VUT 6.4.2006 1 Funkční bezpečnost elektrických přístrojů souvisejících s bezpečností VUT 6.4.2006 Funkční bezpečnost Část celkové bezpečnosti týkající se EUC a systému řízení EUC závislá na správném fungování E/E/EP systémů souvisejících s bezpečností, systémech souvisejících s bezpečností založených na jiných technických principech a vnějších prostředcích pro snížení rizika ČSN EN 61508-4 2 3 VUT 6.4.2006 VUT 6.4.2006 Process. Mechanical Safety Action (if available) Plant Shut-down Wild Process parameter If Operator takes action High Alarm level DCS Functionality Certain Process parameter value High Control level Normal behavior Low Control level Time 4 Safety System. VUT 6.4.2006 Mechanical Safety Action (if available) Plant Shut-down Safety Instrumented System Functionality ESD controlled Trip level Wild Process parameter If Operator takes action High Alarm level DCS Functionality Certain Process parameter value High Control level Normal behavior Low Control level Time 5 VUT 6.4.2006 Have You Been Asked This? “How can you demonstrate that you are safe?” 6 VUT 6.4.2006 Safety Issues for End User / Operators • How do you demonstrate that your operations are ‘safe’? • How do you demonstrate that your equipment is ‘safe’? • How do you demonstrate that your safety and protective systems protect against your hazards? You can answer these questions by demonstrating compliance with Industry Safety Standards IEC61508 - Functional safety of electrical/electronic/programmable electronic safety-related systems 7 VUT 6.4.2006 What is IEC61508? 8 • An international standard relating to the Functional Safety of electrical / electronic / programmable electronic safety related systems – Mainly concerned with E/E/PE safety-related systems whose failure could have an impact on the safety of persons and/or the environment – Could also be used to specify any E/E/PE system used for the protection of equipment or product • It is an industry best practice standard to enable you to reduce the risk of a hazardous event to a tolerable level Technologies Concerned VUT 6.4.2006 • E • • E • • PES • • • • Electrical electro-mechanical / relays / interlocks Electronic solid state electronics Programmable Electronic Systems Programmable Logic Controllers (PLC’s); Microprocessor based systems Distributed Control Systems Other computer based devices (“smart” sensors / transmitters / actuators) VUT 6.4.2006 Features • • • • • Generic Standard Guidance on the use of E/E/PES Comprehensive approach involving concepts of Safety Lifecycle and includes all elements of the protective system Risk-based approach leading to determination of Safety Integrity Levels (S.I.Ls) Considers the entire Safety Critical Loop VUT 6.4.2006 Generic and Application Sector Standards 11 IEC61513 : Nuclear Sector IEC61511 : Process Sector Medical Sector IEC62061 : Machinery Sector VUT 6.4.2006 IEC61511 Functional Safety Safety instrumented systems for the Process industry sector VUT 6.4.2006 IEC 61511 13 “FUNCTIONAL SAFETY: SAFETY INSTRUMENTED SYSTEMS FOR THE PROCESS INDUSTRY SECTOR” Industries VUT 6.4.2006 Applies to a wide variety of industries across the process sector Including: 14 Chemicals Oil refining Oil and gas production Pulp and paper Non-nuclear power generation Pharmaceuticals / Fine Chemicals VUT 6.4.2006 Scope • Process (chemicals, oil & gas, paper, nonnuclear power generation) • End-to-end safety instrumented system (SIS) h/w, s/w, mgt. and human factors • Full safety lifecycle - specification, design, integration, operation, maintenance • Intended for integrators / users – not for equipment designers / vendors 15 Structure VUT 6.4.2006 IEC 61511 – Structure Normative Part 1 – “Framework, definitions, system, hardware and software requirements”. Part 2 – “Guidelines for the application of IEC 61511-1”. Informative 16 Part 3 – “Guidance for the determination of safety integrity levels”. IEC 61511 VUT 6.4.2006 TITLE - “Functional Safety – Safety Instrumented Systems for the Process Industry sector” • This international Standard gives requirements for the specification, design, installation, operation and maintenance of a safety instrumented system, so that it can be confidently entrusted to place and/or maintain the process in a safe state. • This standard has been developed as a process sector implementation of IEC 61508. 