Process Safety Journey

Similar documents
Lessons Learned from the Texas City Refinery Explosion Mike Broadribb

Mark Bly Executive Vice President, Safety and Operational Risk. Managing safety and operational risk in BP

The Risk of LOPA and SIL Classification in the process industry

AUSTRALIA ARGENTINA CANADA EGYPT NORTH SEA U.S. CENTRAL U.S. GULF. SEMS HAZARD ANALYSIS TRAINING September 29, 2011

THE BAKER REPORT HOW FINDINGS HAVE BEEN USED BY JOHNSON MATTHEY TO REVIEW THEIR MANUFACTURING OPERATIONS

Engineering Safety into the Design

Longford Royal Commission into the Explosion and Fire on 25 September 1998 at the Esso Gas Processing Plant

SEMS II: BSEE should focus on eliminating human error

Process Safety Value and Learnings Central Valley Chemical Safety Day March 20, 2014

PRO Lifting Operations

Nitrogen System Contamination

Major Hazard Facilities. Control Measures and Adequacy

PSM TRAINING COURSES. Courses can be conducted in multi-languages

Operational Risk Using BowTie Methodology

Every things under control High-Integrity Pressure Protection System (HIPPS)

Safety in Petroleum Industry

Inherently Safer Design Analysis Approaches

Purpose. Scope. Process flow OPERATING PROCEDURE 07: HAZARD LOG MANAGEMENT

Unattended Bleeder Valve Thaws, Causing Fire

Best Practice RBI Technology Process by SVT-PP SIMTECH

Drain Splash Back Burns Operator

National Safety Council 94 th Annual Congress and Expo. Commitment to a Proactive Safety Culture: Abnormal Situation Recognition and Management

Hazard Management Making your workplace safer

Introduction to Emergency Response & Contingency Planning

Asset Integrity. We must have effective asset integrity management.

A study on the relation between safety analysis process and system engineering process of train control system

Management of Change (MOC) Could Have Prevented Death

Raw Material Spill. Lessons Learned. Volume 05 Issue USW

(2) but does not include a shaft, trench or tunnel that is a mine or is part of the workings of a mine.

Operator Exposed to Chlorine Gas

Using LOPA for Other Applications

Identification and Screening of Scenarios for LOPA. Ken First Dow Chemical Company Midland, MI

Process Safety Management Of Highly Hazardous Chemicals OSHA 29 CFR

Large Valve Causes Back Injury

SAFETY PLAN REVIEW. FirstElement Safety Plan Review Submission for the California Energy Commission General Funding Opportunity GFO

Incorrect Relief Valve Material Causes Release

Project & Task Work Health and Safety Risk Management Procedure

Cutting Oils Used With Metal Cutting Machines Are Biological Hazards

Vessel Overflow Burns Operator

Process Safety Management is the application of management principles and systems to the identification, understanding, and control of process

NAVIGATIONAL SAFETY MANAGEMENT SYSTEM MANUAL

Risks Associated with Caissons on Ageing Offshore Facilities

Safety is a priority at Vault Pipelines.

CONTRACTOR WHS HAZARD STANDARD CONFINED SPACE EXTERNAL USE ONLY

Pressure Test Results in Injury

Temporary Equipment Fails After 20 Years of Use Worker Gets Sandblasted

O&M MANUAL HIGHLIGHTS

How HSE regulates onshore oil and gas

Session One: A Practical Approach to Managing Safety Critical Equipment and Systems in Process Plants

Load Falls From Crane

Isolation Standard - Tags

The Bowtie Methodology

Flammable Environments Guideline

Using Consequence Modeling to Help Make Emergency Decisions

// RoWSaF Making roads safer for road workers rowsaf.org.uk. RoWSaF Strategy 2015

MAHB. INSPECTION Process Hazard Analysis

Pressure Gauge Failure Causes Release

innova-ve entrepreneurial global 1

To comply with the OHS Act, the responsible manager must carry out and document the following:

