This document describes the risk of a potential flash fire during sieving of combustible powders in the soft gelatin area of a GSK site in Egypt. The risk is due to insufficient controls of static electricity generation during sieving and the proximity of an electric panel. The proposed mitigation plans include applying engineering controls to manage static electricity such as installing earthing cables, dissipative sheeting and gaskets, and removing the adjacent electric panel. Implementing these controls aims to prevent serious worker injuries from a possible flash fire event and ensure business continuity.
This document provides guidelines for oil and chemical plant layout and spacing to prevent property losses from fires and explosions. It recommends:
- Adequate spacing between units housing explosion/fire hazards to limit damage. Spacing should be based on hazard analysis and overpressure calculations.
- An open layout with blocks of 300x600 feet or less and access roads between for firefighting. Hazardous units should be separated or buffered.
- Increased spacing for very hazardous equipment like reactors, unless blast walls are used.
- Locating utilities, control rooms, services away from hazards.
This document is an engineering handbook on fire and gas systems published by Kenexis Consulting Corporation. It provides an overview of Kenexis, which is an engineering consulting company focused on implementing safety systems in process plants. The handbook was written by several authors from Kenexis who have experience designing fire and gas systems and safety instrumented systems. It aims to distill best practices for performance-based fire and gas system design based on risk analysis methods from the ISA technical report on this topic. The handbook is intended as a practical reference for everyday use in fire and gas system design.
Safety Lifecycle Management - Emerson Exchange 2010 - Meet the Experts Mike Boudreaux
The document discusses process safety and functional safety. It covers many topics related to ensuring safety in industrial processes, including safety lifecycles, risk assessments, safety instrumented systems, standards like IEC 61511, and maintaining safety through proper design, installation, operation and modification of systems.
Part 4 of 6 - Analysis Phase - Safety Lifecycle Seminar - Emerson Exchange 2010Mike Boudreaux
In San Antonio, Emerson Exchange 2010 featured a new Meet the Experts concept that provides participants to interact with recognized experts on focused topics. Emerson’s Mike Boudreaux provided a 2 hour session on Safety Lifecycle Management. This was an interactive short seminar that has been designed to help business leaders and managers in the process industries have a general understanding of existing industry standards and best practices for safety instrumented systems. This seminar provides a practical overview of the safety lifecycle, including key considerations for each phase. In addition to the typical design concepts related to safety instrumented functions and safety integrity levels, important concepts such as organizational design, competency management, planning, and continuous verification will be discussed.
Part 4 describes the Analysis Phase and explains the managment considerations for hazard and risk assessment, layers of protection analysis, and safety requirements specification.
Critical Review of PSM In Petroleum Industry | Mr. Hirak Dutta, Executive Di...Cairn India Limited
This document summarizes the key points from a presentation on process safety management in India's petroleum industry. It notes that India has become a major exporter of petroleum products, with over 200 million metric tons of annual refining capacity and significant crude oil and gas production. It outlines the pillars of process safety like operational integrity and discusses taking a systemic approach. It emphasizes the importance of recognizing warning signs to avoid accidents and highlights lessons around focusing on leading indicators and inherent safety principles. The document concludes by outlining the Oil Industry Safety Directorate's focus on key drivers of process safety like procedures, hazard identification, and managing change.
Defining kpi in terms of unsafe acts/conditions and near miss Faiz Khan
This document discusses key performance indicators (KPIs) for measuring safety performance, including lagging and leading indicators. It describes lagging indicators like recordable injuries and spills that measure past performance, as well as leading indicators like safety inspections and trainings that predict future safety. The document outlines a tiered framework from API RP 754 for indicators, ranging from infrequent Tier 1 events with highest consequences to more common Tier 4 measures of management system performance. Selection of the right mix of lagging and leading KPIs is important for continuous safety improvement.
Process Safety Management in Design, Construction & Commissioning | Lalit K...Cairn India Limited
This document discusses process safety management during design, construction, and commissioning of oil and gas facilities. It outlines major hazards in the oil industry such as fires and explosions. It summarizes past disasters like the 1984 San Juanico disaster in Mexico and the 2007 LPG fire at a Texas refinery. The document discusses lessons learned like siting facilities away from housing and having effective gas detection and emergency isolation. It also outlines strategies for inherent, passive, active, and procedural safety. Key aspects of process safety are covered for different project stages from conceptualization to commissioning.
This document provides guidelines for oil and chemical plant layout and spacing to prevent property losses from fires and explosions. It recommends:
- Adequate spacing between units housing explosion/fire hazards to limit damage. Spacing should be based on hazard analysis and overpressure calculations.
- An open layout with blocks of 300x600 feet or less and access roads between for firefighting. Hazardous units should be separated or buffered.
- Increased spacing for very hazardous equipment like reactors, unless blast walls are used.
- Locating utilities, control rooms, services away from hazards.
This document is an engineering handbook on fire and gas systems published by Kenexis Consulting Corporation. It provides an overview of Kenexis, which is an engineering consulting company focused on implementing safety systems in process plants. The handbook was written by several authors from Kenexis who have experience designing fire and gas systems and safety instrumented systems. It aims to distill best practices for performance-based fire and gas system design based on risk analysis methods from the ISA technical report on this topic. The handbook is intended as a practical reference for everyday use in fire and gas system design.
Safety Lifecycle Management - Emerson Exchange 2010 - Meet the Experts Mike Boudreaux
The document discusses process safety and functional safety. It covers many topics related to ensuring safety in industrial processes, including safety lifecycles, risk assessments, safety instrumented systems, standards like IEC 61511, and maintaining safety through proper design, installation, operation and modification of systems.
Part 4 of 6 - Analysis Phase - Safety Lifecycle Seminar - Emerson Exchange 2010Mike Boudreaux
In San Antonio, Emerson Exchange 2010 featured a new Meet the Experts concept that provides participants to interact with recognized experts on focused topics. Emerson’s Mike Boudreaux provided a 2 hour session on Safety Lifecycle Management. This was an interactive short seminar that has been designed to help business leaders and managers in the process industries have a general understanding of existing industry standards and best practices for safety instrumented systems. This seminar provides a practical overview of the safety lifecycle, including key considerations for each phase. In addition to the typical design concepts related to safety instrumented functions and safety integrity levels, important concepts such as organizational design, competency management, planning, and continuous verification will be discussed.
Part 4 describes the Analysis Phase and explains the managment considerations for hazard and risk assessment, layers of protection analysis, and safety requirements specification.