17 VUT 6.4.2006 Relationship IEC 61511 & IEC 61508 VUT 6.4.2006 Relationship IEC 61511 & IEC 61508 VUT 6.4.2006 Similarities (IEC 61508 - IEC 61511) 20 • Whole safety lifecycle – Concept, Hazard & Risk Analysis and Design – through operation & maintenance to eventual decommissioning • Safety requirements specification • Safety integrity levels (SIL 1 to 4) • End-to-end system – (Sensor via Logic to Actuator) • Hardware reliability analysis (PFD) • Management of functional safety • Architectural constraints (fault tolerance) VUT 6.4.2006 Key Differences IEC 61511 (IEC 61508) • Terminology – Process (EUC) – Basic Process Control System (EUC Control system) – Safety Instrumented System (E/E/PE S-R-S) – Safety Instrumented Function (Safety function) • Presentation – less rigorous than IEC 61508 – more guidance (especially in Parts 2 & 3) 21 VUT 6.4.2006 Overall Safety Lifecycle in IEC 61508 22 1 Concept 2 Overall Scope Definition 3 Hazard Risk Analysis 4 Overall Safety Requirements 5 Safety Requirements Allocation 9 Overall Planning 6 Overall Operation & Maintenance Planning 7 Overall Validation Planning 8 Overall Installation & Commissioning Planning Safety Related Systems: E / E / PES 10 Realisation 12 Overall Installation & Commissioning 13 Overall Safety Validation 14 Overall Operation & Maintenance 16 Decommissioning Safety Related Systems: Other Technology Realisation 11 External Risk Reduction Facilities Realisation Back to appropriate Overall Safety Lifecycle Phase 15 Overall Modification & Retrofit VUT 6.4.2006 IEC 61508 - ownership of phases PRE-DESIGN End user / operator (Phases 1 to 5) DESIGN AND INSTALLATION (Phases 6 to 13) Engineering Contractors / Equipment Supplier OPERATION End user / operator (Phases 14 to 16) 23 VUT 6.4.2006 Pre-Design : Phases 1 - 5 1 : Concept 2 : Overall Scope Definition 3 : Hazard Risk Analysis 4 : Overall Safety Requirements 5 : Safety Requirements Allocation 24 Can you demonstrate that you have identified all your hazards? Can you demonstrate that you are using adequate and correct methods of hazard protection? Design & Implementation : Phases 6 - 13 VUT 6.4.2006 How do you ensure competencies for all these activities? Can you demonstrate that you pass the necessary information into these activities? Overall Planning 6 : Overall Operations and Maintenance Planning 7: Overall Validation Planning 9 : Safety Related Systems : E/E/PES 8: Overall Installation & Commissioning Planning Can you demonstrate that all necessary information has been passed to you from these activities? 25 10 : Safety Related Systems : Other Technology 11 : External Risk Reduction Facilities 12 : Overall Installation & Commissioning 13 : Overall Safety Validation VUT 6.4.2006 Operation : Phases 14 - 16 14 : Overall Operations and Maintenance 15 : Overall Modification and Retrofit 16 : Decommissioning 26 Can you demonstrate that you maintain / test / analyse your protective systems correctly? Can you demonstrate that you are in control of your modification process? Supply Chain IEC 61511 VUT 6.4.2006 Requirement Specification End User System Designer – Integrator IEC 61508 27 Commissioning and Use Sub-system Designer Component Manufacturer VUT 6.4.2006 Risk VUT 6.4.2006 What is Risk? • The probable rate of occurrence of a hazard causing harm AND • the degree of severity of the harm – Qualitatively - Words – Quantitatively - Figures 29 Levels of Risk and ALARP (As Low As Reasonably Practicable) Risk cannot be justified except in extraordinary circumstances VUT 6.4.2006 Unacceptable region Tolerable only if risk reduction is impracticable or if its cost is grossly disproportionate to the improvement gained The ALARP or Tolerability region (Risk is undertaken only if a benefit is desired) As the risk is reduced the less, proportionately, it is necessary to spend to reduce it further. The concept of diminishing proportion is shown by the triangle. Broadly acceptable region (No need for detailed working to demonstrate ALARP) Negligible risk Necessary to maintain assurance that risk remains at this level 31 VUT 6.4.2006 VUT 6.4.2006 Risk reduction: General concepts Actual risk remaining Risk to meet Level of Safety Plant Under Control risk Necessary minimum risk reduction Actual risk reduction Partial risk covered by Other Technology safety-related systems Partial risk covered by E/E/PES protective systems Partial risk covered by External Risk Reduction Facilities Risk reduction achieved by all protective systems & External Risk Reduction Facilities 32 Increasing risk VUT 6.4.2006 Extent of Safety Related System Equipment (plant) Under Control (EUC) PE SRS SENSOR 33 PROGRAMMABLE ELECTRONICS