Showing posts with label CCPS. Show all posts
Showing posts with label CCPS. Show all posts

Wednesday, June 24, 2020

2020 Hurricane Season and Chemical Facility Safety – CSB and CCPS Insights


We are now less than a month into the official 2020 Hurricane season and we have already had four named storms. With both the official season forecast and recent updates indicating that we are looking at an active hurricane season this year, owners of chemical facilities near the Atlantic or Gulf coasts need to plan for protecting their facilities from potential wind, surge or flooding events associated with tropical systems. Both the Chemical Safety Board (CSB) and the Center for Chemical Process Safety (CCPS) recently produced guidance on what types of actions facility owners need to consider.

CSB Flood Video


No discussion of modern hurricanes and chemical facilities can take place without a brief discussion of the 2017 incident at the Arkema manufacturing facility in Crosby, TX during the aftermath of Hurricane Harvey. The CSB’s Arkema investigation page summarizes the incident:

“On August 29, 2017, flooding from Hurricane Harvey disabled the refrigeration system at the Arkema plant in Crosby, TX, which manufactures organic peroxides. The following day people within a 1.5 mile radius were evacuated. As the trailers increased in temperature the peroxides spontaneously combusted on August 31. Officials ignited the remaining trailers, on Sunday, September 3, 2017. The evacuation zone was lifted on September 4, 2017.”

Yesterday the CSB released a new video about the flooding risks at chemical facilities based upon the lessons learned in their Arkema investigation.

2020 Hurricane Season Guidance


Along with that flooding video, the CSB also published “2020 Hurricane Season: Guidance for Chemical Plants During Extreme Weather Events”. This brief document starts with the introduction of a new guidance document from CCPS (more about that below). It then continues with a discussion about actions that should be taken in restarting a chemical facility after a weather event. It has sections addressing:

• Hazards of startups following an extreme weather event,
• Relying on established safety systems, and
• Checking process equipment thoroughly.

That last section contains a brief checklist of items that need to be addressed. Includes a non-exhaustive list of details to look for when examining:

• Large bulk storage tanks for evidence of floating displacement or damage,
• Pressure vessels and small storage tanks for evidence of floating displacement or damage,
• Insulation systems for piping, vessels, and tanks,
• Sewers and drains,
• Furnace systems,
• Electric motors and drives, and
• Switchgear, conduit, electrical boxes, electronic and pneumatic instrumentation, emergency warning systems, emergency equipment.

CCPS Monograph


As mentioned in both the video and the CSB guidance, the Center for Chemical Process Safety (CCPS) has published a monograph on the “Assessment of and planning for Natural Hazards”. This document was prepared in response to one of the five recommendations from the CSB Arkema incident investigation. This is a much more detailed document (as one should expect) than the CSB guidance discussed above.

The 44-page document has sections on:

• Identifying natural hazards of concern,
• Gathering data about those hazards,
• Identifying equipment to be addressed in natural hazards assessments, and
• Evaluating against design criteria.

There are also two sections addressing post incident activities: recovery and recommissioning. As with most technically oriented documents, there is an extensive list of appendices providing more detailed information on topics such as:

• Site screening for natural hazards,
• Contents of a natural hazard’s emergency response plan,
• Activity list for before, during and after a natural hazard event, a
• List of interdependencies.

Commentary


The CCSP document has a wealth of good information, but there are two points that need to be repeated loudly and often. The first is a proper identification of the equipment that needs to be specifically covered in a natural hazard’s assessment. The document makes this important distinction (pg 2):

“For example, the emergency power system may be important for continued operation during a natural disaster, but the maintenance shop equipment may not be. Any equipment or operation that is required for safe operations or that, if compromised, could lead to a process safety event, harm to personnel the community, or the environment should be identified.”

The second refers to the failing at Arkema that was identified by the CSB accident investigation, ‘common mode failure’. The CCPS document explains (pg 3):

“A challenge in natural hazards response planning is that a number of important systems and pieces of equipment may be impacted by the same hazard at the same time, or in rapid succession. This may also include the layers of protection that have been installed to protect equipment. A common mode failure may be rising flood waters. For example, as the water level continues to rise, more and more equipment may be inundated and, eventually, even the equipment on “high ground” may also be flooded.”

