Updated April 2026 - Those who work in high hazard industries are familiar with the OSHA Process Safety Management (PSM) requirements for routine Process Hazard Analyses (PHA) for their processes. Hazard and Operability (HAZOP) and Layer of Protection Analysis (LOPA) are recognized methods for PHA. LOPA is widely used as a semi-quantitative method to identify, assess, and improve the most effective safeguards for higher consequence scenarios identified in a qualitative HAZOP study . One of the important products of a LOPA is a list of Independent Protection Layers (IPL) . When correctly identified, IPLs are devices, systems, and actions that are capable of preventing a hazard scenario from proceeding to the undesired consequence. In layman’s terms, they are the “best” and most effective of the safeguards that were identified in the HAZOP for specific scenarios and initiating events. The core attributes for safeguards to qualify as IPLs are well-known and have criteria including: Independent of the initiating event and of other protection layers Specific to the hazard Functional, dependable, and reliable (including routine testing) Auditable Secure Subject to management of change There are many reputable sources for training for the HAZOP and LOPA methods. Many organizations also have good internal guidance on this subject. But what happens when inadequate guidance, training, or discipline for the correct use of LOPA and identification of IPLs is present? You might be surprised at how often safeguards not meeting the core attributes are specified as IPLs in industry. It’s easy to find advice detailing the complexities of proper IPL selection and management, but without a facilitator well-versed in the basics of IPL selection, LOPA teams can get off on the wrong foot. The Challenges Many companies and LOPA practitioners employ excellent practices to identify and validate IPLs during LOPA. However, it is surprisingly common for significant IPL selection errors to be encountered during externally facilitated revalidation PHAs, audits and other types of process safety reviews. IPL concerns of the following types are entirely possible to occur in LOPA studies if initial selection or follow-up IPL validation is not as it should be: Use of two or more relief devices, all taken with two or more IPL credits. Relief devices are often a highly effective safeguard. However, they are subject to concerns that should limit the credit taken at times, including use in services where "pluggage" or other common cause failures are credible, engineering assumptions on sizing are not as the PHA team assumed, poor-quality or no routine inspections are performed, and other issues. Use of instrumentation whose failsafe failure modes are opposite of that assumed by the PHA team, which may result in an unrecognized IPL failure to the dangerous mode. Selection of one facet of an IPL such as a BPCS alarm, without recognition that other facets are also needed for a complete IPL, such as alarm prioritization and management, training in the specific alarm response, an operating procedure, and proper field instrument functional testing. Selection of a BPCS alarm and Operator response as an IPL, without confirming that sufficient time is present before hazard development to evaluate and respond effectively to the alarm. Selection of IPLs with insufficient independence from the initiating cause of a hazardous scenario, or insufficient independence from another IPL for the same scenario. A classic example of this is selection of an instrument to alarm or interlock of a process condition that could be initiated by a failure of that same instrument. Crediting design pressure and temperature ratings; both are equipment attributes that should normally be taken into account in identifying the scenario consequences, not credited as an IPL. Building Confidence Improperly selected and validated IPLs can result in high hazard scenarios that have far less risk reduction in place than you think you have. Implementing a systematic process to properly vet your IPL candidates for the core attributes is strongly recommended. Engaging experienced PHA/LOPA facilitators and having the right team during the meeting is the first step in proper IPL selection. Further validation of IPLs to confirm they meet the defined criteria can be time consuming but also goes a long way toward increasing your confidence in your most important safeguards for higher consequence scenarios in highly hazardous chemical processes.

