learning from experience revisited

1
Process Safety Learning from experience revisited I n March/April 2008, this column was about ‘‘Learning from Experience’’. 1 Six years later, recent experience makes this topic worth revisiting. I have been using a US Chemical Safety Board (CSB) video of a fire at a Praxair gas distribution facility in St. Louis, MO 2005 2 in process safety courses. The audience is generally not involved handling flammable, compressed gas cylinders. I ask students, before showing the video, to think about why we are showing it, and what lessons from this incident apply to their facilities. There is a lot to learn from this incident for any facility. To briefly summarize the incident, June 24, 2005 was a hot day, up to 97 8F, in St. Louis. About 3 PM, a fire was seen in the ‘‘empty’’ propylene cylinder (unlikely to really be com- pletely empty) storage area. The fire is believed to have been caused by the opening of a relief valve on a propylene cylinder due to the vapor pressure of propylene, perhaps at a pressure below its set point. The vapor pressure of pro- pylene equals the 390 psig relief valve set pres- sure at 149 8F. The fire rapidly escalated, and within minutes involved the entire facility. Employees immediately evacuated and called for assistance from the St. Louis fire depart- ment. The fire department evacuated people from a 5 block area surrounding the facility and focused on preventing spread of the fire. The rocketing cylinders made it too dangerous to approach the fire too closely. A number of lessons from this incident apply to almost any process facility. A fire can escalate very quickly, and rapid action is necessary to protect people who work in the facility. The CSB reports that within 4 minutes of the fire first being observed, most of the facility was involved and cylinders were already observed to be exploding frequently! The Praxair employees did the right thing – they evacuated the plant and called for help. The fire department also did the right thing and focused on protecting people from the effects of the fire. This is in contrast to other incidents where employees tried to respond to an incident and stop a release of flam- mable or reactive material, and were killed in an explosion when their efforts failed. 3 Although it may have opened prematurely, the relief valve likely did what it was sup- posed to do – it prevented rupture of the cylinder to which it was attached. The fire resulted from ignition of the discharge from the relief valve. Emergency relief is a system, including understanding what happens to the material released. This may be difficult to manage for a portable cylinder, but in a fixed process facility you have control over what happens to a relief device discharge. Relief valve performance can deteriorate fol- lowing activation. A robust process with a larger difference between normal operating pressure (as well as foreseeable deviations) and the relief valve set pressure is inherently safer. The CSB video narration indicates that the relief valve on the cylinder could have been set at a higher pressure – the cylinders were strong enough to withstand greater pressure. This may be true for the cylinders involved in the incident, but perhaps not for all propylene cylinders. This doesn’t only apply to pres- sure, but to any safety-critical process para- meter – you don’t want normal operating conditions to be too close to a hazardous condition. There is a ‘‘learning from experience’’ lesson in this incident. The CSB report identifies two similar incidents that had occurred at other places, in 1997 in Phoenix, AZ, and in 2003 in Tulsa, OK, both involving propylene cylinders and hot weather. About a month after the St. Louis incident, another Praxair facility in Fresno, CA had a similar incident. When reading incident reports and viewing safety videos such as those from the CSB, one of your challenges is to understand how you can apply the lessons to your process, even though the technology may be very different from that involved in the incident. 1 Hendershot, D. C. Learning from Experience. J. Chem. Health Safety, 2008, 15 (2 (March/ April), 34–35. 2 http://www.csb.gov/praxair-flammable-gas- cylinder-fire/ (accessed 8.3.14). 3 For example, the CSB report on the April 2004 explosion at a PVC plant in Illiopolis, IL (http:// www.csb.gov/formosa-plastics-vinyl-chloride- explosion/), and the EPA/OSHA report on an explosion in a blender in Lodi, NJ in April 1995 (http://www.epa.gov/oem/docs/chem/ napp.pdf). 1871-5532/$36.00 ß Division of Chemical Health and Safety of the American Chemical Society 35 http://dx.doi.org/10.1016/j.jchas.2014.03.004 Elsevier Inc. All rights reserved.