Unfortunately, while identifying the ‘common failure mode’ problem, the authors do nothing to provide guidance on what needs to be done to ensure that those failure modes are adequately mitigated, or at least clearly identified in any subsequent risk assessment.

The other area where this CCPS document is light in its coverage is in their discussion of emergency response planning. The information in the two ERP appendices is very good for on-site emergency response planning. What is missing is discussion of pre-incident coordination with the local emergency response planning community. Only two topics (both important, to be sure) are identified:

Communications – “It is important that regional and national Emergency Service Providers be able to communicate with the facility Emergency Response Center and the facility being impacted by the natural disaster (if it is staffed).” Pg 21

Access Credentials – “Area access may be restricted before the disaster hits. Develop a plan for emergency access credentials for employees who will be coming in to staff the plant during the emergency. Do not count on employees being able to get in just because the disaster had not yet occurred. Local emergency officials may have already closed roads to all travelers without appropriate credentials.” Pg 23

What is missing is any discussion about coordination with the Local Emergency Planning Committee (LEPC) or other local/regional emergency planners about the specifically identified natural hazards for the facility and management plans for dealing with them. More importantly, identification of any mitigation assistance the facility might need as an incident progresses, or what off-site implications may need to be dealt with if facility plans fail to adequately contain a chemical incident.

One specific lesson from the Arkema incident is not addressed at all and that is the complication that lead to criminal charges being filed against the Arkema management. During the flooding event in Crosby, TX the road that led past the facility was the only major thorough fair that remained open during the flooding. Having to close that route because of potential chemical releases, caused so much problem for local authorities that they allowed emergency responders, without adequate training or equipment, to continue to use the road while the incident progressed.

An early discussion between facility management and local emergency response personnel should have identified this as an added problem for the facility that should probably have required a pre-flooding evacuation of the peroxides that caused the problems at the facility. Relying on just onsite consequence evaluations minimized the consideration of that option.

All in all, the two documents and video identified here are worthwhile and useful. Any chemical facility management team should review them closely and take appropriate action. Weather events are not going away and seem to be getting worse over time.

Thursday, March 18, 2010

CCSP Congress to Address IST Issues

Thanks to some prodding by a reader from DHS, I just finished taking a look at the program for next weeks Center for Chemical Process Safety’s (CCPS) 6th Global Congress on Process Safety. The reason for the DHS interest is explained in this quote from the CCPS web site:
“The US Department of Homeland Security’s Chemical Security Analysis Center (CSAC), part of the Directorate of Science and Technology, has initiated an effort to enhance the safety and security of hazardous chemicals. As a first step, AIChE’s Center for Chemical Process Safety (CCPS) has received a contract to develop a formal scientific and technical definition of Inherently Safer Technology (IST). This definition is intended to help inform discussions of the role of IST in chemical plant and refinery security.”
Back in February the CCPS and DHS held a workshop for technical experts in the field in Houston, TX. The formal report from that session will be presented at next weeks Global Congress on Process Safety. In fact, there will be two half-day sessions at the meeting in San Antonio that will specifically address the issues surrounding IST and chemical facility security. Both sessions will take place on Monday, March 22nd. The morning session will include:
10:00 am - Overview of Inherently Safer Technology (Dennis C. Hendershot) 10:30 am - The DHS Chemical Facility Anti-Terrorism Standards – A Risk-Based Approach to Chemical Facility Security (Larry Stanton) 11:00 am - Inherently Safer Technology Trade-Offs (Jatin Shah)
The afternoon session will include:
1:30 pm - Federal View of Inherently Safer Technology From the CSB Perspective (John Bresland) 2:00 pm - ACC Philosophy On the Appropriate Application of Inherently Safer Principles (Peter N. Lodal, Laurie A. Miller) 2:30 pm - Applying Inherently Safer Systems – Contra Costa County's Experience (Randall Sawyer) 3:30 pm - Facilitated Panel Discussion and Audience Q&A/Discussion Session
The panel for the afternoon’s discussion will include all of the earlier presenters. While the CCPS is preeminently a safety organization (recognized throughout the world for their safety expertise) they also provide information and expertise that is critical to the thoughtful development of security procedures and processes. As we have come to expect, there will be a number of other presentations at this process safety meeting that will address issues of concern to the chemical security community. They will include:
● Simulating the Consequences of an HF Release and Evaluating the Effectiveness of Safeguards to Reduce those Consequences (Randy Hawkins, Daniel Sheahan) ● Atmospheric Storage Tank Explosion Modeling (Jérôme Taveau, Jérôme Richard) ● Update of “Guidelines to Vapor Cloud Explosion, Pressure Vessel Burst, BLEVE and Flash Fire Hazards” (Quentin A. Baker, Adrian J. Pierorazio, John L. Woodward, Ming Jun Tang) ● Consequence Modeling of Chlorine Release (Prakash Amulakh Shah, Chandrakant J. Patel, Ms. Raja Kirthi Kalluri) ● Learning the Lessons From Buncefield (Ian Travers) ● Process Safety and Chemical Security—the Need for Company Specific Risk Criteria (Brad A. Fuller)
If you can make the time and get to San Antonio, TX next week, I think that the sessions would certainly be worth your time. Registration is still open and CCPS is allowing people to register on each day of the meeting.