Updated April 2026 — Authored by Carolyn Bott — A Process Hazard Analysis (PHA) will prove to be the cornerstone of Process Safety Management (PSM) at any operating facility with the correct tools and the right leaders. Although there are many variables concerning PHAs, the process can be simplified and impactful results can be attained. In this blog, we delve into the 5 facets of an efficient process hazard analysis (PHA). Process Hazard Analysis Scope A well-defined scope for a Process Hazard Analysis is critical to identify potential safety and environmental hazards in a facility. Having a clear and defined Process Hazard Analysis scope does the following: Sets the boundaries of the analysis - This assures all necessary elements are included and relevant risks are identified and assessed Enables the Process Hazard Analysis team to focus on specific areas of concern and analyze them in detail - This reduces the potential for error and minimizes both the time and resources needed Ensures that all stakeholders are aware of the objectives and outcomes of the PHA Standard for Approaching a Process Hazard Analysis Different companies may have their own specific Process Hazard Analysis standards, specific to their operations and the risks involved. These standards typically outline essential measures to perform a thorough PHA, including: Qualifications and training required for team members Selection of appropriate methodologies Level of detail required in the analysis Documentation requirements for the study Frequency of review Ongoing monitoring requirements ensuring the safety and efficiency of operating processes Adherence to these standards is typically required by regulatory bodies and industry best practices. A standard can ensure all relevant factors are considered and a thorough analysis is conducted. Following a standard also facilitates communication and collaboration among stakeholders, enhances consistent decision-making across sites, and promotes continuous improvement in a site’s process safety. Process Hazard Analysis Team An effective Process Hazard Analysis team is composed of individuals with diverse expertise, including engineers, operators, maintenance personnel, and safety professionals. The team: Shall have expertise in engineering and process operations Shall include at least one employee who has experience and knowledge specific to the process being evaluated One member of the team must be knowledgeable in the specific process hazard analysis methodology being used Must be able to work collaboratively to identify hazards, evaluate risks, and develop appropriate risk management strategies Effective communication and teamwork are vital for a successful and efficient PHA. The proficiency of the PHA leader or facilitator has a substantial impact on the team and the outcome of the PHA. A facilitator leans on their own risk management experience and is responsible for guiding the team through the identification and evaluation of all credible process hazards. The leader continuously assesses the team’s dynamic and intervenes when necessary to ensure the group remains on task to complete the PHA efficiently with impactful results. A company can utilize in house experts or hire a third-party to shepherd their Process Hazard Analysis needs – Process Safety Consulting Process Hazard Analysis Techniques & Tools Methodologies The methodology selected must be appropriate to the complexity of the process and site standards. One or more of the following methods, as appropriate, may be used to determine and evaluate the hazards of the process being analyzed: What-if Checklist What-if Checklist Hazard and operability study (HAZOP) Failure mode and effects analysis (FMEA) Fault tree analysis An appropriate equivalent methodology For more info on choosing a risk assessment methodology, check out our webinar that examines the advantages and limitations of various methodologies: Choosing a Risk Assessment Methodology Tools Computer-based systems are used to document Process Hazard Analysis discussions in an organized manner and provide consistency throughout the analysis. Examples of PHA documenting software include: Sphera® PHA-Pro® PrimaTech PHAWORKS RA® aeShield® aeFacilitator® Using appropriate software eases the execution of risk studies. Process Hazard Analysis Review Cycle All Process Hazard Analyses must be updated and revalidated every five years. The periodic review should reflect any changes in the process or surrounding environment that may impact safety. An alternate approach to managing PHA updates is to incorporate them into the study file as changes occur. This method is often called an Evergreen PHA or Continuous PHA Revalidation. An efficient and effective PHA can enhance the safety of processes, reduce the risk of accidents and incidents, improve compliance with regulations and standards, and ultimately support the organization's goals and objectives. Ensuring these five (5) components are in place can help companies have an efficient PHA to identify and mitigate risks before they become safety incidents. The Takeaway | 5 Facets of an Efficient Process Hazard Analysis Summarized Clear and well-defined scope that is relevant to the system being analyzed Systematic and structured approach Multi-disciplinary team of subject matter experts who can identify and evaluate potential hazards from different perspectives Use of appropriate techniques and tools to evaluate and prioritize risks Periodic reviews and updates If you need more guidance for your Process Hazard Analysis, please feel free to reach out to aeSolutions to speak with one of our PHA experts about our capabilities. Click here for more information on aeSolutions' HAZOP Study services