Upload: dennis-c

Post on 30-Dec-2016

219 views

Category:

Documents


1 download

TRANSCRIPT

Process Safety

1871-5532/$36.00

http://dx.doi.org/10.1016/j.jchas.2

Learning from exp

erience revisited

I n March/April 2008, this column wasabout ‘‘Learning from Experience’’.1 Sixyears later, recent experience makes this

topic worth revisiting. I have been using a USChemical Safety Board (CSB) video of a fire at aPraxair gas distribution facility in St. Louis, MO20052 in process safety courses. The audience isgenerally not involved handling flammable,compressed gas cylinders. I ask students, beforeshowing the video, to think about why we areshowing it, and what lessons from this incidentapply to their facilities. There is a lot to learnfrom this incident for any facility.

To briefly summarize the incident, June 24,2005 was a hot day, up to 97 8F, in St. Louis.About 3 PM, a fire was seen in the ‘‘empty’’propylene cylinder (unlikely to really be com-pletely empty) storage area. The fire is believedto have been caused by the opening of a reliefvalve on a propylene cylinder due to the vaporpressure of propylene, perhaps at a pressurebelow its set point. The vapor pressure of pro-pylene equals the 390 psig relief valve set pres-sure at 149 8F. The fire rapidly escalated, andwithin minutes involved the entire facility.Employees immediately evacuated and calledfor assistance from the St. Louis fire depart-ment. The fire department evacuated peoplefrom a 5 block area surrounding the facility andfocused on preventing spread of the fire. Therocketing cylinders made it too dangerous toapproach the fire too closely.

A number of lessons from this incident applyto almost any process facility.

� A

1 HJ.A2 hcy

01

fire can escalate very quickly, and rapidaction is necessary to protect people whowork in the facility. The CSB reports thatwithin 4 minutes of the fire first beingobserved, most of the facility was involvedand cylinders were already observed to beexploding frequently!

� T he Praxair employees did the right thing –

they evacuated the plant and called for help.The fire department also did the right thingand focused on protecting people from theeffects of the fire. This is in contrast to otherincidents where employees tried to respond

endershot, D. C. Learning from Experience.Chem. Health Safety, 2008, 15 (2 (March/pril), 34–35.ttp://www.csb.gov/praxair-flammable-gas-linder-fire/ (accessed 8.3.14).

3 Fexwexex19na

� Division of Chemical

4.03.004

to an incident and stop a release of flam-mable or reactive material, and were killed inan explosion when their efforts failed.3

� A

lthough it may have opened prematurely,the relief valve likely did what it was sup-posed to do – it prevented rupture of thecylinder to which it was attached. The fireresulted from ignition of the discharge fromthe relief valve. Emergency relief is a system,including understanding what happens tothe material released. This may be difficultto manage for a portable cylinder, but in afixed process facility you have control overwhat happens to a relief device discharge.

� R

elief valve performance can deteriorate fol-lowing activation.

� A

robust process with a larger differencebetween normal operating pressure (as wellas foreseeable deviations) and the relief valveset pressure is inherently safer. The CSBvideo narration indicates that the relief valveon the cylinder could have been set at ahigher pressure – the cylinders were strongenough to withstand greater pressure. Thismay be true for the cylinders involved in theincident, but perhaps not for all propylenecylinders. This doesn’t only apply to pres-sure, but to any safety-critical process para-meter – you don’t want normal operatingconditions to be too close to a hazardouscondition.

� T

here is a ‘‘learning from experience’’ lessonin this incident. The CSB report identifiestwo similar incidents that had occurred atother places, in 1997 in Phoenix, AZ, and in2003 in Tulsa, OK, both involving propylenecylinders and hot weather. About a monthafter the St. Louis incident, another Praxairfacility in Fresno, CA had a similar incident.

When reading incident reports and viewingsafety videos such as those from the CSB, oneof your challenges is to understand how youcan apply the lessons to your process, eventhough the technology may be very differentfrom that involved in the incident.

or example, the CSB report on the April 2004plosion at a PVC plant in Illiopolis, IL (http://ww.csb.gov/formosa-plastics-vinyl-chloride-plosion/), and the EPA/OSHA report on anplosion in a blender in Lodi, NJ in April95 (http://www.epa.gov/oem/docs/chem/pp.pdf).

Health and Safety of the American Chemical Society 35Elsevier Inc. All rights reserved.