A MESSAGE FROM THE MD

MARINE SAFETY PLAN

Codex Seven HACCP Principles. (Hazard Identification, Risk Assessment & Management)

SAFETY PLAN REVIEW ITM

Dow s New Practice for Locating Temporary Portable Buildings. P. Partridge 9/29/05 UNRESTRICTED - May be shared with anyone Slide 1

LADDERS FIXED AND PORTABLE

Health and Safety Executive. Key aspects of HS(G) 253. Andrew Hall HID CI 1G. HM Specialist Inspector (Mechanical)

Process Safety Fundamentals Gulf of Mexico Engagement. Copyright of Shell International

Instrument Craftsman Receives Caustic Burn to Ear

SUMMARY OF SAFETY INVESTIGATION REPORT

MAINTENANCE AND SAFETY OF CNG REFUELLING STATIONS

Significant Change to Dairy Heat Treatment Equipment and Systems

Section 4. Fundamentals of Accident/Incident Prevention. Accidents/Incidents are Preventable

A Continued Worker Safety Issue

Managing Injury Risk at Grain Handling Facilities. Matt Shurtliff Director of Safety and Environmental Issues J.D. Heiskell & Co January 17, 2018

INHERENTLY SAFER DESIGN CASE STUDY OF RAPID BLOW DOWN ON OFFSHORE PLATFORM

Hazardous Waste Training Plan. Supersedes: 02/15/16 (Rev.02) Preparer: Owner: Approver: EHS Team Member EHS Team Member EHS Manager

The Relationship Between Automation Complexity and Operator Error

Safety Engineering - Hazard Identification Techniques - M. Jahoda

CONTRACTOR SAFETY INDUCTION HANDBOOK

DIGITAL SOLUTIONS TRAINING CATALOGUE. QRA and CFD simulation. Phast, Safeti and KFX SAFER, SMARTER, GREENER

CONTRACTOR WHS HAZARD STANDARD HAZARDOUS CHEMICALS EXTERNAL USE ONLY

1. Objective of the initiative To ensure that all employees and subcontractors are aware of the risks associated with working at height.

HEALTH & SAFETY ARRANGEMENTS FOR MANAGEMENT OF WORK AT HEIGHT

Biomedical Laboratory: Its Safety and Risk Management

SECTION 1 PROFILE. (c) Competent Authority: HHRM - HELLENIC HYDROCARBONS RESOURCES MANAGEMENT SA

A Production Operator Received a Lime Burn on His Wrist

VALIDATE LOPA ASSUMPTIONS WITH DATA FROM YOUR OWN PROCESS

REPEATED ACCIDENT CAUSES CAN WE LEARN?

ISS Safety Rules. Make safety second nature

OPERATING PROCEDURES

Dropped Object Prevention Scheme Recommended Practice

Eliminating Dropped Objects at the Worksite

Bogo Operations Pollution Incident Response Management Plan

Employ The Risk Management Process During Mission Planning

Issue: Issued By: Environment, Health & Safety Part: Hazard Identification and Assessment Revision #: 2 Revision

Songa Mercur King Post Failure

WHS PROCEDURE P Confined Spaces. Approved by: Ruth Hampton Review Date: 6 th December 2015

2. IMMEDIATE RESPONSE ACTIONS AND NOTIFICATION PROCEDURES

Improving Accuracy of Frequency Estimation of Major Vapor Cloud Explosions for Evaluating Control Room Location through Quantitative Risk Assessment

Section J. How to develop safety elements for project safety management system. How to develop safety elements for project SMS

Transcription:

Process Safety Journey

Agenda The Status in early 2000s The Journey to improvement in Process Safety management Managing risks and barriers How has this impacted Kwinana?