What’s a HIPPS and where are they used? Updated April 2026 - There are two common applications for a High Integrity Pressure Protection System (HIPPS) . First, many process facilities have expanded to the point where the original pressure relieving and flare system may no longer be able to handle a potential event. Preventing a potential overpressure through the use of a HIPPS can be done at a much lower cost compared to installing a new flare and header system. Second, many subsea and land based pipelines are not designed to withstand full wellhead pressure. So a HIPPS measures pressure (usually using redundant transmitters), utilizes a logic solver (many technologies and configurations are acceptable), and closes valves. While such designs are allowed per current codes, the justification of such a system requires careful analysis by a team of specialists. The justification and analysis of a HIPPS must consider all operating and upset conditions that might cause an overpressure. Process dynamics must be analyzed to determine if the HIPPS can respond quickly enough to prevent the hazard. Some cases may be quite complex with multiple scenarios and multiple HIPPS. Without an adequately sized conventional relief system, the HIPPS represents the last line of defense against an overpressure event. Subsequently, many end users require an independent, third party review of the justification of such a system. How good is good enough? A HIPPS should offer performance as good or better than the conventional relief system it may be replacing. The performance of relief valves in the process industries varies considerably depending upon the application. Published sources of data show that relief valves in some applications offer performance no better than the equivalent of Safety Integrity Level 1 (SIL 1). Considering the uncertainty of the data, many specify that HIPPS meet SIL 3 performance. This requires the use of fault tolerant sensors a nd valves. The use of a SIL 2 system is still a possibility, with significantly lower capital and operational costs. Questions to ask yourself Do you have a case where the existing relieving system is unable to adequately handle the load, and has this been documented in a thorough hazards analysis? Is the vessel in air, water or steam service? (If yes, the use of a HIPPS is not permissible.) Is approval of local authorities required? Do you have a case where a pipeline is not rated for the full wellhead pressure? Have you performed a SIL selection study to determine the level of performance that will be required by the HIPPS? aeSolutions is here to help aeSolutions can help you determine whether a HIPPS is a viable option for your application. If justified, we can work with you to develop the requirements specification and deliver a system that will meet your specific safety and cybersecurity needs. #HIPPS Click here for more information on aeSolutions' pressure relief study services

By Chris Hickling Updated April 2026 - A Fire & Gas System (FGS) philosophy provides a solid foundation for the design of an effective gas detection system, which in turn helps protect plant and personnel from gas releases and resulting flammable and/or toxic effects. An FGS philosophy for a process facility that is not fit for purpose or does not have a firm auditable basis can increase the likelihood of undetected leaks incurring risk to personnel or unnecessary expenses for the company. Under-engineering a gas detection system has safety implications, while over-engineering has commercial implications such as increasing capital and maintenance costs without significantly reducing risk. The workflow for an FGS philosophy can be summarized in the following steps: Assess FGS requirements – review regulatory requirements, corporate standards, pertinent Process Hazard Analysis (PHA) recommendations, and Recognized And Generally Accepted Good Engineering Practices (RAGAGEP) Develop FGS philosophy and procedures – review materials and properties (flammable, toxic, or inert), process flow, and risk tolerance criteria Define FGS scenarios and zones – determine hazards using data for process conditions, weather, occupancy, and airflow data, and drawings such as plot plans, Piping & Instrumentation Diagrams (P&IDs), and Cause & Effects (C&Es) Define zone FGS performance requirements – Develop criteria to assess facility layout and define areas Develop criteria for FGS detector placement What makes an effective FGS philosophy? Firstly, it's important to establish the scope of the FGS system. Is it intended to protect on-site personnel and equipment, offsite community, and/or environment? A comprehensive review of the entire facility is essential – if individual process units at the facility are exclusively analyzed for gas detection, it could result in a fractured response and unforeseen effects at other units. A gas cloud doesn't care where it's released or where it's going, and it doesn't respect boundaries. Secondly, the FGS philosophy should follow applicable codes like NFPA 72 and be applied consistently across the facility. Issues could arise if different areas of the plant use different gas detection technologies or alarm levels; for example, if one unit of the plant alarms at 10% of the Lower Explosive Limit (LEL) and another unit alarms at 20% LEL, or there are inconsistent color of warning strobes for a toxic gas release. Consistency in gas detection, alarms, and encompassing standardized procedure(s) helps the operators and employees respond efficiently. Additionally, the FGS philosophy should lay down the criteria for decisions on gas detection required and appropriate mitigative response such as alarm levels (e.g., alarm at 10% LEL). The FGS philosophy also helps decide the voting criteria for the number of gas detectors to take action. For example, two out of two (2oo2) gas detectors may be required to alarm before starting the sprinkler system or dumping Halon. Finally, an FGS philosophy should be