About Piper Alpha Platform
The Happening Event Timeline
Cause of the Disaster
Effect of the Disaster
Key Failures
Improvement and Prevention
Conclusion
I. Background about Piper Alpha
II. General Purpose of the platform operation
III. The happening Event Timeline
IV. Cause and Effect of the disaster
V. Key Failures
VI. Improvement and prevention
VII. Conclusion
Piper Alpha was an oil production platform in the North Sea that caught fire in 1988, resulting in the deaths of 167 workers. The platform began oil production in 1976 and was later converted to gas production. On July 6, 1988, a gas leak caused an explosion and massive fire that destroyed the platform within hours. The fire spread due to the platform's design which lacked firewalls between modules and the continued pumping of gas and oil from connected platforms. It was one of the worst offshore oil disasters in history.
On July 6, 1988, an explosion destroyed the Piper Alpha oil platform in the North Sea, killing 167 workers. Piper Alpha was a large fixed platform that produced oil and gas from 24 wells. A series of explosions were caused by failures in the condensate pumps and gas lines. As a result of the disaster, the Cullen Inquiry was established and new safety regulations were implemented for operating in the North Sea, focusing on equipment procedures, personnel training, platform design, and emergency response.
Piper Alpha was an oil production platform located in the North Sea that produced natural gas, LPG, and crude oil. On July 6, 1988, an explosion occurred on the platform due to a leak from a safety valve that was under maintenance but mistakenly connected to a pump that was put into use. This caused a chain reaction of explosions and fire that ultimately destroyed the platform, killing 167 workers. The disaster was caused by poor documentation and separation of paperwork regarding maintenance and safety procedures for pumps and valves. In response, the oil industry implemented new safety measures, permit systems, and formal assessments.
The document provides background information on the Piper Alpha oil production platform disaster that occurred in 1988, killing 167 people. It discusses the platform's management and operations, industrial processes, and identifies multiple causes of the accident. The primary initiating event was an explosion caused by a condensate pump startup during maintenance, which allowed gas to leak and ignite. This led to secondary and tertiary explosions as fires spread and structures collapsed. Root causes included failures in the company's management of safety systems like permit-to-work and a lack of emergency response training and authority. Human errors also contributed through improper maintenance procedures and sign-offs.
Accidental Short Report on Texas City Refinery Explosion 2005Farooq Ahmed Fk
On March 23, 2005, an explosion and fire occurred at the BP Texas City refinery, killing 15 people. The incident was caused when operators overfilled a raffinate splitter tower during startup, causing flammable liquid to overflow and be released uncontrollably from a blowdown stack without a flare to burn off vapors. The released liquid evaporated and formed a large flammable vapor cloud that was ignited by a nearby truck, causing an explosion. A investigation found organizational and safety deficiencies throughout BP contributed to the incident. Warnings signs of problems had been present for years but not addressed by the company.
Piper Alpha was an oil production platform located in the North Sea that exploded and sank on July 6, 1988. The platform began producing oil in 1976 and was processing oil and gas from 24 wells at the time of the disaster. On the night of July 6th, a gas leak caused an explosion that engulfed the platform in fire. Two additional gas lines ruptured, causing massive explosions and spreading the fire across the entire platform. Within hours, the platform completely collapsed and sank into the sea, resulting in the deaths of 167 workers in one of the worst offshore oil disasters in history.
I. Background about Piper Alpha
II. General Purpose of the platform operation
III. The happening Event Timeline
IV. Cause and Effect of the disaster
V. Key Failures
VI. Improvement and prevention
VII. Conclusion
Piper Alpha was an oil production platform in the North Sea that caught fire in 1988, resulting in the deaths of 167 workers. The platform began oil production in 1976 and was later converted to gas production. On July 6, 1988, a gas leak caused an explosion and massive fire that destroyed the platform within hours. The fire spread due to the platform's design which lacked firewalls between modules and the continued pumping of gas and oil from connected platforms. It was one of the worst offshore oil disasters in history.
On July 6, 1988, an explosion destroyed the Piper Alpha oil platform in the North Sea, killing 167 workers. Piper Alpha was a large fixed platform that produced oil and gas from 24 wells. A series of explosions were caused by failures in the condensate pumps and gas lines. As a result of the disaster, the Cullen Inquiry was established and new safety regulations were implemented for operating in the North Sea, focusing on equipment procedures, personnel training, platform design, and emergency response.
Piper Alpha was an oil production platform located in the North Sea that produced natural gas, LPG, and crude oil. On July 6, 1988, an explosion occurred on the platform due to a leak from a safety valve that was under maintenance but mistakenly connected to a pump that was put into use. This caused a chain reaction of explosions and fire that ultimately destroyed the platform, killing 167 workers. The disaster was caused by poor documentation and separation of paperwork regarding maintenance and safety procedures for pumps and valves. In response, the oil industry implemented new safety measures, permit systems, and formal assessments.