Critical Review of PSM In Petroleum Industry | Mr. Hirak Dutta, Executive Di...Cairn India Limited
This document summarizes the key points from a presentation on process safety management in India's petroleum industry. It notes that India has become a major exporter of petroleum products, with over 200 million metric tons of annual refining capacity and significant crude oil and gas production. It outlines the pillars of process safety like operational integrity and discusses taking a systemic approach. It emphasizes the importance of recognizing warning signs to avoid accidents and highlights lessons around focusing on leading indicators and inherent safety principles. The document concludes by outlining the Oil Industry Safety Directorate's focus on key drivers of process safety like procedures, hazard identification, and managing change.
Defining kpi in terms of unsafe acts/conditions and near miss Faiz Khan
This document discusses key performance indicators (KPIs) for measuring safety performance, including lagging and leading indicators. It describes lagging indicators like recordable injuries and spills that measure past performance, as well as leading indicators like safety inspections and trainings that predict future safety. The document outlines a tiered framework from API RP 754 for indicators, ranging from infrequent Tier 1 events with highest consequences to more common Tier 4 measures of management system performance. Selection of the right mix of lagging and leading KPIs is important for continuous safety improvement.
Process Safety Management in Design, Construction & Commissioning | Lalit K...Cairn India Limited
This document discusses process safety management during design, construction, and commissioning of oil and gas facilities. It outlines major hazards in the oil industry such as fires and explosions. It summarizes past disasters like the 1984 San Juanico disaster in Mexico and the 2007 LPG fire at a Texas refinery. The document discusses lessons learned like siting facilities away from housing and having effective gas detection and emergency isolation. It also outlines strategies for inherent, passive, active, and procedural safety. Key aspects of process safety are covered for different project stages from conceptualization to commissioning.
Optimizing Fire3 and Gas System Design Using the ISA Technical Report ISA TR8...Kenexis
Fire and Gas Detection and Suppression Systems (FGS) have long been successfully employed as a safeguard in the process industries. Unfortunately, design methods for determining the quantity and placement of detectors have historically been less than satisfactory. Design practices based on rules of thumb and experiences have often resulted in design inconsistencies, and achievement of tolerable risk cannot be ascertained. Rule-based methods often place detectors where they are not needed and leave high risk areas unnecessarily exposed. ISA released technical report TR 84.00.07 to address this problem. This technical report explains the metrics, such as detector coverage, and techniques that can be applied to the design of FGS which results in optimal designs that are safer and more repeatable. This paper will provide an overview of the contents of the technical report, and also provide some case study examples that show how these performance-based methods result in superior designs to currently used techniques such as grid-based approaches.
Safety-critical systems are computer systems whose failure could result in injury, death, or environmental damage. Examples include aircraft control systems, nuclear power plant controls, medical devices like pacemakers, and railway signaling systems. These systems require high integrity to avoid hazards and ensure safety. Techniques like developing diverse redundant systems can improve safety by detecting and tolerating a wider range of faults.
The document discusses using wireless technology to monitor process safety key performance indicators (KPIs). It notes that wireless monitoring can provide real-time visibility into critical areas like steam traps and safety showers to improve safety compliance and efficiency. Monitoring technologies like acoustic transmitters and discrete I/O transmitters integrate with existing wireless networks to gain insights into hazards and inefficiencies.
Enform oil and gas safety: Process safey vs. personal safety Enform
Process safety focuses on preventing catastrophic accidents associated with hazardous materials, while personal safety focuses on preventing workplace injuries. Process safety concerns low probability, high consequence events like explosions, whereas personal safety addresses more frequent, lower impact incidents like slips and falls. Process safety requires technical expertise to identify major hazard risks and implement controls like engineering solutions. It also demands buy-in from senior management. The goal of process safety is to protect people, property and the environment from rare but severe incidents, while personal safety aims to prevent a series of minor incidents. Both areas are important, and their management systems have considerable overlap.
lain Engels
Product Manager Level & Safety Applications Consultant
Endress+Hauser
Alain werkt bij Endress+ Hauser sinds 1984.
Hij heeft verschillende functies gehad zoals Product Manager van Druk, Temperatuur en Niveaumetingen.
In paralell was hij ook Industrie specialist voor Chemie & Oil & Gas en ATEX, SIL en PED.
Kunzite presents iso 90012015 part 1 pdca & vendor selection processHpm India
This document discusses continual improvements in various areas like environment, health and safety, quality, and customer support. It outlines ISO 9001:2015 requirements and processes for vendor selection, quality control, hazard identification, risk assessment, and environmental aspect identification. Key areas covered include vendor audit and evaluation process, quality management principles, in-process and final product quality checks, hazard and risk ranking criteria, aspect and impact assessment, and environmental monitoring. The overall goal is to plan and implement actions to address risks, eliminate hazards, reduce impacts, and ensure continual improvements across operations.
A real-world introduction to PSM’s 14 Elements360factors
A number of recent incidents in various parts of the world have highlighted the increasing importance of effective Process Safety Management (PSM). This webinar presents a high-level overview of OSHA’s PSM requirements as well as real-world examples of how companies handle compliance.
Objectives
• Describe some of the major catastrophes which led to the formulation of PSM regulations.
• Introduce the 14 Elements of PSM.
• Present examples of various implementation approaches.
The expert group on Measurement and Control Technology aims to reach:
- Representatives from supplier circles
- Representatives from companies, study and engineering offices
- Teachers from secondary and higher education
With the following activities:
- Evening lectures: use of new equipment, method or technology, in cooperation with companies.
- Study days: thematically focused and accompanied by demonstrations or exhibitions, in cooperation with manufacturers.
- Theme-oriented courses
- Discussion meetings: for own training within the study group, with the cooperation of specialists.
This document discusses risk analysis and environmental hazard management. It begins by defining risk, hazard, and toxicity. It then outlines the steps involved in hazard identification, including HAZID, HAZOP, and HAZAN. The document presents a case study of a hypothetical gas collecting station, identifying potential accidents and hazards. It discusses quantitative and qualitative approaches to risk analysis, including calculating a fire and explosion index. The document concludes by discussing hazard management strategies like preventative measures, control measures, fire protection, relief operations, and the importance of training personnel on safety.
The document discusses process safety and functional safety. It covers topics like hazard and risk assessments, safety instrumented systems (SIS), safety integrity levels (SIL), and the safety lifecycle described in standards like IEC 61511. The purpose of process safety management is to reduce the frequency and severity of chemical accidents by implementing layers of protection that can include inherently safer design, equipment reliability, formal safety assessments, operating procedures, training and emergency response. Functional safety focuses specifically on instrumented safety systems and ensuring safety instrumented functions are designed and maintained to a reliability suitable for their risk reduction purpose.
