health impacts -- 7. Process intensification -- 8. Inherent safety regulation -- 9. The future -- References -- Chapter Four: Multiscale process integration techniques for inherently safer design -- 1. Introduction -- 2. What is process integration? -- 3. The multiscale nature of process integration towards ISD -- 4. Incorporating process-integration targets into a multicriteria economic framework -- 5. Conclusions -- References -- Chapter Five: ISD indices -- 1. Introduction -- 2. Indices based on material and chemistry aspects -- 2.1. Prototype index of inherent safety (PIIS) -- 2.2. iSafe Index -- 3. Indices based on equipment aspects -- 3.1. Inherent safety index (ISI) -- 3.2. Inherent safety index calculation (ISIC) -- 3.3. Multi-tier inherent safety indices -- 3.4. Inherent safety assessment of process equipment (ISAPE) -- 4. Indices including economic aspects -- 4.1. Rapid risk analysis-based design -- 4.2. Integrated inherent safety index (I2SI) -- 4.3. Risk-based inherent safety index (RISI) -- 5. Other indices -- 5.1. Inherent Benign-ness Indicator (IBI) -- 5.2. Inherent occupational health index (IOHI) -- 6. Summary and discussion -- References -- Chapter Six: Application of inherently safer design in human factor engineering -- 1. Introduction -- 2. What is human factor engineering (HFE) -- 3. Application of inherently safer design in human factor engineering -- 4. Existing studies of inherently safer design on HFE -- 4.1. Extensive discussions in the Trevor Kletz Compendium book -- 4.2. Other related works.
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|a 5. ISD to reduce workers exposure in occupational health study -- 5.1. Health hazards and risks factors -- 5.2. Health hazards -- 5.3. Health risks -- 5.4. Human exposure assessment -- 5.5. Assumptions in the exposure assessment -- 5.6. Fugitive emissions -- 6. Inherent safety strategies on HFE -- References -- Chapter Seven: Conceptual and practical applications of ISD -- 1. Introduction -- 2. Process risk management incorporating ISD -- 2.1. Integrating ISD with HAZID/PHA -- 2.2. Risk-based inherently safer design -- 2.2.1. Risk-based Inherent Safety Index (RISI) -- 2.2.2. Risk estimation of base design (RiskBD) -- 2.2.3. Estimation of inherent safety risk (ISRisk) and selection of optimal design -- 3. ISD framework for technical and non-technical initiatives -- 3.1. Road map for incorporating ISD concepts through the life cycle -- 3.2. Selection of optimal initiatives -- 3.3. Evaluation indexes and decision-making -- 4. Inherently safer design considering potential accident costs -- 4.1. Gaps in the cost analysis of ISD -- 4.2. Methodology for selecting optimal ISD scheme -- 4.3. Case study -- 5. Dust explosions -- 5.1. Inherent safety principles of dust explosions -- 5.2. Application to process hazard analysis -- 5.3. Application to risk management of dust explosions -- 6. Applications to the nuclear industry -- 7. Conclusions -- References -- Chapter Eight: Challenges to ISD application -- 1. Introduction -- 2. Approaches to inherent safety assessment and to ISD -- 3. ISD implementation in design and monitoring practices -- 4. Limits in current ISD approach -- 5. Challenges related to industry perception of ISD -- 6. Challenges related to regulatory requirements for other measures in the hierarchy of controls -- 7. Implementation of risk metrics in ISD -- 7.1. Widening the scope of ISD.
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|a 7.2. Integrating ISD with a broader framework concerning sustainability analysis -- 8. Conclusions -- References -- Chapter Nine: ISD regulatory requirements -- 1. Introduction -- 2. Regulatory design types -- 3. Inherent safety in united states regulations -- 3.1. Environmental protection agency -- 3.2. New Jersey toxic catastrophe prevention act -- 3.3. California accidental release prevention regulations -- 3.3.1. Contra Costa County Ordinance -- 4. United kingdom inherent safety regulations -- 5. Concluding remarks -- References -- Chapter Ten: Inherently safer design: Case studies -- 1. Introduction -- 2. Detailed case studies -- 2.1. The Flixborough disaster -- 2.1.1. Minimization or intensification -- 2.1.2. Moderation -- 2.2. The Bhopal gas tragedy -- 2.2.1. Minimization or intensification -- 2.2.2. Substitution -- 2.3. Mexico City disaster -- 2.3.1. Minimization -- 2.3.2. Moderation -- 2.3.3. Substitution -- 2.3.4. Simplification -- 2.4. Westray coal mine explosion -- 2.4.1. Minimization -- 2.4.2. Substitution -- 2.4.3. Moderation -- 2.4.4. Simplification -- 2.5. West fertilizer explosion -- 2.5.1. Minimization -- 2.5.2. Simplification -- 2.5.3. Substitution -- 3. Lessons from other accidents -- 4. Conclusion -- References -- Further reading -- Chapter Eleven: Information security risk-based inherently safer design for intelligent oil and gas pipeline systems -- 1. Introduction -- 2. Bibliometric and knowledge graph analysis -- 3. Information security risk and novel accident-causing mechanisms for intelligent pipeline systems -- 3.1. Attack issues -- 3.2. Vulnerability issues -- 3.3. Propagation issues -- 4. Early warning of different types of attacks on information security threats -- 5. Conclusion -- References -- Chapter Twelve: Deep probability learning-based release consequence estimation approach for inherently safer design of ch.
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|a 1. Introduction -- 2. Framework of deep probability learning-based release consequence estimation for inherently safer design of chemical plant -- 2.1. Input data related to chemical process -- 2.2. Deep probability learning-based release and dispersion consequence modeling -- 2.3. Application to inherent safer design of chemical plant -- 3. Case study 1: Hydrogen refueling station -- 3.1. Benchmark dataset -- 3.2. Model development, validation and comparison -- 4. Case study 2: LNG plant -- 4.1. Benchmark dataset -- 4.2. Model development, validation and comparison -- 5. Case study 3: Offshore platform -- 5.1. Benchmark datasets -- 5.2. Model development, validation and comparison -- 6. Conclusions -- References -- Chapter Thirteen: ISD and inherently safer operation (ISO) -- 1. Introduction -- 1.1. Dimensions of inherent assessment -- 1.2. Inherent safety and process life cycle -- 2. Inherently safer operation (ISO) -- 2.1. Scope of ISO -- 2.2. How to implement ISO -- 2.3. How ISO can be helpful -- 3. Guidewords for ISO -- 4. Case studies for ISO implementation -- 4.1. Bromine storage facility-Minimization and simplification -- 4.2. Ammonia storage-Substitution -- 4.3. Ethylene oxide-Moderation and simplification -- 4.4. Waste heat boiler-Substitution and screening review importance -- 5. Available research and future prospects -- 6. Summary and conclusions -- References -- Chapter Fourteen: Future of inherently safer design -- 1. Introduction -- 2. What can the history of ISD teach us? -- 3. ISD in education -- 4. ISD success stories -- 5. ISD in other industries -- 6. ISD in regulations and standards -- 7. Concluding remarks -- References.
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|a Chemical engineering
|x Safety measures.
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| 650 |
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|a S�ecurit�e du travail.
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|w (OCoLC)1361673218
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|u https://sciencedirect.uam.elogim.com/science/bookseries/24686514/7
|z Texto completo
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