auditable. During its development, assumptions are made which feed into how the gas release is modeled and location of gas detectors. If a bad assumption is made and a leak later occurs, it is essential to be able to revisit the original FGS philosophy and assess the original basis for the design. If the gas detection system has a performance-based design, the layout of the system is documented so that it can be reviewed and adjusted. Traditional rules of thumb gas detector placement do not offer this ability to review and update the basis. Once these practices are incorporated into a facility's FGS philosophy, a comprehensive and well-documented FGS philosophy provides a solid foundation for the design of an effective and auditable gas detection system. Facilities can have a dependable basis to ensure an appropriate number of gas detectors in the appropriate locations, potentially lowering risk and minimizing costs for the gas detection system. Click here for more information on aeSolutions' SOP Training and Development services

Understanding a Dust Hazard Analysis (DHA) Updated April 2026 - Following on from the first four aeSolutions blogs on the subject of combustible dust concerns , this blog provides another deep dive into the topic. We previously addressed the basic concerns around combustible dusts, many of the standards that address dust hazard guidance , and the properties and testing for combustible dusts ; potential ignition sources ; and potential safeguards . This article will build on those topics to pull it all together and review a commonly used dust hazard analysis (DHA) method. The Challenges | Dust Hazard Analysis (DHA) A Dust Hazard Analysis or DHA is an important method to assess the risk posed by ignition of combustible dusts. Companies handling highly hazardous chemicals (HHC) routinely conduct process hazard analyses (PHAs), but it is not common to encounter PHAs that thoroughly review combustible dust hazards or company internal standards that address combustible dust hazards. Many companies’ PHAs do not address combustible dust hazards in an organized manner or in a manner that complies with industry guidance on dust hazard analyses (DHA), if the dust hazards are reviewed at all. Why Would You Conduct a Dust Hazard Analysis For a Combustible Dust Process? There are several reasons, and the most obvious is to protect people, the environment, assets, and reputation from dust explosions and fires. Other reasons for a Dust Hazard Analysis (DHA) include: The OSHA general duty clause requires that, in addition to compliance with hazard-specific standards, all employers provide a work environment " …free from recognized hazards that are causing or are likely to cause death or serious physical harm. " A company may identify the need for a Dust Hazard Analysis on an existing combustible dust process internally due to this requirement. A dust explosion incident involving a dust with identical or similar properties to that in an existing process may occur. An industrial hygiene review of process dust or particulates may identify combustibility concerns. A PHA team may identify the need for a deeper dive into dust risks. A codes and standards review may identify NFPA 652 (Standard on the Fundamentals of Combustible Dust) as a needful standard for compliance. NFPA 652 is considered to be a Recognized And Generally Accepted Good Engineering Practice ( RAGAGEP ). An insurance company providing coverage for the facility may request it. How to Conduct a Risk-Based Dust Hazard Analysis A Dust Hazard Analysis is a focused method to improve facility safety by identifying combustible dust hazards and necessary safeguards associated with a process. There are variations across companies on how DHAs are conducted, similar to the many variations on PHAs that can be found in industry, but there are two basic approaches: a traditional approach based on an engineering analysis and standards compliance; and a risk based approach. Most companies opt for a risk-based approach and those basic steps are described here: Identify the relevant properties of a combustible dust (as described in part 2 of this series). Form a suitable team to perform the Dust Hazard Analysis, including a qualified facilitator. Determine which internal and industry standards apply to the Dust Hazard Analysis and educate team members on those standards. (There is a partial list of applicable industry standards in part 1 of this series.) Assemble or develop the process safety information that the Dust Hazard Analysis team will need, including equipment ratings, electrical area classification designations, dust data, safe operating ranges, operating procedures, housekeeping protocols, and current maintenance regimes, among other data. If there are existing mitigating safeguards (as described in part 4 of our Dust Hazard Analysis series ), data on those systems should also be readily available. With guidance from a qualified facilitator, the team develops the credible dust cloud and dust layer scenarios internal and external to the equipment. The team identifies the credible internal and external ignition sources for each scenario (as described in part 3 of our Dust Hazard Analysis series ). The team then assumes that an ignition occurs in each scenario and assesses and describes the potential unmitigated safety and environmental (and sometimes commercial and reputational) consequences. Guidance from a qualified facilitator is crucial at this step. The team then assesses the likelihood of occurrence of the credible ignition sources. Guidance from a qualified Dust Hazard Analysis facilitator is also crucial at this step. Risk ranking results and acceptance criteria vary from company to company, but typically the team then uses the consequence and likelihood to develop an unmitigated risk rank for each scenario. The team then assesses