This document summarizes a presentation on compliance with IEC 61508 for actuators. It discusses causes of valve failures, measures manufacturers take to exclude systematic errors, how valves are tested, designing and implementing automated testing, and numerical ratings. The presentation addresses questions about certification, failure rates, diagnostic coverage, useful lifetime, and achieving SIL levels. It emphasizes following the safety lifecycle to avoid systematic errors through activities like periodic inspection, examination during operation, and documentation of failures.
This document provides an overview and definitions related to Safety Instrumented Systems (SIS). It discusses the need for SIS to protect personnel, equipment, and the environment from hazardous events in industries like chemical and oil & gas. SIS are designed to reduce the likelihood or impact of emergencies. The document defines common SIS terms and describes the basic components and purpose of SIS, which include sensors to detect process parameters, a logic solver to determine necessary actions, and final control elements like valves to isolate the process. It also discusses the concept of layers of protection to prevent and mitigate hazardous events, with SIS comprising the final active prevention layer.
Ti ps conference ed marszal new process kpiKenexis
The document proposes a new process safety KPI (key performance indicator) using two metrics: (1) initiating event demand rate and (2) safeguard unavailability. This aims to better predict major losses compared to typical lagging metrics. The KPI can be automatically collected from process data and presented to management to identify unsafe areas and guide corrective actions. An example shows how a CEO and plant managers drilled down through the KPI data to identify and address frequently failing level control increasing demand rates. The KPI approach allows proactive major loss prevention through improved management oversight of process safety performance.
Process safety aims to prevent incidents involving hazardous materials that could endanger workers, property, and the environment. It involves applying engineering and operating practices to control hazards. Key elements of process safety management include process hazard analysis, operating procedures, employee participation, training, contractor management, pre-startup safety reviews, mechanical integrity programs, emergency response planning, compliance audits, and incident investigation. The goal is to anticipate, identify, evaluate, and control hazards to protect people and prevent accidents.
This document identifies and assesses environmental aspects and impacts from processes at an HPM Chemicals & Fertilizers plant. It lists various process activities, the associated aspects that could pollute the environment, potential impacts, an SSPD rating to determine significance, and actions to address significant impacts. Monitoring of air, ETP, and water quality is also included. The core team is identified and responsibilities are assigned to address issues, implement control plans, and conduct regular reviews to minimize environmental impacts and ensure compliance.
This document assesses environmental aspects and impacts from operations at an HPM Chemicals & Fertilizers plant. It identifies 8 processes that could pollute the air, soil, water or generate noise. For each process, it evaluates the severity of impact, probability of occurrence, detection difficulty and calculates an SSPD rating. Processes with SSPD over 100 are considered significant. Two processes - emissions to air from manufacturing and stack emissions - were found significant. The document lists actions already taken like installing scrubbers and conducting monitoring. It also identifies responsibilities and status of addressing significant aspects to reduce environmental impacts from plant operations.
The formation of the Process Safety Leadership Group (PSLG) in September 2007 was designed
to meet the need for an effective framework for interaction between industry, trade unions and
the COMAH Competent Authority (CA); a framework in which they could carry out a dialogue to
jointly develop, progress and implement meaningful, effective recommendations and practices that
improve safety in our industries.
This report and its recommendations represent the outcome of a tremendous amount of work by
the industry, trade unions and the regulator. I would like to thank them for all their efforts, tenacity
and input. Our work can and will make a significant contribution to improving process safety – the
challenge for all of us now is to deliver!
One the most important problem in the chemical, oil&gas or nuclear Industry is the Risk Assessment evaluation. In the theoretical studies, the part of risk analysis is sometimes not considered because the case of study is not real or it hasn't been still industrialized. In the real industry there are different processes for industrializing a product. The HAZOP technique is one example of Risk assessment tecniques. For further information go to: http://www.cholarisk.com/
Layer of Protection Analysis (LOPA) is an effective semi-quantitative tool for process hazard analysis and risk assessment. It lies between qualitative and quantitative analysis. LOPA evaluates risks by analyzing accident scenarios, their likelihood and severity. It also considers independent protective layers that can prevent or mitigate consequences. The key steps of LOPA include establishing consequence criteria, identifying scenarios, evaluating frequency and severity, examining protective layers, and comparing results to risk tolerance limits. LOPA is useful for decision making regarding safety systems and managing risks cost effectively.
The document is a newsletter from Green Circle Inc. that provides various environmental, health and safety updates. It includes:
1. News items on pollution control board initiatives in India, decreased time for environmental clearances, record low Arctic sea ice levels, and India signing the Paris Agreement.
2. Tips on effective fire protection systems including complying with fire codes, using distributed network systems, and improving evacuation routes.
3. A case study on a company that underwent modernization and a cleaner production assessment, investing 5.5 lakh and saving 11.5 lakh annually.
The document reports the results of a laser scan inspection of part wm025867-0002. A total of 4172081 data points were captured and 11894 were identified as outliers. The maximum deviation was 1.74 mm and the average deviation was 0.08/-0.12 mm. Annotation views 1-5 identify 30 points (A001-A030) by their X, Y, Z coordinates and deviation from reference in mm. All points were within the tolerance of +/-0.5 mm.
The document discusses the benefits of exercise for mental health. Regular physical activity can help reduce anxiety and depression and improve mood and cognitive function. Exercise causes chemical changes in the brain that may help protect against mental illness and improve symptoms.
Optimizing Fire3 and Gas System Design Using the ISA Technical Report ISA TR8...Kenexis
Fire and Gas Detection and Suppression Systems (FGS) have long been successfully employed as a safeguard in the process industries. Unfortunately, design methods for determining the quantity and placement of detectors have historically been less than satisfactory. Design practices based on rules of thumb and experiences have often resulted in design inconsistencies, and achievement of tolerable risk cannot be ascertained. Rule-based methods often place detectors where they are not needed and leave high risk areas unnecessarily exposed. ISA released technical report TR 84.00.07 to address this problem. This technical report explains the metrics, such as detector coverage, and techniques that can be applied to the design of FGS which results in optimal designs that are safer and more repeatable. This paper will provide an overview of the contents of the technical report, and also provide some case study examples that show how these performance-based methods result in superior designs to currently used techniques such as grid-based approaches.