The document provides background information on the Piper Alpha oil production platform disaster that occurred in 1988, killing 167 people. It discusses the platform's management and operations, industrial processes, and identifies multiple causes of the accident. The primary initiating event was an explosion caused by a condensate pump startup during maintenance, which allowed gas to leak and ignite. This led to secondary and tertiary explosions as fires spread and structures collapsed. Root causes included failures in the company's management of safety systems like permit-to-work and a lack of emergency response training and authority. Human errors also contributed through improper maintenance procedures and sign-offs.
Accidental Short Report on Texas City Refinery Explosion 2005Farooq Ahmed Fk
On March 23, 2005, an explosion and fire occurred at the BP Texas City refinery, killing 15 people. The incident was caused when operators overfilled a raffinate splitter tower during startup, causing flammable liquid to overflow and be released uncontrollably from a blowdown stack without a flare to burn off vapors. The released liquid evaporated and formed a large flammable vapor cloud that was ignited by a nearby truck, causing an explosion. A investigation found organizational and safety deficiencies throughout BP contributed to the incident. Warnings signs of problems had been present for years but not addressed by the company.
Piper Alpha was an oil production platform located in the North Sea that exploded and sank on July 6, 1988. The platform began producing oil in 1976 and was processing oil and gas from 24 wells at the time of the disaster. On the night of July 6th, a gas leak caused an explosion that engulfed the platform in fire. Two additional gas lines ruptured, causing massive explosions and spreading the fire across the entire platform. Within hours, the platform completely collapsed and sank into the sea, resulting in the deaths of 167 workers in one of the worst offshore oil disasters in history.
An explosion occurred at a British Petroleum oil refinery in Texas in 2005, killing 15 people and injuring 170. The explosion was caused by a buildup of hydrocarbon vapors from a malfunctioning isomerization process unit. An investigation found that safety systems had deficiencies, procedures were not followed, and organizational weaknesses like inadequate training and a culture of noncompliance contributed to the accident. The explosion resulted in OSHA fines against BP and lawsuits from victims' families.
On November 19, 1984, a series of explosions occurred at a liquefied petroleum gas (LPG) storage and distribution facility in San Juanico, Mexico City, operated by Pemex, Mexico's state-owned petroleum company. An 8-inch feed pipe ruptured, releasing a gas cloud that ignited and caused the first explosion. This was followed by 18 additional explosions over the next 1.5 hours as fires engulfed the facility's LPG storage tanks. The explosions and fires killed 500-600 people, injured 5000-7000, and left 10,000-60,000 homeless. Lessons learned included the need for proper plant layout and maintenance, adequate safety systems, and housing located further
here we have discuss about Flixborough disaster what are its causes, consequences, how to prevent such kinds of disasters.
it is my college presentation, I have uploaded this document so that it may help other students thank you :)
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/
The Flixborough disaster was the largest peacetime explosion in UK history, occurring on June 1st, 1974 at a chemical plant in Flixborough, UK. The explosion killed 28 workers and caused widespread property damage within a 6 mile radius. The public inquiry into the cause determined that the immediate cause was the rupture of a poorly designed 20-inch bypass pipe between two reactors. However, subsequent analysis suggested that the more likely cause was the presence of water in one of the reactors during startup when the stirrer was not operating, allowing an unstable water-cyclohexane azeotrope to form and violently erupt, causing the bypass pipe to fail without high pressure. The disaster highlighted the importance of considering all
Improper management of highly hazardous chemicals, including toxic, reactive or flammable liquids, can cause accidental releases and emergency responses. OSHA’s Process Safety Management of Highly Hazardous Chemicals standard (29 CFR 1910.119) regulates the management of highly hazardous chemicals. Violations can carry fines of up to $126,000. Do you have a PSM program in place?
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.
The document summarizes the Deepwater Horizon oil spill, including causes and timeline of events. It describes:
1) The spill occurred when the Deepwater Horizon oil rig exploded on April 20, 2010, killing 11 crew and spilling over 4 million barrels of oil.
2) A series of decisions ignored warnings and best practices, compromising the well design and cementing job. This included only using 6 centralizers instead of the recommended minimum of 21.
3) Pressure tests before temporarily abandoning the well showed warning signs of integrity issues but these were ignored. The rig then exploded as hydrocarbon gases rose up the well.
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 discusses health and safety in the oil and gas industry. It covers several topics:
- Management systems for health and safety with planning, performance, assessment, and improvement.
