30 years ago, in the ammonia plant where I worked, the sight glass of a high pressure (200 Kg/cm2) ammonia separator leaked during start up. Luckily we managed to shut the plant down safely with no injury to anyone. The root cause was the wrong torquing procedure used. A good article about sight glasses mentions the following:
December 17, 2011
December 14, 2011
Laser scanning - a tool for Management of change and Asset Integrity
The most difficult elements to implement in a PSM program are management of change and asset integrity simply because of the large quantity of data involved and less time available. I was reading an interesting concept of laser scanning in an article in Power magazine. It mentions the following:
"Laser scanning also provides a dimensionally accurate representation of the plant and all its equipment as well as a photographic quality visual representation. The laser scan database can be integrated with a variety of plant design applications to provide comprehensive facility management support".
The concept will be very useful for PHA teams who are analysing changes/modifications as they can virtually "see" the proposed modification. It is also an useful tool for managing your asset integrity as another article mentions.
Read the article on laser scanning in this link
Read the article on Virtual asset integrity management in this link.
"Laser scanning also provides a dimensionally accurate representation of the plant and all its equipment as well as a photographic quality visual representation. The laser scan database can be integrated with a variety of plant design applications to provide comprehensive facility management support".
The concept will be very useful for PHA teams who are analysing changes/modifications as they can virtually "see" the proposed modification. It is also an useful tool for managing your asset integrity as another article mentions.
Read the article on laser scanning in this link
Read the article on Virtual asset integrity management in this link.
December 11, 2011
US Unions briefing on Process Safety
The USW union of the US has briefed the US Congress about health and safety problems in the oil industry. As per a news article,"USW Health and Safety Specialist Kim Nibarger outlined five fatal flaws at the briefing on where the oil industry needs to improve its health and safety record: process safety, mechanical integrity, management of change, incident investigation and control room alarms and instrumentation. “When things go bad in a refinery, they go really bad and people die,” he told the briefing. “Focusing on personal safety—the wearing of hard hats and safety glasses, slips, trips and falls—says nothing about how safe a refinery is for workers and the surrounding community. BP had a low personal injury rate at its refineries, but the 2005 explosion and fire at its Texas City plant showed it failed miserably in terms of process safety. Fifteen people were killed and 170 were injured in the 2005 accident as a result of this failure. “The oil companies are playing Russian roulette with their equipment,” Nibarger said. “They are doing quick, stopgap fixes, like placing clamps on pipes instead of replacing the pipe. They’re extending the time between unit shutdowns when all the equipment is checked. When there is a shutdown they’re not always repairing or replacing critical equipment. When they do repair equipment they’re not bringing it up to current RAGAGEP (Recognized and Generally Accepted Good Engineering Practices) standards.”
If the above sound familiar to you, take a hard look at your PSM program!
Read the full article in this link.
If the above sound familiar to you, take a hard look at your PSM program!
Read the full article in this link.
December 9, 2011
Adding too much chemical causes an incident
A news report mentions an incident where an orange gas cloud leaked from a manufacturing facility for making ferric sulphate. Apparently, too much nitric acid was added to a batch, resulting in a violent reaction that
produced excess amounts of nitrogen dioxide that escaped from the
reactor into the air.Nitrogen dioxide is a reddish brown gas and is highly toxic if inhaled and is
also corrosive.
Ensure that you have proper controls over addition of chemicals, especially if adding an excess of one chemical can trigger something unwanted. Engineering controls are the best to avoid such mishaps. Depending only on an SOP in such situations may cause an an incident to happen.
Read the article in this link.
Ensure that you have proper controls over addition of chemicals, especially if adding an excess of one chemical can trigger something unwanted. Engineering controls are the best to avoid such mishaps. Depending only on an SOP in such situations may cause an an incident to happen.
Read the article in this link.
December 7, 2011
Boiler burst kills 4
A boiler of a dyeing unit burst on Tuesday, killing four persons and injuring 20 others on Tuesday. Inquiries are on to find out the reason for the blast. An official said that the safety valve failed release in time, leading to pressure building up inside the boiler.Read about it in this link.