Safety-critical systems are computer systems whose failure could result in injury, death, or environmental damage. Examples include aircraft control systems, nuclear power plant controls, medical devices like pacemakers, and railway signaling systems. These systems require high integrity to avoid hazards and ensure safety. Techniques like developing diverse redundant systems can improve safety by detecting and tolerating a wider range of faults.
The document discusses using wireless technology to monitor process safety key performance indicators (KPIs). It notes that wireless monitoring can provide real-time visibility into critical areas like steam traps and safety showers to improve safety compliance and efficiency. Monitoring technologies like acoustic transmitters and discrete I/O transmitters integrate with existing wireless networks to gain insights into hazards and inefficiencies.
Enform oil and gas safety: Process safey vs. personal safety Enform
Process safety focuses on preventing catastrophic accidents associated with hazardous materials, while personal safety focuses on preventing workplace injuries. Process safety concerns low probability, high consequence events like explosions, whereas personal safety addresses more frequent, lower impact incidents like slips and falls. Process safety requires technical expertise to identify major hazard risks and implement controls like engineering solutions. It also demands buy-in from senior management. The goal of process safety is to protect people, property and the environment from rare but severe incidents, while personal safety aims to prevent a series of minor incidents. Both areas are important, and their management systems have considerable overlap.
lain Engels
Product Manager Level & Safety Applications Consultant
Endress+Hauser
Alain werkt bij Endress+ Hauser sinds 1984.
Hij heeft verschillende functies gehad zoals Product Manager van Druk, Temperatuur en Niveaumetingen.
In paralell was hij ook Industrie specialist voor Chemie & Oil & Gas en ATEX, SIL en PED.
Kunzite presents iso 90012015 part 1 pdca & vendor selection processHpm India
This document discusses continual improvements in various areas like environment, health and safety, quality, and customer support. It outlines ISO 9001:2015 requirements and processes for vendor selection, quality control, hazard identification, risk assessment, and environmental aspect identification. Key areas covered include vendor audit and evaluation process, quality management principles, in-process and final product quality checks, hazard and risk ranking criteria, aspect and impact assessment, and environmental monitoring. The overall goal is to plan and implement actions to address risks, eliminate hazards, reduce impacts, and ensure continual improvements across operations.
A real-world introduction to PSM’s 14 Elements360factors
A number of recent incidents in various parts of the world have highlighted the increasing importance of effective Process Safety Management (PSM). This webinar presents a high-level overview of OSHA’s PSM requirements as well as real-world examples of how companies handle compliance.
Objectives
• Describe some of the major catastrophes which led to the formulation of PSM regulations.
• Introduce the 14 Elements of PSM.
• Present examples of various implementation approaches.
The expert group on Measurement and Control Technology aims to reach:
- Representatives from supplier circles
- Representatives from companies, study and engineering offices
- Teachers from secondary and higher education
With the following activities:
- Evening lectures: use of new equipment, method or technology, in cooperation with companies.
- Study days: thematically focused and accompanied by demonstrations or exhibitions, in cooperation with manufacturers.
- Theme-oriented courses
- Discussion meetings: for own training within the study group, with the cooperation of specialists.
This document discusses risk analysis and environmental hazard management. It begins by defining risk, hazard, and toxicity. It then outlines the steps involved in hazard identification, including HAZID, HAZOP, and HAZAN. The document presents a case study of a hypothetical gas collecting station, identifying potential accidents and hazards. It discusses quantitative and qualitative approaches to risk analysis, including calculating a fire and explosion index. The document concludes by discussing hazard management strategies like preventative measures, control measures, fire protection, relief operations, and the importance of training personnel on safety.
The document discusses process safety and functional safety. It covers topics like hazard and risk assessments, safety instrumented systems (SIS), safety integrity levels (SIL), and the safety lifecycle described in standards like IEC 61511. The purpose of process safety management is to reduce the frequency and severity of chemical accidents by implementing layers of protection that can include inherently safer design, equipment reliability, formal safety assessments, operating procedures, training and emergency response. Functional safety focuses specifically on instrumented safety systems and ensuring safety instrumented functions are designed and maintained to a reliability suitable for their risk reduction purpose.
This document summarizes a presentation on compliance with IEC 61508 for actuators. It discusses causes of valve failures, measures manufacturers take to exclude systematic errors, how valves are tested, designing and implementing automated testing, and numerical ratings. The presentation addresses questions about certification, failure rates, diagnostic coverage, useful lifetime, and achieving SIL levels. It emphasizes following the safety lifecycle to avoid systematic errors through activities like periodic inspection, examination during operation, and documentation of failures.
This document provides an overview and definitions related to Safety Instrumented Systems (SIS). It discusses the need for SIS to protect personnel, equipment, and the environment from hazardous events in industries like chemical and oil & gas. SIS are designed to reduce the likelihood or impact of emergencies. The document defines common SIS terms and describes the basic components and purpose of SIS, which include sensors to detect process parameters, a logic solver to determine necessary actions, and final control elements like valves to isolate the process. It also discusses the concept of layers of protection to prevent and mitigate hazardous events, with SIS comprising the final active prevention layer.
Ti ps conference ed marszal new process kpiKenexis
The document proposes a new process safety KPI (key performance indicator) using two metrics: (1) initiating event demand rate and (2) safeguard unavailability. This aims to better predict major losses compared to typical lagging metrics. The KPI can be automatically collected from process data and presented to management to identify unsafe areas and guide corrective actions. An example shows how a CEO and plant managers drilled down through the KPI data to identify and address frequently failing level control increasing demand rates. The KPI approach allows proactive major loss prevention through improved management oversight of process safety performance.
Process safety aims to prevent incidents involving hazardous materials that could endanger workers, property, and the environment. It involves applying engineering and operating practices to control hazards. Key elements of process safety management include process hazard analysis, operating procedures, employee participation, training, contractor management, pre-startup safety reviews, mechanical integrity programs, emergency response planning, compliance audits, and incident investigation. The goal is to anticipate, identify, evaluate, and control hazards to protect people and prevent accidents.
This document identifies and assesses environmental aspects and impacts from processes at an HPM Chemicals & Fertilizers plant. It lists various process activities, the associated aspects that could pollute the environment, potential impacts, an SSPD rating to determine significance, and actions to address significant impacts. Monitoring of air, ETP, and water quality is also included. The core team is identified and responsibilities are assigned to address issues, implement control plans, and conduct regular reviews to minimize environmental impacts and ensure compliance.