- Personal protective equipment (PPE) including responsibilities, hazard assessment, protective clothing, and training.
- Electrical safety including responsibilities, hazards, flash hazard analysis, and qualifications.
- Control of hazardous energy sources including lockout procedures.
- Emergency contingency planning including different plans for shelter in place, administrative closings, and occupant emergencies.
The Deepwater Horizon oil rig exploded in the Gulf of Mexico 1,500 meters below the surface and 66 km off the coast of Louisiana, killing 11 workers. Over the next 36 hours, the rig burned and eventually sank, leaving a damaged wellhead that was leaking oil into the Gulf. For months, oil gushed from the wellhead at an estimated rate of up to 40,000 barrels per day, spreading across 1,500 square km of the Gulf and reaching the coasts of Louisiana, Florida, and elsewhere in the Gulf region due to ocean currents. The well was finally capped on July 15, over 80 days after the initial explosion.
This document outlines the scope of work for an EPC contract for a Central Area Field Complex Project in Algeria. It includes 180 pages describing the project overview, general contracting requirements, work descriptions, design and engineering scope, HSE requirements, materials procurement, construction, commissioning, and special notes. The contractor will be responsible for engineering, procurement, construction, and commissioning of the facilities, and must comply with Algerian regulations and international HSE standards.
Chevron Refinery in Richmond the largest oil refinery in Northern California. This is an overview of refinery fire in 2012, including event timeline leading to disaster and the aftermath.
The document provides information about various processes at an oil refinery. It discusses desalting crude oil to remove salt. It then describes the main distillation units like atmospheric distillation and vacuum distillation that separate crude oil into different hydrocarbon fractions. Other process units mentioned include hydrotreating to remove contaminants, catalytic reforming to increase octane of naphtha, fluid catalytic cracking to convert heavy fractions to lighter products, and hydrocracking to break larger molecules.
The document discusses the key elements of Process Safety Management (PSM), a regulation promulgated by OSHA to prevent chemical disasters like the 1984 Bhopal disaster. It outlines the 14 elements of PSM, which include process hazards analysis, mechanical integrity, compliance audits, and emergency response. For each element, it provides the purpose, requirements, and tips for real-world implementation to help companies effectively achieve the safety goals of the PSM standard.
Risk Assessment At Tank- Truck Unloading Section Of LPG Bottling Plant I Gaur...Gaurav Singh Rajput
The document summarizes a risk assessment conducted at the LPG tank truck unloading section of an LPG bottling plant. The objectives were to identify hazards, assess risks through fault tree analysis and event tree analysis, and estimate individual and societal risk. Methodology included HAZOP study to identify hazards, consequence analysis using PHAST Risk software, and calculation of individual risk using thermal radiation exposure models. Key findings were an individual risk of 1x10-4 per year and societal risk within acceptable limits defined by the F-N curve. Recommendations to reduce risk included following standard operating procedures and improving safety systems.
The document summarizes information about the 2010 Deepwater Horizon oil spill in the Gulf of Mexico. It provides background on the location and stakeholders involved. It then describes the causes of the spill, including failures in safety systems and issues with cementing and pressure testing. It discusses impacts on fisheries, marine species, seabirds, invertebrates, corals and ecosystems. Finally, it outlines remedial measures taken, including containment booms, dispersants, controlled burns, and skimming operations.
Zlatko Bikic has over 35 years of experience in commissioning and operations in the oil and gas industry. He has worked on numerous projects around the world, holding roles such as Commissioning Process Supervisor, Pre-Commissioning Operation Supervisor, and Shift Superintendent. Some of the companies he has worked for include Tecnimont, Saipem, and Snamprogetti on projects in Saudi Arabia, UAE, Qatar, Iran, Libya, and Croatia.
The document discusses several engineering disasters including the Space Shuttle Challenger explosion, Three Mile Island nuclear accident, Bhopal gas tragedy, and Uphaar Cinema fire. It summarizes the key events and identifies technical failures, lack of safety protocols, cost-cutting measures, and human errors as contributing factors. The document emphasizes engineers' responsibility to consider safety and protect public welfare.
An explosion occurred at a British Petroleum oil refinery in Texas in 2005, killing 15 people and injuring 170. The explosion was caused by a buildup of hydrocarbon vapors from a malfunctioning isomerization process unit. An investigation found that safety systems had deficiencies, procedures were not followed, and organizational weaknesses like inadequate training and a culture of noncompliance contributed to the accident. The explosion resulted in OSHA fines against BP and lawsuits from victims' families.