The Status in early 2000s Focus was on personal safety RIF rates, DAFW etc Process safety was driven by the regulator There were some pockets working on process safety Hazops, inspection teams etc Management focus was on (personal) safety, efficient operation and reducing cost

Significant Incidents

The Process Safety Journey Senior management more mindful that big incidents can happen and we need to do something about them first step was to consistently define risk rank the risks set an acceptability criteria for the risks

Define Risk What is Risk? Risk = Severity * Frequency Severity is number of injuries or fatalities, how bad the environmental or societal damage or how much it costs Frequency is how often Therefore a big explosion may have the same risk level as falling over twisting your ankle on gravel

Ranking the Risks Many Fatalities, huge cost BP confidential These risks positioned on the matrix reflect an internal risk process intended to provide a relative understanding of risks for the purpose of business prioritization and risk reduction. It is intended to be read in conjunction with GDP3.1 0001 and RM P 3.1 0101 and RM P 3.1 0103 for the year to which this S&O Risk Process document relates, which underpin the process and provide further context. 1 2 3 4 5 6 7 8 8 9 10 11 12 13 14 15 7 8 9 10 11 12 13 14 Severity 6 7 8 9 10 11 12 13 5 6 7 8 9 10 11 12 4 5 6 7 8 9 10 11 3 4 5 6 7 8 9 10 2 3 4 5 6 7 8 9 Injury, small cost 1 2 3 4 5 6 7 8 Every million yrs Frequency More than yearly Colours in Matrix determines at what level in company needs to endorsed continued operation eg Purple = CEO

Determination of the Risk We then used a model (QRA type) to define significant events and their severity and frequency Using a standardised procedure we mapped these onto the 8*8 matrix We also set up an independent organisation to assure conformance of expectations and that we ensured visibility and control of how we managed our risks. Three key concepts: Standardized Systems Third Party Inspection ( You don t get what you expect you get what you inspect ) Developing the Skills and Attitudes of Individuals - The guts to suspend operations when necessary You need to respect even the smallest amount of risk and evaluate the risk constantly. Risk management is a process not an event

The Risk Matrix- A Balance of Scenarios Low frequency Higher consequence High frequency lower consequence

Improving our Risks We reviewed our risks (locally and with the corporate organisation) and started focusing on purple level risks We then started designing them out Put lots of Investment into many projects in many entities around the world Shutdown some high risk facilities (eg HF alky plant at Bulwer in Queensland)

Ongoing Risk The oil industry is a high risk industry ( we boil oil up to 700 deg c!!) A lot can be designed out however we will always have to manage residual risk This is done by understanding and managing the barriers we have to protect us

Original Barriers - TEXAS CITY ISOM FAILURE Hierarchy of control Bias towards hardware/inherent safety & reducing the scope for human error multi barrier defence Relief and Blowdown System Learning from the Past Operations Procedures Effective Supervision / Leadership Audit & Self Regulation Communication Active & Passive Fire Protection Rescue & Recovery Investigation & Lessons Learned Inherent Design Plant Layout Control, Alarm & Shutdown system Maintenance & Inspection Work Control Training & Competency Management of Change Escape / Access Support to Next of Kin & Injured HAZARD Normal Hydrocarbon Inventory in Raffinate Splitter HAZARD REALIZATION Loss of containment Ignition Explosion Inventory increased Proximity of nonessential personnel to hazard Flare not used No up to date relief study - design basis unclear Capacity of blowdown drum exceeded Operate outside envelop No failsafe shutdown No mass balance or attention to other data Lost process control Previous incidents & upsets not reported Admin. rather than ISD solutions Hierarchy of control not applied Faulty high level alarm not reported Procedures not followed Steps not signed off Use of local practices Failure to recognize hazard to trailers from start-up People not notified of startup Multiple sources of ignition in adjacent areas Confusion over who was in charge No verification on procedures in use Absent from unit at critical times Inadequate HAZID skills Lack of underpinning knowledge Failure to follow procedures Pre-start-up review not performed Procedural compliance not checked Supervisor offsite No interventions Inadequate KPI s for process safety No effective handover between shifts Unit alarm not sounded No / incomplete MOC s for trailer siting Blowdown drum modified without rigorous MOC Multiple fatalities and injuries Active & passive fire protection Access & escape route diversity Access to scene Emergency response by site and external authorities Hospitalization 12