This document assesses environmental aspects and impacts from operations at an HPM Chemicals & Fertilizers plant. It identifies 8 processes that could pollute the air, soil, water or generate noise. For each process, it evaluates the severity of impact, probability of occurrence, detection difficulty and calculates an SSPD rating. Processes with SSPD over 100 are considered significant. Two processes - emissions to air from manufacturing and stack emissions - were found significant. The document lists actions already taken like installing scrubbers and conducting monitoring. It also identifies responsibilities and status of addressing significant aspects to reduce environmental impacts from plant operations.
The formation of the Process Safety Leadership Group (PSLG) in September 2007 was designed
to meet the need for an effective framework for interaction between industry, trade unions and
the COMAH Competent Authority (CA); a framework in which they could carry out a dialogue to
jointly develop, progress and implement meaningful, effective recommendations and practices that
improve safety in our industries.
This report and its recommendations represent the outcome of a tremendous amount of work by
the industry, trade unions and the regulator. I would like to thank them for all their efforts, tenacity
and input. Our work can and will make a significant contribution to improving process safety – the
challenge for all of us now is to deliver!
One the most important problem in the chemical, oil&gas or nuclear Industry is the Risk Assessment evaluation. In the theoretical studies, the part of risk analysis is sometimes not considered because the case of study is not real or it hasn't been still industrialized. In the real industry there are different processes for industrializing a product. The HAZOP technique is one example of Risk assessment tecniques. For further information go to: http://www.cholarisk.com/
Layer of Protection Analysis (LOPA) is an effective semi-quantitative tool for process hazard analysis and risk assessment. It lies between qualitative and quantitative analysis. LOPA evaluates risks by analyzing accident scenarios, their likelihood and severity. It also considers independent protective layers that can prevent or mitigate consequences. The key steps of LOPA include establishing consequence criteria, identifying scenarios, evaluating frequency and severity, examining protective layers, and comparing results to risk tolerance limits. LOPA is useful for decision making regarding safety systems and managing risks cost effectively.
The document is a newsletter from Green Circle Inc. that provides various environmental, health and safety updates. It includes:
1. News items on pollution control board initiatives in India, decreased time for environmental clearances, record low Arctic sea ice levels, and India signing the Paris Agreement.
2. Tips on effective fire protection systems including complying with fire codes, using distributed network systems, and improving evacuation routes.
3. A case study on a company that underwent modernization and a cleaner production assessment, investing 5.5 lakh and saving 11.5 lakh annually.
The document reports the results of a laser scan inspection of part wm025867-0002. A total of 4172081 data points were captured and 11894 were identified as outliers. The maximum deviation was 1.74 mm and the average deviation was 0.08/-0.12 mm. Annotation views 1-5 identify 30 points (A001-A030) by their X, Y, Z coordinates and deviation from reference in mm. All points were within the tolerance of +/-0.5 mm.
The document discusses the benefits of exercise for mental health. Regular physical activity can help reduce anxiety and depression and improve mood and cognitive function. Exercise causes chemical changes in the brain that may help protect against mental illness and improve symptoms.
1. O documento apresenta normas técnicas para elaboração de monografias de conclusão de curso.
2. Inclui definições de monografia, trabalho de conclusão de curso e ABNT, além de instruções sobre formato, estrutura e modelos de referências.
3. O autor, José Maria da Silva, busca padronizar as normas de apresentação dos trabalhos acadêmicos de acordo com as diretrizes da ABNT.
Este documento describe los principales servicios que ofrece Internet, incluyendo la navegación web, los buscadores, el correo electrónico, los foros, la mensajería instantánea, la voz sobre IP, la videoconferencia y otros servicios como el comercio electrónico, la administración electrónica y la formación a distancia. Explica brevemente cómo funcionan cada uno de estos servicios y qué se necesita para utilizarlos.
La opinión pública se forma a través de varios procesos. Se ve influenciada por la familia, la educación, los grupos sociales y los medios de comunicación. Refleja las tendencias e ideas predominantes en una sociedad sobre temas de interés común. Aunque no es simplemente la suma de opiniones individuales, la opinión pública puede cambiar con el tiempo al alterarse las condiciones culturales y psicológicas de una época.
Este documento presenta un resumen de los valores familiares discutidos en una clase de informática en la Escuela Politécnica. Describe valores como el respeto, la responsabilidad, la solidaridad y la justicia, y cómo estos se desarrollan y fomentan dentro de la familia. También expone cómo la familia es fundamental para la formación de la personalidad y los valores de sus miembros.
Microsoft Excel es una aplicación de hojas de cálculo desarrollada y distribuida por Microsoft que se usa comúnmente para tareas financieras y contables. Los gráficos dinámicos representan visualmente los datos de una tabla dinámica en Excel. Las macros en Excel consisten en código programado en VBA que automatiza tareas.
O documento apresenta o início de um mistério envolvendo uma pessoa que acorda com uma sombra grudada nela que conversa e atormenta. O detetive Pena é chamado para investigar o assassinato de duas mulheres em uma casa de penhores que ele já havia investigado anteriormente por um assalto/explosão. Ele nota semelhanças com o caso antigo.
Este documento resume las ventajas y desventajas del uso de las tecnologías de la información y la comunicación (TIC) en la educación. Algunas ventajas para los estudiantes incluyen aprendizaje más rápido, flexibilidad y acceso a más recursos, mientras que algunas desventajas son adicción, aislamiento y problemas de visión. Algunas ventajas para los profesores son acceso a más recursos educativos y actualización profesional, mientras que algunas desventajas son estrés, esfuerzo adic
Este documento presenta tres ejercicios de probabilidad y estadística. El primer ejercicio analiza la probabilidad de que pacientes tengan hipertensión arterial o hiperlipemia. El segundo ejercicio evalúa dos tratamientos para úlceras por presión y calcula las probabilidades de curación. El tercer ejercicio analiza la probabilidad de que una persona tenga más de 55 años o padezca deterioro de la movilidad.
Somos una empresa cuyo propósito principal es establecer relaciones de confianza con Socios de Negocio/Clientes mediante el acompañamiento en soluciones que brindan innovación y agilizan las actividades productivas. El documento describe un sistema de información llamado INTEGRITY que permite la atención remota de asociados de cooperativas a través de funciones integrales como la consulta y actualización de datos personales, estados de cuentas y transacciones vía portal web.
1) O artigo discute 15 dicas para melhorar a comunicação no trabalho com colegas, superiores, clientes e fornecedores. 2) As palavras que mudaram de gênero como "hóspeda", "cantatriz" e "parenta" são analisadas. 3) A fraude em tributo a Nelson Mandela reabre o debate sobre a variedade das línguas de sinais.