On November 19, 1984, a series of explosions occurred at a liquefied petroleum gas (LPG) storage and distribution facility in San Juanico, Mexico City, operated by Pemex, Mexico's state-owned petroleum company. An 8-inch feed pipe ruptured, releasing a gas cloud that ignited and caused the first explosion. This was followed by 18 additional explosions over the next 1.5 hours as fires engulfed the facility's LPG storage tanks. The explosions and fires killed 500-600 people, injured 5000-7000, and left 10,000-60,000 homeless. Lessons learned included the need for proper plant layout and maintenance, adequate safety systems, and housing located further
here we have discuss about Flixborough disaster what are its causes, consequences, how to prevent such kinds of disasters.
it is my college presentation, I have uploaded this document so that it may help other students thank you :)
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/
The Flixborough disaster was the largest peacetime explosion in UK history, occurring on June 1st, 1974 at a chemical plant in Flixborough, UK. The explosion killed 28 workers and caused widespread property damage within a 6 mile radius. The public inquiry into the cause determined that the immediate cause was the rupture of a poorly designed 20-inch bypass pipe between two reactors. However, subsequent analysis suggested that the more likely cause was the presence of water in one of the reactors during startup when the stirrer was not operating, allowing an unstable water-cyclohexane azeotrope to form and violently erupt, causing the bypass pipe to fail without high pressure. The disaster highlighted the importance of considering all
Improper management of highly hazardous chemicals, including toxic, reactive or flammable liquids, can cause accidental releases and emergency responses. OSHA’s Process Safety Management of Highly Hazardous Chemicals standard (29 CFR 1910.119) regulates the management of highly hazardous chemicals. Violations can carry fines of up to $126,000. Do you have a PSM program in place?
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.
The document summarizes the Deepwater Horizon oil spill, including causes and timeline of events. It describes:
1) The spill occurred when the Deepwater Horizon oil rig exploded on April 20, 2010, killing 11 crew and spilling over 4 million barrels of oil.
2) A series of decisions ignored warnings and best practices, compromising the well design and cementing job. This included only using 6 centralizers instead of the recommended minimum of 21.
3) Pressure tests before temporarily abandoning the well showed warning signs of integrity issues but these were ignored. The rig then exploded as hydrocarbon gases rose up the well.
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 discusses health and safety in the oil and gas industry. It covers several topics:
- Management systems for health and safety with planning, performance, assessment, and improvement.
- Personal protective equipment (PPE) including responsibilities, hazard assessment, protective clothing, and training.
- Electrical safety including responsibilities, hazards, flash hazard analysis, and qualifications.
- Control of hazardous energy sources including lockout procedures.
- Emergency contingency planning including different plans for shelter in place, administrative closings, and occupant emergencies.
The Deepwater Horizon oil rig exploded in the Gulf of Mexico 1,500 meters below the surface and 66 km off the coast of Louisiana, killing 11 workers. Over the next 36 hours, the rig burned and eventually sank, leaving a damaged wellhead that was leaking oil into the Gulf. For months, oil gushed from the wellhead at an estimated rate of up to 40,000 barrels per day, spreading across 1,500 square km of the Gulf and reaching the coasts of Louisiana, Florida, and elsewhere in the Gulf region due to ocean currents. The well was finally capped on July 15, over 80 days after the initial explosion.
This document outlines the scope of work for an EPC contract for a Central Area Field Complex Project in Algeria. It includes 180 pages describing the project overview, general contracting requirements, work descriptions, design and engineering scope, HSE requirements, materials procurement, construction, commissioning, and special notes. The contractor will be responsible for engineering, procurement, construction, and commissioning of the facilities, and must comply with Algerian regulations and international HSE standards.
Chevron Refinery in Richmond the largest oil refinery in Northern California. This is an overview of refinery fire in 2012, including event timeline leading to disaster and the aftermath.
The document provides information about various processes at an oil refinery. It discusses desalting crude oil to remove salt. It then describes the main distillation units like atmospheric distillation and vacuum distillation that separate crude oil into different hydrocarbon fractions. Other process units mentioned include hydrotreating to remove contaminants, catalytic reforming to increase octane of naphtha, fluid catalytic cracking to convert heavy fractions to lighter products, and hydrocracking to break larger molecules.
The document discusses the key elements of Process Safety Management (PSM), a regulation promulgated by OSHA to prevent chemical disasters like the 1984 Bhopal disaster. It outlines the 14 elements of PSM, which include process hazards analysis, mechanical integrity, compliance audits, and emergency response. For each element, it provides the purpose, requirements, and tips for real-world implementation to help companies effectively achieve the safety goals of the PSM standard.