ACTUATOR What is a Safety Related System (SRS) ? VUT 6.4.2006 Examples • Any system that implements safety functions necessary to achieve a safe state for the “Equipment Under Control”, or to maintain it in a safe state. VUT 6.4.2006 Hazard Identification and Risk Analysis A typical Methodology for Hazard Identification and Risk Analysis (by the end user) • • • • • • • Hazard studies and HAZOPs Evaluate possible consequences Establish tolerable frequencies vs ALARP Build event chain Estimate demand rates Define protection required Specify required SIL “ Failure categories” in IEC 61508 VUT 6.4.2006 • A = Random Hardware Failures OR • B = Systematic Failures • specification; • systematic hardware; • software; • maintenance; • all failures that are not random A B VUT 6.4.2006 Safety Integrity Level SIL LOW DEMAND MODE OF OPERATION SAFETY (Probability of failure INTEGRITY to perform its LEVEL designed function on (SIL) demand) CONTINUOUS/HIGH DEMAND MODE OF OPERATION (Probability of one dangerous failure per hour) 4 >= 10-5 up to < 10-4 >= 10-9 up to < 10-8 h-1 3 >= 10-4 up to < 10-3 >= 10-8 up to < 10-7 h-1 2 >= 10-3 up to < 10-2 >= 10-2 up to < 10-1 >= 10-7 up to < 10-6 h-1 >= 10-6 up to < 10-5 h-1 1 PFD PFH Probability of Failure on Probability of Failure per Demand Hour 38 Basic Design Unacceptable Increasing Severity VUT 6.4.2006 Risk and Determination of Safety Integrity Levels No Protection Increasing Likelihood VUT 6.4.2006 Risk Reduction Requirements 39 Safety Integrity Risk Reduction Level 1 10-100 2 100 – 1,000 3 1,000 – 10,000 4 10,000 – 100,000 VUT 6.4.2006 Reliability, Failure Rate and Availability at each level 40 Reliability Probability of failure on demand Trip Unavailable (per year) 90% - 99% 0.1 to 0.01 876 to 87.6hrs 99% - 99.9% 0.01 to 0.001 87.6 to 8.76hrs SIL 1 SIL 2 SIL 3 99.9% 99.99% 0.001 to 0.0001 8.76hrs to 52.6 mins SIL 4 99.99% 99.999 % 0.0001 to 0.00001 52.6 mins to 5.3 mins VUT 6.4.2006 Protective System Technology SIL 1 SIL 2 SIL 3 SIL 4 41 Standard components, single channel or twin non-diverse channels Standard components, 1 out of 2 or 2 out of 3, possible need for some diversity. Allowance for common-cause failures needed Multiple channel with diversity on sensing and actuation. Common-cause failures a major consideration. Should rarely be required in Process Industry Specialist design. Should never be required in the Process Industry VUT 6.4.2006 Determined to achieve the correct SIL level... VUT 6.4.2006 SIL assessment • Various methods available: • Qualitative risk graph • Calibrated risk graph (methodology only – not definitive) • Layer Of Protection Analysis (LOPA) • Hazardous event severity Matrix • Quantified Risk Analysis (QRA) • Which one to use? Develop your own? VUT 6.4.2006 Calculation of PFDAVG 35% of PFD Avg SE 15% of PFD Avg LS 50% of PFD Avg FE Distribution of the Failure Measures 35 % Sensors + 15 % Logic solver + 50 % Final elements VUT 6.4.2006 PFD-figures for a HIMA system, example 35 % 15% 50% Risk Graph acc. DIN V VDE 19250 probability of the frequency possibility unwanted occurrence & exposure of avoiding relatively slight very slight time hazardous high events minor injury no influence to the environment possible VUT 6.4.2006 consequence risk parameter dead of 1 person rare not possible periodic influence to the environment possible frequent not possible dead to several people rare permanent influence to the environment frequent disaster RC/AK according DIN V VDE 19250 SIL according IEC 61508 requirement classes RC or AK Safety Integrity Levels (SIL) IEC 61508 Concept of layers of protection acc. IEC 61511 VUT 6.4.2006 LOPA COMMUNITY EMERGENCY RESPONSE Emergency broadcasting PLANT EMERGENCY RESPONSE Evacuation procedures MITIGATION Mechanical mitigation systems Safety instrumented control systems Operator supervision PREVENTION Mechanical protection system Process alarms with operator corrective action Safety instrumented control systems Safety instrumented prevention systems CONTROL and MONITORING Basic process control systems Monitoring systems (process alarms) Operator supervision PROCESS VUT 6.4.2006 Hazardous event severity Matrix VUT 6.4.2006 Funkční bezpečnost 49 Část celkové bezpečnosti týkající se EUC a systému řízení EUC závislá na správném fungování E/E/EP systémů souvisejících s bezpečností, systémech souvisejících s bezpečností založených na jiných technických principech a vnějších prostředcích pro snížení rizika
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