Barrier & OMS Evolution H A Z A R D BARRIERS ESCALATION CONTROLS TOP EVENT C O N S E Q U E N C E - We started to understand and recognise barriers and how they prevented and mitigated incidents - We developed centrally an OMS (operating management system) which systematically defined how we should operate our facilities and hence manage our barriers 2005 2015

Example of Standard Barriers in 2015 Prevention P1 - Plant Layout P4 - Mechanical integrity P5 - Relief systems P6 BPCS P7 SISs P8 Safety Related Alarms P10 - Conformance to critical procedures (S/U, S/D, Cracker Pro. Mitigation M2 - Fire, Explosion, and Toxic Gas Protection M3 - Emergency response M4 - Ignition prevention M6 - Fire and gas detection and shutdown M7 - Active fire protection P13 - Isolation, intervention and reinstatement - (Control of Work) P13 -Task Risk Assessment (CoW)

Maintaining Barriers Next Step is the health of barriers Over time everything degrades Need Self verification/audit/assurance Focus began on monitoring leading KPIs as well as the existing lagging KPIs for both Personal and Process safety (e.g. Orange Book reporting across Group) Management Review (of self-verification programme) Operating Programme Reviews (OPR) Field Inspections (FI)

Orange Book Metrics Review - Kwinana Major Incidents and HiPo's Workforce Fatalities MIA's Levels A E HiPo's Levels A E Process Safety Events PSE Tier 1 Incidents PSE Tier 2 Incidents Operations Integrity Loss of Primary Containment (Levels A G) Fires and Explosions All Severities Number of Oil Spills > 1bbl Volume of Oil Spills > 1bbl total volume Health and Safety DAFWCF DAFWC Recordable Injury Frequency (RIF) (per month) Number of Injuries (Recordable) Severe Vehicle Accident Rate (SVAR) First Aid Injuries Assets Overdue Plant Inspections & Tests Priviledge to Operate Compliance Notices Government Reportables Action Tracking Number of Purple & Blue C+ Risks No of Overdue Actions Group Audit No of Delinquent Actions Incident Investigations (A E) No Overdue Open Actions Incident Investigations (F) No Overdue Open Actions Plant Inspections & Tests Overdue Corrective Actions HVL's Overdue Actions Examples of KPIs reported to head office tracking personal and process safety 16

Performance Showing real Improvements 10

Process Safety Management Steps in 2015 Understand your risks Evaluate your risks (severity & frequency) Eliminate or minimise your risks by design Manage your remaining risks Ensure your understand your barriers Put adequate barriers in place Verify and assure your barriers are still strong (KPIs)

How Has this impacted Kwinana Spent lots of Investment on mitigation of risks, some examples are New/strengthened buildings Water sprays on toxic plants to knock toxics Fire fighting equipment, mobile and fixed on tanks (this is all on top of a very good (BP best in class) system previously) Improved our barriers, some examples are Implemented the grouped defined OMS (operating management system) to ensure greater systemisation in operation and hence barrier control Significant costs on improving our inspection Improved our understanding of criticality of equipment Implement many self verification and audit programs on test health of barriers

How Has this impacted Kwinana This change in culture has significantly impacted the performance at Kwinana Process safety incidents and near misses have significantly reduced Operational Availability and Reliability has increased However..At a cost we re still recovering from: Majority of Investment on Safety / Compliance vs Commercial Severe damage to our reputation Cost was rarely in the conversation for a number of years and while competitors were getting more efficient and increasing capability Why must each generation have to re-learn the lessons of the previous one?