Risk Assessment At Tank- Truck Unloading Section Of LPG Bottling Plant I Gaur...Gaurav Singh Rajput
The document summarizes a risk assessment conducted at the LPG tank truck unloading section of an LPG bottling plant. The objectives were to identify hazards, assess risks through fault tree analysis and event tree analysis, and estimate individual and societal risk. Methodology included HAZOP study to identify hazards, consequence analysis using PHAST Risk software, and calculation of individual risk using thermal radiation exposure models. Key findings were an individual risk of 1x10-4 per year and societal risk within acceptable limits defined by the F-N curve. Recommendations to reduce risk included following standard operating procedures and improving safety systems.
The document summarizes information about the 2010 Deepwater Horizon oil spill in the Gulf of Mexico. It provides background on the location and stakeholders involved. It then describes the causes of the spill, including failures in safety systems and issues with cementing and pressure testing. It discusses impacts on fisheries, marine species, seabirds, invertebrates, corals and ecosystems. Finally, it outlines remedial measures taken, including containment booms, dispersants, controlled burns, and skimming operations.
Zlatko Bikic has over 35 years of experience in commissioning and operations in the oil and gas industry. He has worked on numerous projects around the world, holding roles such as Commissioning Process Supervisor, Pre-Commissioning Operation Supervisor, and Shift Superintendent. Some of the companies he has worked for include Tecnimont, Saipem, and Snamprogetti on projects in Saudi Arabia, UAE, Qatar, Iran, Libya, and Croatia.
The document discusses several engineering disasters including the Space Shuttle Challenger explosion, Three Mile Island nuclear accident, Bhopal gas tragedy, and Uphaar Cinema fire. It summarizes the key events and identifies technical failures, lack of safety protocols, cost-cutting measures, and human errors as contributing factors. The document emphasizes engineers' responsibility to consider safety and protect public welfare.
Three Mile Island Unit 2 experienced a partial meltdown in 1979 due to equipment failures and human errors. About half of the reactor core melted during the accident. The reactor is now permanently shut down, defueled, and in monitored storage. The accident resulted in major changes to nuclear safety regulations, including improved emergency response, operator training, and oversight of plant management.
Air France Flight 4590 An Accident Investigation ReportMartha Brown
Air France Flight 4590 crashed during takeoff from Paris Charles de Gaulle Airport on July 25, 2000, killing all 109 people on board. The crash was caused by the disintegration of a tire on takeoff, which sent debris into the left wing fuel tank and engines. This caused a fire and loss of thrust from both engines on the left side. The crew was unable to regain control and the plane crashed. The accident report found fault with Continental Airlines for the loose debris on the runway, but human factors like crew resource management and lack of dual engine failure procedures also contributed to the chain of events leading to the crash.
Herman Waminan has over 29 years of experience as a gas turbine technician and aircraft maintenance engineer. He currently works as a gas turbine technician for Oil Search, where he performs maintenance on gas turbine compressor and generator sets. Previously, he worked for 13 years in the mining and oil & gas industry and 16 years in the aviation industry, gaining experience working with various gas turbine and piston engines. He holds qualifications in aircraft maintenance engineering and secondary education from Papua New Guinea and Australia.
Flight 236 from Toronto to Lisbon lost all engine power over the Atlantic Ocean due to a fuel leak caused by improper maintenance. The pilots, Captain Robert Piché and First Officer Dirk de Jager, glided the plane for over 100 km and landed safely in the Azores, saving all 306 people on board. An investigation found that a wrongly installed part during maintenance caused a fuel line to rupture. While pilot error was also cited, the pilots were hailed as heroes for their emergency landing without power.
The document summarizes several major industrial accidents that occurred between 1974 and 2009, including fires and explosions at oil and chemical plants. It then focuses on describing a major fire that took place at an oil terminal in Jaipur, India in 2009. The fire resulted in 11 fatalities and damage estimated at $60 million. An investigation committee analyzed the causes and contributing factors, and made over 100 recommendations to improve safety at oil installations. Many of the recommendations focused on engineering and operational procedures to prevent similar accidents from occurring in the future.
This document contains the resume and work history of Mohamed Moustafa, an Egyptian marine engineer. It lists his contact information and over 15 years of experience working in engine rooms on various oil tankers and cargo ships in roles including 3rd and 4th Engineer. It details his responsibilities maintaining engines, generators, pumps, boilers and other machinery. It also lists his education and qualifications as a marine engineer as well as safety training and certificates.
Piper Alpha was an oil production platform in the North Sea that exploded on July 6, 1988, killing 165 workers. The platform was located 177km off the coast of Scotland and was producing 30,000 tons of crude oil per day at its maximum capacity. Poor safety practices and a lack of communication between shifts contributed to the disaster. Key issues included an ineffective work permit system, unsafe machinery placement, and no emergency response plan. The explosion was likely caused by gas leaks and improper hot work. It was one of the worst offshore oil disasters in history and highlighted the importance of safety protocols and communication in the oil industry.