Mill Creek Entertainment is a leading home entertainment company that licenses and distributes content from major studios. It has a vast library of over 5,000 films, 10,000 TV shows, and 15,000 hours of special interest content. Mill Creek focuses on creating high value DVD and Blu-ray programs and has successful ongoing partnerships with various retailers. It is headquartered in Minneapolis and uses a large distribution facility to service customers.
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El documento describe los diferentes comités organizados en una institución educativa. Cada comité tiene un objetivo específico como mejorar la convivencia, fomentar el deporte, cuidar el medio ambiente, manejar la comunicación, promover la lectura, organizar eventos, evaluar temas académicos y conocer asuntos de solidaridad. Cada comité está integrado por 4 o 5 estudiantes o profesores responsables de liderar las actividades relacionadas con el objetivo del comité.
2015 palestra realizado pela patrulha ambiental do rio ivai na apae 10 07-2015Victor Ha-Kã Azevedo
A Patrulha Ambiental realiza diversas ações para preservação do meio ambiente na região do Rio Ivaí, como plantio de mudas, arrastões de limpeza dos rios, campanhas contra a dengue e palestras educativas nas escolas para conscientizar a comunidade sobre a importância da preservação ambiental e mudança de hábitos. A organização já plantou 3000 mudas em 2015 e realizou 6 arrastões contra a dengue, além de palestras sobre o impacto ambiental e a necessidade de mudanças nos hábitos diários
O documento descreve o movimento humanista no contexto do fim da Idade Média e início do Renascimento. O humanismo valorizou o ser humano e seu potencial, rompendo com a visão teocêntrica da época. A poesia palaciana, a prosa historiográfica e o teatro de Gil Vicente foram manifestações literárias desse novo pensamento no Portugal do século XV.
A turma C2 é orientada pela professora Rosário. O documento faz referência a uma turma e sua professora, sem fornecer mais detalhes sobre o conteúdo ou propósito.
Existe diferença entre plenitude de defesa e ampla defesa segundo a Constituição Brasileira. A plenitude de defesa é um direito exclusivo dos réus em julgamentos de júri e permite todos os meios de defesa, inclusive não jurídicos. A ampla defesa se aplica a todos os processos e assegura o uso de todos os meios lícitos de defesa reconhecidos em direito.
The document discusses High-Integrity Pressure Protection Systems (HIPPS), which are instrumented systems that can provide overpressure protection as an alternative to pressure relief devices. A HIPPS includes sensors, logic solvers, and final control elements arranged to reach a fail-safe state if overpressure occurs. HIPPS are safety instrumented systems that must meet standards like IEC 61511. They require careful documentation, design, testing and maintenance to ensure the level of protection is equal to or greater than a conventional pressure relief device system.
Sample risk assessment report for dcc safety studentsMuizz Anibire
The risk assessment report analyzed hazards at Xcel Energy's hydroelectric plant in Denver, Colorado. It identified the top three hazards as: 1) Entrapment in the confined penstock tunnel, 2) Fire or explosion from using flammable solvents to clean equipment, and 3) Health effects from toxic solvent exposure. The report recommended controls following the hierarchy of controls, such as substituting non-flammable cleaners. It estimated a 65-94% reduction in risks through engineering and administrative controls and substituting safer materials.
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In September 2015, the National Fire Protection Association (NFPA) issued NFPA 652, Standard on the Fundamentals of Combustible Dust. This new standard ties together myriad industry-specific codes and standards related to combustible dusts, including NFPA 61 and 654, under one overarching standard that establishes minimum requirements for managing dust hazards across all industries. Most importantly, this standard is retroactive, meaning that all facilities that handle combustible dusts must meet these new criteria by the deadline of September 2018. What are the specific requirements of this standard and how can you ensure compliance quickly and with minimal cost or disruption? This presentation will explain the testing and documentation requirements and discuss the newly-required Dust Hazard Analysis (DHA) in order to prepare your facility for compliance with NFPA 652.
1. The risk assessment identifies hazards like slips, trips, falls, vibrations, noise, dust, and heat exposure that could harm workers at the National Refinery rig site. It notes controls already in place like PPE and trainings.
2. Further actions are recommended within 1 week to 4 weeks like improving mud management, installing vibration controls, restricting cell phone use, adding air conditioning, and replacing damaged electrical wires.
3. Responsibilities are assigned to managers and supervisors to implement controls for hazards like installing exhaust ventilation, conducting safety meetings, and repairing generators. Completing these further actions would help better protect workers at the rig site.
Ahmed Hassan Reedy has 19 years of experience in process safety, health, and loss prevention in the oil, gas, and petroleum industries. He has extensive experience conducting hazard identification studies and risk assessments using various quantitative and qualitative methods. Reedy has served as the chairman for over 100 HAZOP studies and 30 SIL assessments. He is proficient in various risk analysis software tools and has conducted risk assessments and consequence modeling for over 50 projects.
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Pipeline integrity assessment with LRUT methodpaulus konda
As a product of transportation facility, pipeline sould be having a good integrity. Pipeline failure means that pipeline can not operate both at some segment/section or all of pipeline segment can not deliver product/service as per their function. Or failure of pipeline also means loss of pipeline integrity for some segment pipeline section or all of segment pipeline.
Poster_EGY_TE_Anas Momen_Hilal-Failure Modes and Effects AnalysisAnas Momen
1) The Failure Modes and Effects Analysis (FMEA) was conducted on the wellhead control panel (WHCP) of the Hilal Project in Egypt, the first time FMEA was used at such a scale in BP.
2) The FMEA identified potential failures in the WHCP's specially designed hydro-electrical control system and assessed risks, resulting in 63 actions to improve design reliability and safety.
3) Through participation of experts from various teams, the FMEA enhanced the WHCP design, enabled future Safety Integrity Level verification, and reduced risks associated with 40 items on the system. The study's procedures and lessons learned will guide BP on future projects.
This document provides information on process safety and the ten pillars of compliance approach. It begins with defining process safety and distinguishing it from occupational safety. It then discusses the ten pillars of compliance which include safety management systems, aging plant, competence, safety instrumented systems, overfill protection, containment, emergency response plans, process safety performance indicators, and safety leadership. Examples of process safety incidents caused by lack of management of change are provided. The document also includes videos and links related to process safety concepts.
Pressure Relief Systems Vol 2
Causes of Relief Situations
This Volume 2 is a guide to the qualitative identification of common causes of overpressure in process equipment. It cannot be exhaustive; the process engineer and relief systems team should look for any credible situation in addition to those given in this Part which could lead to a need for pressure relief (a relief situation).
