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    Safety and Security Review for the Process Industries

    Safety and Security Review for the Process Industries

    - Application of HAZOP, PHA, What-IF and SVA Reviews

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    Bog E-bog
    • Format
    • Bog, hardback
    • Engelsk

    Beskrivelse

    Dennis Nolan, drawing on decades of experience as a well-known safety author and senior loss prevention specialist at Saudi Aramco, provides the essential procedures and checklists in Safety and Security Review for the Process Industries. In addition to guiding the reader through the selection and execution of efficient and complete hazard analysis and safety reviews (such as HAZOP, PHA, What-If, SVA, LOPA, Bowtie), Nolan shares his personal experience and illustrates procedures with real-world examples. Updated throughout to reflect changing practices, the fourth edition expands its scope to include maintenance, exploratory drilling, and governmental regulation updates. It adds best practice guidelines on CHAZOP reviews, expands on threats in the security vulnerability analysis, and includes more information on chemical process facilities and hydrocarbon/chemical plant safeguards. Up-to-date form templates and “what-if” checklists are also available for purchasers of the book to download, making this a complete safety review toolkit.

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    Detaljer
    • SprogEngelsk
    • Sidetal192
    • Udgivelsesdato05-09-2014
    • ISBN139780323322959
    • Forlag Gulf Publishing Company
    • FormatHardback
    Størrelse og vægt
  • Vægt410 g
    • coffee cup img
    10 cm
    book img
    15,2 cm
    22,9 cm

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    Design Information Software Distribution Audit Notes TARGET Schedule+ Acceptance Insurance Leadership Computer Speed Reputation Communication Marketing Adaptation Threat Consultants Culture Documentation Efficiency Engineering Evaluation Hazardous substances Identification Insight Knowledge Management Meetings Organization Regulations Risk Production Modification Cost Analysis Methodology Participation Chemicals Note-taking Draft Costs Policy Pipelines Contractors Effectiveness Description Format Safety Personnel Hardware Columns Experience Natural gas Qualitative Quality Confidentiality Duties Records Defects Brainstorming Drawings Law enforcement Word processing Failures Causes Quantitative Time Reviews Value Location Maintenance Petroleum Duration Life cycle Overhead projection Policies Review Security Resources Loss Implement Implementation Obligations Stages Data Legal Assessment Probability Vapor Récord Mapping Safety Instrumented System Files Résolution Likelihood Procedure Titles Formula Risk-reduction Limitations Trained Final Human Errors Onshore Flexible Concern Consequence Offshore Objectives Preparation Steps Toxic Expectations Refinery Effects Preliminary Adversary Failure Mode Availability Nodes SVA What if? Visible Détail Risk analysis Meeting Security requirements Rejected Threat Analysis Operations Unrest Markers Project Manager Conceptual Statement Assumptions Hazard Identification Design Review Checklist Hazards Team Leader Responsibilities Scénario Vulnerability Comments Consultant Valuable Report Qualifications Diagram Incident Facility Electronic Efficient Drilling Severity Independent Calculation Cost-effective Feasibility Study Systematic Procedures Node Effort Criteria Concerns Reports Regulatory Rôle Worksheets Identify Support Team dynamics Deviations Ranking Vulnerability Assessment Issues Suggestions Important Experts Prioritization Vulnerabilities Hazard Hazard assessment Recommendations PHA Step up BTA Vulnerable Bow tie Addendum Unmanned Cost Estimate Methodical Economical Incidents Safeguards Scribe Accepted Temporary Worksheet Pumping Disadvantages Cost-benefit Copies Sessions Credible Team members acknowledge administrative support ALARP American Institute of Chemical Engineers (AIChE) As-Built Business interruption American Petroleum Institute (API) Butterfly diagram Chemical Facility Anti-Terrorism Standard (CFATS) Chemical Safety Hazard Investigation Board (CSB) Cause consequence diagram Chemical plant Department of Homeland Security (DHS) Deliberate acts CHAZOP Estimate Event Tree (ET) evaluated Gas plant Exposures EHAZOP Facility changes Environmental Protection Agency (EPA) Guideword Hard copies Failure Modes and Effects Analysis (FMEA) final design Credible scenarios Incidental costs detailed design HAZOP interruptions Initiating cause Judged Electrical apparatus failure Example calculation executive order Magnitude Fault Tree (FT) Management approval Monetary commitment Mitigate loss prevention Occupational Safety and Health Administration (OSHA) Process Hazard Analysis process operations Periodic evaluation Industry practices Pre-startup safety review (PSSR) Process condition road map Public population Process Hazard Analysis (PHA) Separation facility Supplemental members Inadequate recommendations Team Approach Time bar variances Labor rate wellheads lopa Process Safety Management (PSM) Safety Integrity Level Personnel-hours Tank Farm Security Vulnerability Analysis (SVA) skill level Transcribe

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