The document provides safety instructions and information for a ship visit. It outlines what to do in case of emergencies, safety gear requirements, smoking areas, and includes a brief ship history. A tour of the vessel will be given and closed toe shoes are required. The muster point in case of an emergency in the poop deck area is now at the lifeboats on Deck D, port side.
The aim of this module is to introduce delegates to the specific safety issues and regimes relevant to offshore installations.
Identify the generic hazards which are specific to offshore oil and gas installations, potential risks associated with those hazards, and how controls are put in place to eliminate or reduce risks.
Identify key offshore related safety regulations and explain the basic safety management concepts.
The document describes upgrades made to the control systems for two gas turbines and four centrifugal compressors at DCP Midstream's Goldsmith gas processing plant. The original OEM controls were replaced with new redundant controls from Tarco to increase reliability, efficiency, and simplify operation. The project included replacing turbine fuel controls, compressor anti-surge controls, installing a new control building, fire/gas panel, control valves, instrumentation, and integrating the new controls with the DCS. The upgrades improved plant availability, reliability, and reduced downtime to 10 days for the project commissioning.
This document outlines testing requirements for the construction and classification of a new ship. It lists over 15 items that must be tested, including the hull, piping systems, machinery like pumps and engines, electrical systems, and safety equipment. Tests include non-destructive testing of welds, pressure testing of pipes and tanks, performance testing of steering, propulsion, and auxiliary systems, and verifying alarms and safety features. The goal is to ensure that all key ship systems and structures meet classification standards before the vessel is approved and put into service.
This document outlines the fire drill roles and responsibilities for crew members aboard a ship. It assigns the following roles:
1) Captain to oversee all operations and communication from the bridge.
2) Emergency response teams led by the Chief Mate, Chief Engineer, Cook, and 2nd Mate who will coordinate firefighting, engine support, first aid, and boundary cooling efforts.
3) All other crew are assigned to support roles to assist the emergency teams as needed by closing openings, isolating systems, and setting up equipment under the direction of their team leaders.
The document provides details on fire prevention, detection, and fighting procedures as well as the specific duties of each role in responding to a reported fire
1. The document outlines various safety initiatives and trainings undertaken at a facility, including providing extra large hand guards, a new face shield with helmets, and zebra crossings with pedestrian walkways.
2. Trainings provided included first aid training, fall arrest system training, fire hydrant demonstrations, and training on using carbolic acid as a snake repellent.
3. Safety improvements implemented were a 4 wheel stopper system, hot surface enclosures, anti-skid slopes, spill kit provisioning, and chemical suit provisioning. PPE compliance was also emphasized.
Six accidents involving significant radiation overdoses occurred between 1985-1987 with the Therac-25 radiation therapy machine, resulting in patient deaths. An investigation found a race condition bug in the software that allowed this to happen. The Therac-25 was recalled in 1987 due to this software error that caused harm. Other major failures discussed include a 1990 AT&T long-distance system crash, a 1991 Patriot missile failure to intercept an Iraqi Scud, and the 1996 explosion of the Ariane 5 rocket shortly after launch.
Enabling Reusable and Adaptive Modeling,Provisioning & Execution of BPEL Proc...Ahmad El Tawil
This document proposes an architecture for enabling reusable and adaptive modeling, provisioning, and execution of BPEL processes. The architecture supports collaborative, dynamic, and complex systems through reusable process fragments and abstract activities that can be flexibly modeled and executed. It consists of a modeling environment to create and manage process models using fragments, and a runtime environment containing an execution engine, integration layer, and persistence layer to instantiate and execute processes by injecting fragments at runtime. The architecture was evaluated through a use case of modeling and executing payment processes across different transportation systems.
MapReduce is a programming model and implementation for processing large datasets in a distributed environment. It allows users to write map and reduce functions to process key-value pairs. The MapReduce library handles parallelization across clusters, automatic parallelization, fault-tolerance through task replication, and load balancing. It was designed at Google to simplify distributed computations on massive amounts of data and aggregates the results across clusters.
Map reduce advantages over parallel databases Ahmad El Tawil
MapReduce has several advantages over parallel databases for processing large datasets:
1) MapReduce can handle heterogeneous systems with different storage systems more easily than parallel databases which require data copying and analysis.
2) Complex functions are more straightforward to express in MapReduce's simple map and reduce model compared to SQL in parallel databases which can require complicated user defined functions.
3) MapReduce provides better fault tolerance than parallel databases by using techniques like batching, sorting, grouping and smart task scheduling during data transfers between mapping and reducing tasks.