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0 INTRODUCTION
The four main sources of Fugitive Emissions on most plants are valves, machine seals, re-makable joints and pressure relief devices. Other possible sources include open-ended lines, sampling connections, drains and vents.
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Regulatory requirements covering Fugitive Emissions exist in many countries and therefore a leak reduction program should be implemented. Fugitive Emissions also represent financial losses to the business as well as potential damage to the environment.
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ISO20072: the device developer's perspective | Insight, issue 5
Soft Gelatin PS risk21-9
1. GlaxoSmithKline - Egypt Appendix 6 to SOP TO 524/10
RISK SITUATION, TARGET AND PROPOSAL (STP) Page 1 of 6
Originating Site: Cairo Risk Identifier. Risk Internal No.:
Date of Issue: 15/9/2016 STP Ref. No.: Version: 01
RISK TITLE
Include brief, specific and clear title of the risk. The risk title should state the hazard/risk event and its major impact.
Potential flash fire during Sieving combustible powders in soft gelatin area due to insufficient controls of staticelectricity and adjacent
electric panel which might lead to operator severe burns and business interruption
RISK OWNER DETAILS
Name:
Yasser Mahdy
Job Title:
VS Head
Department:
Manufacturing
RISK STP DOCUMENT APPROVAL
Completion of the following signature block signifies that the approver has read, understands, and agrees with the content of this document.
ROLE/JOB TITLE NAME SIGNATURE DATE
STP AUTHORS:
The Author signs as having prepared this version of the risk STP in accordance with Company Policies
Risk Owner: Yasser Mahdy
Mitigation Plan 1 Owner: Helmy Ismail
Mitigation Plan 2 Owner: Amr Younis
STP APPROVERS:
Signs as agreeing with the content of this STP, with reference to the scope, background, analysis, scoring and mitigation det ails and authorizing this document as
a source for details of the described risk and for introduction into the site risk register
Head of EHS and Area of
Impact Responsible:
Sherine Zaki
Engineering / Capital
Head
Ayman El Leissy
GMS Cairo Site Director: Najib Chabaa
2. GlaxoSmithKline - Egypt Appendix 6 to SOP TO 524/10
RISK SITUATION, TARGET AND PROPOSAL (STP) Page 2 of 6
Originating Site: Cairo Risk Identifier. Risk Internal No.:
Date of Issue: 15/9/2016 STP Ref. No.: Version: 01
SITUATION
RISK DESCRIPTION
Describe the existing or potential risk hazard/event, the main cause of this hazard or event and the ultimate impact of the risk (on business, compliance, safety,
quality……)
Potential flash fire during Sieving combustible powders (Biotin , Nicotinamide & Ascorbic acid ) in soft gelatin area due to insufficient
controls of staticelectricity ,
The above 3 components represent the fire triangle by Which
-Fuel will be Combustible powder and related dust generated from thesieving process
-Ignition source will be Heat generated at the mesh surface of the sieve, Electrostatic charges from the operator, Sparks from adjacent
electric panel, all are liable to occur.
-Oxygen , exist in the normal atmosphere
It is also worth to mention that for a fire to occur there must be sufficient concentration of thefuel ignited by enough energy of the ignition
source.
With no machine controls related to the Russell sieve used except for general earthing , and No controls on operator electrostatic charges
, Moreover electric hazard from adjacent control panel which is not properly sealed with possibility of dust accumulation inside the panel .
This might lead to flash fire that will cause operator severe burns and business interruption.
BACKGROUND INFORMATION
Describe the details behind seeing or considering this problem as a risk. State facts or statistics that support this risk, and refer to potential events might happen.
Refer or attach relevant supporting references whenever appropriate. The following questions may be answered to cover a risk background:
• How did you discover the presence of this risk?
Risk was discovered after conducting Process safetyassessmentcovering manufacturing sieving processes and was also
highlighted in Sieving departmental risk assessment.
Moreover , several GEMBA done on the process pointed to the high level of dustassociated with this process ,this can be
noticed over the walls surrounding the process ,Control panel , Electric sockets
3. GlaxoSmithKline - Egypt Appendix 6 to SOP TO 524/10
RISK SITUATION, TARGET AND PROPOSAL (STP) Page 3 of 6
Originating Site: Cairo Risk Identifier. Risk Internal No.:
Date of Issue: 15/9/2016 STP Ref. No.: Version: 01
• What mightgo wrong? How is it different from the normal/standard?
• Accumulation of static charges during the sieving process especially , This will be liable to occur during the manufacturing
of ( Haemoton – Supravit – Vitamax)
Material * Minimum ignition energy(mj)
Biotin 60
Nicotinamide 15
Ascorbic Acid 12
*Minimum ignition energy (mj) The lowest energy of a discrete spark that is capable of igniting a dispersed dust
Due the nature of the sieving process , it is likely to generate heatat the sieve location that mightignite dustvapor
accumulated in the surrounding area ,It was also noticed thatthere is a Dustextraction system above the sieving location
which need to be reviewed regarding efficiency and suitability.
• Where will be the risk found? When will it occur? Why mightthings go wrong?
At Soft Gelatin area , Sieving room during the sieving of the ( Haemoton – Supravit – Vitamax) , Severe burns to the
operator from the expected flash fire .
• What is the extent or scope of the risk?
GSK operators handling sieving process in softgelatin area
• How mightthis risk impactthe business?
Serious injuries due to severe burns will affect site personnel moral and impactthe business due to losttime expected for
one or multiple employees.
Incidents/Accidents: e.g. non-conformities, complaints, rejects, deviations, accidents, serious events,….
EHS – ENG Alert 12 -011 (Low Humidity suite dust ignition )
12-011GMS Eng- EHS
Sydney Powder Ignition .docx(12-011).docx
Gaps against standards or requirements: Attach reference to gap analysis
- GES 202 (Prevention and control of DustExplosions )
- Hazardous area classification done on site at 2012 and did not include Sieving process in Soft Gelatin area
44NK9034.P01.0001
-ANNEXURE-7.3 SOFT GEL CAPSULES - Vita max.pdf
Audit observation: Attach reference
L1 L2 L3 L4
N/A
Other tools used in identification of this risk: Specify and attach references
- Process safety HAZID assessment
- Departmental risk assessment for Sieving process
HAZID Sieving at
Soft Gelatin .xlsx
DRA Sieving and
milling in Soft Gelatin processing area (2).docx
4. GlaxoSmithKline - Egypt Appendix 6 to SOP TO 524/10
RISK SITUATION, TARGET AND PROPOSAL (STP) Page 4 of 6
Originating Site: Cairo Risk Identifier. Risk Internal No.:
Date of Issue: 15/9/2016 STP Ref. No.: Version: 01
EXISTING CONTROLS
Describe all currently applied measures that ensure putting the stated risk under certain level of control
- Dustextraction system presentlevel of control regarding notreaching high dustaccumulation over the sieve.