December 6, 2011
A change in piping material may overlook something else!
A plant decided to change its sulphuric acid piping from Cast Iron to SS. However, they decided to conduct piping design analysis as per code requirement.The analysis found out that design did not adequately consider the
difference in cross-sectional thickness between Cast Iron and SS (Cast iron is very thick
compared to stainless steel). Also, the heat transfer rates of CI and SS differ. The piping expert redesigned the
piping system to account for the thinner cross-section and thermal
expansion properties of stainless steel and thus avoided premature failure.
Read the article in this link.
Read the article in this link.
December 4, 2011
Explosion in sulphuric acid tank
An explosion in a sulphuric acid tank has injured four personnel in Japan. There is the danger of presence of hydrogen in sulphuric acid tanks and when you do hot work be aware of the simple precautions like gas testing etc.
Read about the accident in this link. The Chemical Safety Board had earlier brought out a safety bulletin on the Dangers of Hot work, which is worth reading for every plant operation, maintenance and safety personnel. Read it in this link.
Read about the accident in this link. The Chemical Safety Board had earlier brought out a safety bulletin on the Dangers of Hot work, which is worth reading for every plant operation, maintenance and safety personnel. Read it in this link.
December 2, 2011
Fire in Pharma Plant
A fire in the vacuum dryer area of a pharma plant has reportedly seriously injured three people. As per Company press release, it states "There was a fire incident in a powder processing area at early hours
on Nov 28,2011, at unit 11 which is located at Pydibhimavaram, Srikakulam near
Vizag, A.P. Three persons were injured and they were taken to the
hospital. The powder processing area is isolated from the intermediate
block. There was no impact to the operations as well as to the assets".
Another news report indicates that the fire was caused by an explosion due to high pressure in the vacuum dryer.
Read the news reports in these links
Link 1
Link 2
Link 3
Another news report indicates that the fire was caused by an explosion due to high pressure in the vacuum dryer.
Read the news reports in these links
Link 1
Link 2
Link 3
December 1, 2011
Remembering Bhopal............
Please spend December 2nd/3rd as “Process Safety Day” in your organisation. Educate your personnel on the Bhopal Gas tragedy and its lessons. 27 years ago, on the night on December 2nd/3rd, 1984, on a wintry night in Bhopal, thousands of men, women and children died an excruciating death when MIC leaked from the Union Carbide factory. The survivors and the next generation children born to those exposed to the gas still are suffering from the effects of the gas. Bhopal is an ongoing tragedy and should never be forgotten. The Bhopal gas disaster comprises actually of three disasters - the first was the actual incident, the second was the inadequate compensation received and the third is the ongoing legacy of genetic defects and effects of the hazardous waste that has seeped into the ground water. Every plant operating, maintenance and safety personnel must never forget the lessons of Bhopal. They are still relevant today:
1. Do not cut costs without looking at the effects on process safety
2. Maintain all your layers of defense including asset integrity
3. Continually ensure that competency of personnel operating and maintaining plants are updated and current
4. Be prepared for the worst case scenario.
5. Understand the risks and measures to eliminate / reduce or control them
6. Learn from your past incidents. Those who do not learn are condemned to repeat the incidents.
7. Pay heed to your process safety management system audit reports
As you are aware, this blog is also dedicated to the surviving victims of Bhopal and for my regular subscribers, I appeal to you to buy my book "Practical Process Safety Management", the proceeds from which are donated to the surviving victims of Bhopal.Contact me at bkprism@gmail.com for buying the book.
See a presentation on the Bhopal Gas Tragedy by Vijita S Aggarwal, Associate Professor, University School of Management Studies,GGS Indraprastha University,Delhi, India in this link.
Read my older post comparing the Bhopal and the BP incident of 2005 in this link
Read the then Police Chief’s account of the tragedy in this link.
November 29, 2011
Witness to a catastrophic near miss!