This document provides a risk assessment report on cloud computing. It begins with an abstract discussing how cloud computing has increased risks that consumers should be aware of. It then presents an introduction on cloud computing and the need for risk assessment. Several existing risk assessment approaches are studied. The discussion section analyzes previous risk assessment methods. It finds that while approaches assess risks for consumers, a complete qualitative or quantitative risk assessment method is still needed. The conclusion is that trust between consumers and providers requires a structured risk assessment approach that covers all domains.
Introduction
Survey Risk Assessment for Cloud Computing
Assessing the Security Risks of Cloud Computing
Security and Privacy Challenges in Cloud Computing
Conclusion
This document describes a fruit detection technique using morphological image processing. It outlines image acquisition by collecting fruit sample images in JPEG format. Image preprocessing steps like enhancement and noise removal are applied. Color and texture features are then extracted using color space conversion and Canny edge detection. Image segmentation is performed using a clustering algorithm. Morphological dilation is applied to segmented images to count fruit objects. The results show this technique can automatically count and distinguish fruits, providing a low-cost alternative to manual quality inspection.
Cloud computing risk assesment presentationAhmad El Tawil
This document discusses risk assessment for cloud computing. It outlines the steps in risk assessment, which include threat identification, vulnerability identification, risk determination, and control recommendation. It also discusses assessing the security risks of cloud computing, including evaluating data location, recovery, viability, and support in reducing risk. Finally, it covers security and privacy challenges in cloud computing such as authentication, access control, secure service management, and privacy/data protection.
The Bhopal Disaster occurred in 1984 at a Union Carbide plant in Bhopal, India. Several gas leaks had occurred at the plant in previous years, exposing workers to toxic gases. On the night of December 2, 1984, a major leak released 30-45 tons of toxic methyl isocyanate gas into the air, impacting 500,000 to 600,000 people with numerous health issues. The gas leak caused immediate effects like coughing, eye irritation, and difficulty breathing. There were also arguments that negligence and lack of safety precautions by the plant owners contributed to the massive toxic gas release.
The document proposes algorithms to securely and efficiently apply mobile ad hoc networks (MANETs) using identity-based cryptography. It aims to address problems with the extreme vulnerability of military MANETs to foreign attacks by maintaining secrecy, confidentiality, and functionality even if nodes are captured. The key algorithms involve using large keys up to 65536 bits, designating node and main station roles, and refreshing keys through a public key generator that periodically generates new prime parameters, especially when nodes are compromised.
Bayesian networks are graphical models that represent conditional independence relationships between variables. A Bayesian network consists of nodes representing variables, and directed edges representing conditional dependencies. It encodes a joint probability distribution over all the variables. Bayesian networks allow efficient inference and can represent incomplete data. They are useful for modeling causal relationships and combining domain knowledge with data.
The document discusses authentication, authorization, and accounting (AAA) and provides instructions for configuring AAA on Cisco routers. It begins with an introduction to the three A's of AAA - authentication, authorization, and accounting. It then covers identifying each component and implementing authentication using local services or external servers like TACACS+ and RADIUS. The document also discusses authenticating router access, configuring AAA on Cisco routers including enabling AAA globally and setting authentication lists, and troubleshooting AAA using debug commands.
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A workshop hosted by the South African Journal of Science aimed at postgraduate students and early career researchers with little or no experience in writing and publishing journal articles.
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The event will cover the following::
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আমাদের সবার জন্য খুব খুব গুরুত্বপূর্ণ একটি বই ..বিসিএস, ব্যাংক, ইউনিভার্সিটি ভর্তি ও যে কোন প্রতিযোগিতা মূলক পরীক্ষার জন্য এর খুব ইম্পরট্যান্ট একটি বিষয় ...তাছাড়া বাংলাদেশের সাম্প্রতিক যে কোন ডাটা বা তথ্য এই বইতে পাবেন ...
তাই একজন নাগরিক হিসাবে এই তথ্য গুলো আপনার জানা প্রয়োজন ...।
বিসিএস ও ব্যাংক এর লিখিত পরীক্ষা ...+এছাড়া মাধ্যমিক ও উচ্চমাধ্যমিকের স্টুডেন্টদের জন্য অনেক কাজে আসবে ...
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2. Outline
About Piper Alpha Platform
The Happening Event Timeline
Cause of the Disaster
Effect of the Disaster
Key Failures
Improvement and Prevention
Conclusion
2
3. About Piper Alpha (1/5)
It was discovered in 1973 by Occidental
Petroleum (Caledonia)
In 1975 Piper Alpha Oil Rig was constructed
On July 6th 1988, an explosion of the
Piper Alpha platform
3
4. About Piper Alpha (2/5)
located in:
British sector
North Sea oil field
120 miles Aberdeen
Scotland
4
5. About Piper Alpha (3/5)
In 1976 platform started
production of oil.