Thursday, November 5, 2009

2nd Edition of IST Bible

Earlier this week John Wiley and Sons announced the release of the 2nd Edition of the book “Inherently Safer Chemical Processes: A Life Cycle Approach, 2nd Edition”. The book by the Center for Chemical Process Safety is an update of the 1996 edition that looks at the latest chemical engineering advances supporting the concept of inherent safety. There is a chapter on inherent safety and security. According to the contents page this chapter addresses:
“Chemical Security Risk. “Security Strategies. “Countermeasures. “Assessing Security Vulnerabilities. “Inherent Safety and Chemical Security. “Limitations to Implementing IS Concepts in Security Management. “Conclusions.”
I have my copy on order through Amazon.com. Using the reviewing tools that Amazon.com provides to its customers I was able to find one quote from that chapter (pg 160) that should be considered by members of the House that will be voting on some IST provisions as they consider amendments to HR 2868 today. It address the difficulty in assessing the efficacy of IST applications in the security arena.
“However, inherent safety can be a complex issue. Inherent safety may or may not be the most effective security strategy, particularly if a new security concern is created or the security risk is simply shifted. It may be unrealistic to expect that all hazards are eliminated by inherent safety. Instead, all options must be examined in a complex context to assess risk reduction benefits and costs and to consider ris/risk tradeoffs that may unintentionally occurs. They also must be weighed against the benefits of the operation, as well as alternatives, such as more traditional security measures, and whether the overall risk is sufficiently managed.”
Everyone that has concerns, pro or con, about the use inherently safer technology to reduce the risk of terrorist attacks needs to get their own copy of this book. I’ll be looking at the book in more detail in future blogs.

Monday, July 13, 2009

CCPS Safety Beacon – Safety Instrumented Systems

Every month the Center for Chemical Process Safety publishes out a ‘Safety Beacon’ poster that addresses some chemical process safety issue. This month the Safety Beacon deals with Safety Instrumented Systems (SIS); automated systems that are put into place to protect chemical processes from ‘upset’ conditions that can lead to an unsafe release of hazardous chemicals. Typically these systems are physically separated from ‘normal’ control system so that damage or an attack to that system would not affect the SIS. They are also provided with automatic backup power so that they continue to operate in the event of a power failure. These system consist of three separate parts. A sensor system is employed to detect the abnormal condition. A logic controller compares the output of the sensor to programmed set of pre-defined upset conditions. Finally a control device is employed to counteract or correct the process upset. SIS as Security Systems High-risk chemical facilities that already employ SIS technologies should take a hard look at those systems to see if they have some applicability to the facility’s site security plan. Systems that would limit the amount of a toxic release COI that would reach the fence line could be listed as a security system under RBPS #4 {Metric 4.5: “process controls or systems that rapidly render the critical asset nonhazardous even if a breach of containment were to occur” (pg 58, RBPS Guidance document)}. Fire suppression systems that would prevent or limit a flammable release COI from forming a detonatable cloud upon release should also be reportable under these circumstances. Similarly, facilities should also look to designing similar stand alone Security Instrumented Systems to perform a dedicated security function. The example that DHS uses in Metric 4.5 is ‘a rapid chemical neutralization system”, but any system that mitigates the effects of a release would serve the same purpose.
 
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