On 29.11.1984, I was working in an ammonia plant when a cylcone hit the place. Management had taken advance action and instructed us to shut off the back end of ammonia plant (the back end of the ammonia plant involves high pressures). We had shut down the back end and were waiting for the cyclone to hit us. The wind speeds were very high and all of us were taking shelter in the control room. A complaint then came in from the another plant that was located within the same complex, that they were experiencing severe ammonia odour. Thinking that the pilot burners of the ammonia derrick supported flare that was provided for emergency venting of the ammonia storage tank was put off by the high winds, I requested operators to go out and check them. Three operators had to go, holding each other tightly,as the wind speed was so high and could blow a man off his feet. After a short while they came back and reported that the flare was missing. I went out to check with another team and we found to our horror that the flare structure had collapsed on the main ammonia vapor line coming from the tank. The derrick structure was weak and could not bear the brunt of the wind speeds, but the main flare gas pipe was in good condition and when the derrick toppled, the main gas pipe prevented it from falling all of a sudden. Instead it fell slowly and came to rest on the ammonia vapor line! The 8" main ammonia vapour line from the tank was dented, but did not leak.
When you conduct your asset integrity program, pay attention to structures. Nowadays, in many plants, painting schedules are taking a back seat, with the net result that corrosion creeps in. Corrosion is a silent killer. It will hit you one day if you don't maintain your assets.
Interestingly, recently I read an article where a complete flare structure repair was done with minimum downtime in a plant.Read the article in this link.
When you conduct your asset integrity program, pay attention to structures. Nowadays, in many plants, painting schedules are taking a back seat, with the net result that corrosion creeps in. Corrosion is a silent killer. It will hit you one day if you don't maintain your assets.
Interestingly, recently I read an article where a complete flare structure repair was done with minimum downtime in a plant.Read the article in this link.
November 25, 2011
Escaping from steam
Many of you will be working with steam. During startups the possibility of water hammer in a steam pipeline has the potential to rupture the line or flange joints. Your SOPs must warn operators about the dangers of water hammer. An article mentions that the best way to escape from a closed space in which a steam leak has been triggered due to water hammer is to escape in the direction in which the steam is leaking through an exit. Read this article in
this link
November 22, 2011
Heat transfer fluids
Paratherm have brought out a good booklet on heat transfer fluids - do's. dont's and best practices. Some of the points brought out are:
"If any hydrocarbon liquid (oil, grease, heat transfer fluid, hydraulic fluid) is allowed to enter porous insulation, it will begin to oxidize, raising the insulation’s internal temperature. If this temperature exceeds the fluid’s autoignition temperature, the fluid is likely to spontaneously combust into a smoldering fire. Thoroughly inspect all insulation for signs of wetness and other damage.Although “hydro” testing is a commonly accepted practice with heat transfer systems,alternatives such as pressure-testing with inert gas or with the heat transfer fluid itself should be considered. Water in a system can cause pump cavitation and corrosion and, if trapped in a “dead leg” and hit by high-temperature oil, can flash to steam and literally blow the pipe or tubing apart. And if the pipe doesn’t burst, the expansion can push a slug of hot oil out the expansion tank’s vent—a serious safety hazard".
Read the complete article in this link.
"If any hydrocarbon liquid (oil, grease, heat transfer fluid, hydraulic fluid) is allowed to enter porous insulation, it will begin to oxidize, raising the insulation’s internal temperature. If this temperature exceeds the fluid’s autoignition temperature, the fluid is likely to spontaneously combust into a smoldering fire. Thoroughly inspect all insulation for signs of wetness and other damage.Although “hydro” testing is a commonly accepted practice with heat transfer systems,alternatives such as pressure-testing with inert gas or with the heat transfer fluid itself should be considered. Water in a system can cause pump cavitation and corrosion and, if trapped in a “dead leg” and hit by high-temperature oil, can flash to steam and literally blow the pipe or tubing apart. And if the pipe doesn’t burst, the expansion can push a slug of hot oil out the expansion tank’s vent—a serious safety hazard".
Read the complete article in this link.
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