In 1978 Piper Alpha was
modified to process and
export the natural gas to
comply with UK gas
conservation
requirements
5
7. About Piper Alpha (5/5)
The Flotta oil terminal in the Orkney Islands will
receive and process oil in these fields.
MCP-01 compression platform
226 workmen
It is the major Northern Sea Oil and Gas for
drilling and production that time
Tartan, Claymore, and MCP-01 platfor
7
8. The happening Event Timeline
(1/6)
12 noon - 6:00 PM:
Pump A Failed
Removed safety valve
Maintenance
Replaced by blind flange
Permit that the Pump A wont be working till 6:pm
8
9. The happening Event Timeline
(2/6)
9:45 PM - 10:00 PM:
Pump B fails
Pump A permit
Pump A activated
Gas leak
Explosion
9
10. The happening Event Timeline
(3/6)
10:04 PM:
Evacuation started
Emergency shutdown activated
Firefighting system inaccessible since it is in the
control room
Gathered on the deck
10
11. The happening Event Timeline
(4/6)
10:20 PM:
Tartan and Claymore platforms oil pipeline
connected to Piper Alpha supplied more oil to the
fire
Tartan and Claymore platforms gas pipeline
connected to Piper Alpha bursts and leaked gas
Causing Explosion
11
12. The happening Event Timeline
(5/6)
10:30 PM:
Tharos attempted to assist Piper Alpha
Burst of MCP-01
12
13. The happening Event Timeline
(6/6)
11:20 PM:
Final gas pipeline burst
Block were platform members gathered falls into the
sea
Rest of the platform continued falling
13
14. Cause of the disaster
Safety valve on Pump A was replaced by blind
flange for maintenance
Crew members reactivated Pump A
Leaking
Explosions
Emergency Shutdown system failed
Fire intensified
Helicopters couldn’t help
14
15. Effect of the disaster
165 workmen dead (out of 226)
2 men from the rescue boat
US$ 3.4 billion cost in property damage
100 kg of hydrocarbons loss
61 survivor
Bad injuries
Loss body parts
15
17. Design Failures (1/4)
Firewalls between modules not upgraded to blast
proof tilesː
The fire barriers (tiles) between modules were not
upgraded
When the initial explosion occurred in module C, the
tiles acted as shrapnel and caused damage to
modules B and D
17
18. Design Failures (2/4)
Control room adjacent to gas compression
moduleː
Adjacent to module C without proper shielding
Failure in module C cause damage to the control
room
18
19. Design Failures (3/4)
Primary supply lines from other oil rigs permitted
backflowː
Main supply lines on Piper Alpha failed
Piper Alpha could not stop the flow itself
Supply lines from the Tartan and Claymore
platforms fed Piper Alpha's fire
19
20. Design Failures (4/4)
Tharos rescue vessel design flawsː
Evacuation gangwayː
Couldn’t extended enough to rescue all personnel
Fire pump issuesː
The pumps became flooded, needed 10 minutes to restart
Fire pumps too powerful for personnelː
Too powerful to use while personnel on board
20
21. Management Failures (1/2)
Normal operation during major construction,
maintenance, and upgradesː
The safety valve maintenance wasn’t finished, and
they didn’t noticed the blind flange plate
21
22. Management Failures (2/2)
Oil feeds from Tartan and Claymore weren’t
shut off until too lateː
Supervisors
noticed the fire
didn’t know the damage
Didn’t know if they have the authority to shut down
production on their platforms
22
23. Procedural Failures (1/3)
Engineer neglected to inform on-duty
custodian of Pump A’s conditionː
Custodian wasn’t informed that the safety valve had
been removed from Pump A
23
24. Procedural Failures (2/3)
Evacuation protocols broke downː
The radio and control room were not functional
Personnel were alarmed
24
25. Procedural Failures (3/3)
Firefighting system was set to manualː
Manual activation
Inaccessible
No way to fight the fire
25
26. Improvement and Prevention
Safety training
Emergency response training
How to respond to emergencies
Active and passive fire protection systems
Secondary escape equipment’s
Provide annual safety training
26
27. Conclusion (1/2)
Most tragic gas and oil accident
Errors and questionable decisions
Initial leak was the result of poor maintenance
procedures
Improper structural design
27
28. Conclusion (2/2)
Companies’ management should not aim to
save more money
Understaffed facilities
Less experienced operators
Companies’ responsibilities to subject their
employees on
Safety training
Emergency response training
28