- Sieve head is covered to minimize dustrelease
- Sieve body is earthed
- Electric panel is closed all over the process
- Good air change in the room ( 10-15 ACH)
- Operator understanding for the hazard while joining all the assessments .
EXISTING MONITORING
Describe all currently applied techniques, procedures or systems that are used to monitor the progress in the level of the stated risk
- GEMBA at the location
- ZAPs
- Escalation to EHS Council
RISK EVALUATION
Include here all details that support your risk scoring exercise
Initial Risk Score
Risk Area of Impact Consequence Statement Consequence
Score Likelihood Statement Likelihood
Score RIV
Business - Cost
Business - Reputation
Business - Supply
Environment,Health & Safety Severe burn or tissue damage 4
May see severalincidents
during w orking life
2 8
Product Quality
Quality Compliance
Other Compliance
Comment on initial risk score:
N/A
Current Score: Severe burn or tissue damage 4
May see severalincidents
during w orking life 2 8
Comment on current risk score:
ROOT CAUSE ANALYSIS
Include here the results of root cause analysis of the stated risks
Ref. Root Cause Category
RC01 Insufficient control of static electricity in Sieving process Process
RCO2 Insufficient design assessment for both Control Panel and existing Suction hood Design
Comment on root cause analysis:
N/A
5. GlaxoSmithKline - Egypt Appendix 6 to SOP TO 524/10
RISK SITUATION, TARGET AND PROPOSAL (STP) Page 5 of 6
Originating Site: Cairo Risk Identifier. Risk Internal No.:
Date of Issue: 15/9/2016 STP Ref. No.: Version: 01
TARGET
IDEAL SOLUTION SPECIFICATIONS
State the criteria that need to be fulfilled by the ideal solution to this risk. You may select from the below stated criteria or specify new criteria
Address identified rootcause/s
Complywith local regulations
Complywith companystandards/rules
Achievable within acceptable timeframe
Realistic and adequatelyresourced
Sustainable and preventrecurrence
Other criteria: please specify:
EXPECTED BENEFITS
State the benefits that will be gained when the below proposed solution is implemented
Prevent serious injuries to GSK employees atSoft Gelatin area
PROPOSAL
PROPOSED SOLUTION OPTIONS
Specify options proposed to mitigate this risk. Specify the scope of each option and its impact. Specify the selected options.
-Apply engineering controls to achieve high level of control on static electricity ( Earthing cable - Dissipative sheet - Sieve
Dissipative gaskets –Ground monitor.
-Remove adjacentcontrol panel
AGREED RISK MITIGATION PLANS
Specify the details of agreed mitigation plans
Mitigation Plan 1:
Mitigation Plan Description
Mitigation Plan
Owner
Due Date
Root Cause
Ref.
Apply engineering controls to achieve high level of control on static
electricity
Helmy Ismail July 2017 RC01
Mitigation Action Plans:
ID Action Plan Description Action Plan Owner Due Date Status
1 Issue CCR for the proposed changes in the room. Helmy Ismail Oct 2016
2 Install earthing bar in the room Mohamed El Hosary Nov- 2016
3 Avail 2 FM Approved Earthing clamps in the sieving room Amr Younis Jan-2017
4
Install ST ST earthed sheetwith suitable size for operator to
stand on
Amr Younis Jan-2017
5 Get offers for Ground monitor Helmy Ismail Dec-2016
6 Issue PO for ground monitor Helmy Ismail Jan-2017
7 Install Ground Monitor in the Sieving room Helmy Ismail May-2017
8 Replace Sieve gaskets with dissipative gaskets Amr Younis Apr- 2017
9
Review Sieve earthing continuity to comply with EHS ENG Alert
12-002
Amr Younis
Dec-2016
10
Update Sieving operation SOP to include all added controls and
provide training to all operators accordingly
Helmy Ismail June-2017
11
Include dustextraction system in site preventive maintenance
plan
Kirollos Kamel Jan-2017
12
ConductAAR for the completed risk actions and update HAZID
assessmentaccordingly
Ahmed Mohamed
Said
July-2017
6. GlaxoSmithKline - Egypt Appendix 6 to SOP TO 524/10
RISK SITUATION, TARGET AND PROPOSAL (STP) Page 6 of 6
Originating Site: Cairo Risk Identifier. Risk Internal No.:
Date of Issue: 15/9/2016 STP Ref. No.: Version: 01
Mitigation plan comments:
Mitigation Plan 2:
Mitigation Plan Description
Mitigation Plan
Owner
Due Date
Root Cause
Ref.
Assess the design and location of both the existing control
Panel and the dust extraction system
Ahmed Mohamed
Said
Jan-2017 RC02
Mitigation Action Plans:
ID Action Plan Description Action Plan Owner Due Date Status
1 Assess the location ofthe control panel as per area HAC zoning
Ahmed Mohamed
Said
Dec-2016
2
Assess the performance ofthe existing Suction hood with
Versus manufacturing specs.
Kirollos Kamel Nov-2016
3
Assess the current performance ofthe suction hood against
operation requirements
Ahmed Mohamed
Said
Jan-2017
Mitigation plan comments:
MITIGATED INDEX VALUE
Include here all details that support your risk scoring after completing the proposed mitigation plans
Risk Area of Impact Mitigated ConsequenceStatement Mitigated
Consequence
Mitigated Likelihood Statement Mitigated
Likelihood MIV
EHS Severe burn or tissue damage 4 Probability of incident is rare 1 4
Comment on mitigated index value:
MITIGATION PLAN RSOURCES
Specify the details of resources required to execute the agreed mitigation plans
Financial Resources: Value Currency Payment Year
OPEX
Budgeted
40.000 LE 2016 Not budgeted
CAPEX
Budgeted
N/A Not budgeted
Other Resources: Specify details of or reference to non-financial resources needed to complete the agreed mitigation plans
RISK MITIGATION COMPLETION DATE:
Rationale to changes in risk mitigation completion date (if any):
Document History:
Date Version Reason for Revision Ref.
01 First issue N/A