Hazard and Operability (HAZOP)& Hazard Analysis Training HAZOP Fundamental A scenario… • You and your family are on a road trip by using a car in the middle of the night You were replying a text message while driving at 100 km/h and it was raining heavily The car hits a deep hole and one of your tire blows You hit the brake, but due to slippery road and your car tire thread was thin, the car skidded and was thrown off the road Points to ponder What is the cause of the accident? What is the consequence of the event? What can we to prevent all those things to happen in the first place? (5 minutes for brainstorming ideas) What other possible accidents might happen on the road trip? Can we be prepared before the accident occurs? Can we make it more systematic? Parameter Guideword Possible Causes Consequences Action Safeguard Car speed Too fast Too slow Rushing Skidded when emergency brake - Slow down - Speed up - ABS brake system - Safety belt - Air bag Tire No thread Less thread Car skidded Window visibility Low Tire too old, often speeding and emergency break Car light Dim No light Road With holes Rocky Travel time Night Foggy Rain Very low - Check frequently - Have spare tire Cannot see the road - Stop car - Go to nearest garage - Use emergency signal Breaks the car tire No street light - Put a signboard - Street lights - Travel during daylight What is HAZOP? • Systematic technique to IDENTIFY potential HAZard and OPerating problems • A formal systematic rigorous examination to the process and engineering facets of a production facility • A qualitative technique based on “guide-words” to help provoke thoughts about the way deviations from the intended operating conditions can lead to hazardous situations or operability problems • HAZOP is basically for safety - Hazards are the main concern - Operability problems degrade plant performance (product quality, production rate, profit) • Considerable engineering insight is required - engineers working independently could develop different results Origin of HAZOP • I n i t i a l l y p r e p a r e d b y D r H G Lawley and associates of ICI at Wilton in 1960’s • Subsequently C J Bullock and A J D J e n n i n g f r o m ChE D e p t Teeside Polytechnic under supervision of T.A Kletz applied the method at h i g h e r i n s t i t u t i o n ( p o s t - graduate level) • In 1977, Chemical Industries Association published the edited version L a t e r D e v e l o p m e n t - HAZOP • • ICI expanded the procedure called HAZARD STUDY steps to The ICI six steps : Project exploration / preliminary project assessment – t o i d e n t i f y i n h e r e n t h a z a r d s o f process chemicals, site suitability and probable environmental impact Project definition – to identify and reduce significant hazards associated with items and areas, check conformity with relevant standards and codes of practices USE CHECK LISTS L a t e r D e v e l o p m e n t - HAZOP Design and procurement – to examine the PID in detail for identification of deviations from design intent capable of causing operability problems or hazards During final stages of construction – to check that all recommended and accepted actions recorded in steps i, ii and iii implemented During plant commissioning – to check that all relevant statutory requirements have been acknowledges and all installed safety systems are reliably operable HAZOP Vessel FLOW PATH • (Illustrative example of HAZOP) Feed Tank Pump Check Valve REVERSAL OF FLOW To Distillation Column Distillation materials returning via pumparound Pump failure could lead to REVERSAL OF FLOW Check valve located properly prevents deviation Move check valve downstream of pumparound 91 Loss of Containment Deviations • • • • • Pressure too high Pressure too low (vacuum) Temperature too high Temperature too low Deterioration of equipment 92 HAZOP’s I n h e r e n t Assumptions • Hazards are detectable by careful review • Plants designed, built and run to appropriate standards will not suffer catastrophic loss of containment i f o p s stay within design parameters • Hazards are controllable by a combination of equipment, procedures which are Safety Critical • HAZOP conducted with openness and good faith by competent parties 93 HAZOP – P r o s a n d C o n s • C r e a t i v e , o p e n - ended • Completeness – i d e n t i f i e s a l l p r o c e s s hazards • Rigorous, structured, yet versatile • I d e n t i f i e s s a f e t y and o p e r a b i l i t y i s s u e s • Can be time- c o n s u m i n g ( e g , i n c l u d e s operability) • Relies on having right people in the room • Does not distinguish between low probability, high consequence events (and vice versa) 94 FMEA – Fa i l u r e Mo d e s , Ef f e c t s An a l y s i s • Manual analysis to determine the consequences of component, module or subsystem failures • Bottom- u p a n a l y s i s • Consists of a spreadsheet where each failure mode, possible causes, probability of occurrence, consequences, and proposed safeguards are noted 95 FMEA – F a i l u r e M o d e K e y w o r d s • • • • • • • • • • Rupture Crack Leak Plugged Failure to open Failure to close Failure to stop Failure to start Failure to continue Spurious stop • • • • • • • • • Spurious start Loss of function High pressure Low pressure High temperature Low temperature Overfilling Hose bypass Instrument bypassed 96 FMEA on a Heat Exchanger Failure Mode Causes of Failure Symptoms Tube rupture Corrosion from fluids (shell side) H/C at higher pressure than cooling water Predicted Frequency Impact Frequent – Critical – has could happened 2x cause a in 10 yrs major fire • Rank items by risk (frequency x impact) • Identify safeguards for high risk items 97 FMEA – Fa i l u r e Mo d e s , Ef f e c t s An a l y s i s • FMEA is a very structured and reliable method for evaluating hardware and systems • Easy to learn and apply and approach makes evaluating even complex systems easy to • Can be very time- consuming (and expensive) and does not readily identify areas of multiple fault that could occur • Not easily lent to procedural review as it may not identify areas of human error in the process 98 Fault Tree Analysis • Graphical method t h a t s t a r t s w i t h a hazardous event and works backwards to identify the causes o f t h e top event • Top- d o w n a n a l y s i s • Intermediate events related to the top event are combined by using logical operations such as AND and OR 99 FTA 100 Fault Tree Analysis • Provides a traceable, logical, quantitative representation of causes, consequences and event combinations • Amenable to – but for comprehensive systems, requiring – use of software • Not intuitive, requires training • Not particularly useful when temporal aspects are important 101 Accident Scenarios May Be Missed by PHA • No PHA method can identify all accidents that could occur in a process • A scenario may be excluded from the scope of the analysis • The team may be unaware of a scenario • The team consider the scenario but judge it not credible or significant • T h e t e a m m a y o v e r l o o k t h e s c e n a r i102 o Summary Despite the aforementioned issues with PHA: • Companies that rigorously exercise PHA are seeing a continuing reduction is frequency and severity of industrial accidents • Process Hazard Analysis w i l l c o n t i n u e t o play an integral role in the design and continued examination of industrial processes 103 Using What You Learn • The ideas and techniques of Process Hazard Analysis will be immediately useful in upcoming recitation e x e r c i s e o n Hazard Evaluation • Expect t o b e p a r t o f a P r o c e s s Hazard Analysis Team early on in your professional career 104 Where to Get More Information • Chemical Safety and Hazard I n v e s t i g a t i o n B o a r d ’s w e b s i t e : www.csb.gov • M P R I w e b s i t e : www Mpri.lsu.edu/main/ • Crowl a n d Louvar – C h e m i c a l P r o c e s s Safety: Fundamentals with Applications • Kletz – HAZOP & HAZAN: Notes on the Identification and Assessment of Hazards 105