existing preventive and mitigating safeguards for each scenario, using those factors to determine the existing mitigated risk rank for each. When the mitigated risk ranking does not meet the risk criteria set by the company, then the team typically develops recommendations for additional engineering and/or administrative safeguards. The team may also need to issue recommendations to ensure that safeguards have sufficient specificity, independence, dependability, and auditability, similar to Layer of Protection Analysis (LOPA) independent protection layers , if that is a company expectation. Finally, the facility follows up on the Dust Hazard Analysis (DHA) recommendations. If this process sounds a great deal like a HAZOP study to you, then you are right on target. It is also a common practice for companies to adapt their LOPA methods to be suitable for Dust Hazard Analyses for the higher consequence scenarios. It is generally a feasible task to adapt or develop HAZOP and LOPA software templates to be suitable for DHAs. It can even be done in spreadsheets or word processing documents in case of need, though this type of documentation is a little more difficult to initially develop. An excellent reference for those who wish a deeper dive into DHA methods is Guidelines for Combustible Dust Hazard Analysis , 1st Edition, 2017, by Center for Chemical Process Safety, published by Wiley-AIChE available on-line from your favorite technical bookseller. The Risk of Dust Hazards Do you handle potentially combustible dusts at your site? It is difficult to adequately control a hazard that is not well-understood. Even if you have a good-quality PHA, it may not delve deeply enough into the combustible dust topic in accordance with NFPA 652. NFPA 652 states that existing processes and compartments (e.g., building compartments) shall have a completed DHA by September 7, 2020 (¶ 7.1.1.2) and that the Dust Hazard Analysis shall be reviewed and updated at least every five years (¶ 7.1.4). Are you in compliance? Are you positive your site is managing its combustible dust risks in all phases of operation well enough to prevent a serious explosion? The Takeaway - Dust Hazard Analysis (DHA) If you have not previously taken a deep dive into the combustibility properties of your particular dust(s) and completed a Dust Hazard Analysis at your site, now would be a good time to do so. If you do not have the right expertise in your staff to assess dust hazards, consider engaging a process safety consultancy with deep experience and expertise to assist you. Their range of experience enables assessors to share the general and specific methods proven to minimize dust explosion hazards across industry. This independence from the site and company has the best probability of a careful analysis with fresh eyes on the relevant critical systems and leads to more efficient compliance with the necessary standards. Written by Judith Lesslie, CFSE, CSP AIChE Webinar: Combustible Dusts and Dust Hazard Analysis: Assess Your Risk presented by Judith Lesslie - Senior Principal Specialist - aeSolutions

by Judith Lesslie, CFSE, CSP Updated April 2026 - Those who work in high hazard industries are familiar with the OSHA Process Safety Management ( PSM ) and EPA Risk Management Plan (RMP) requirements for routine audits to assess and verify compliance with these regulations. In a prior blog, we reviewed different strategies for accomplishing these audits. In this blog, we will cover specific types of concerns that have been identified at many manufacturing sites. The Challenges Companies conduct audits in order to assess the effectiveness of their process safety systems, with the primary goal of ensuring their covered processes are managed in a way that minimizes the risk of process safety incidents. In a review across many manufacturing segments, company, and site PSM and RMP audits, it has been found that the same types of concerns are present at many locations. These areas of concern occur across the entire range of PSM and RMP elements. In Part 1 we discuss PSM/RMP applicability, Employee Participation, Incident Investigation, Contractor Management and Hot Work, Emergency Response and Audits: In the area of PSM and RMP applicability , it is important for sites to assess and document their inventories of highly hazardous chemicals (HHC), keeping in mind that the PSM and RMP HHC lists are not identical. In a related vein, failure to analyze HHC inventories near occupied buildings and failure to completely assess interconnectivity of potentially covered process equipment can be serious concerns. Employee Participation is an important element of compliance. While most sites have a reasonable level of employee participation in their process safety programs, that participation is often not described in a procedure or road map. This represents a missed opportunity to document participation and to educate site personnel on their opportunities to get involved in process safety activities. Sites often have a one-size-fits-all Incident Investigation method, which may be either too simple or too complex for some incidents; this leads to the potential for missed root causes that need to be addressed or to spending too much time and effort on less severe incidents. Allowing for a range of investigation methods depending on the actual and potential severity of an incident is an excellent practice to consider. Management of Contractors is typically reasonably good across sites, with the possible exception of failure to consider past performance of contractors in ongoing selection processes. A process to define acceptance criteria and to assess past performance of contract firms via review of their OSHA logs is sometimes found to be a concern. One would think that compliance with the Hot Work element would be simplest of all since the requirements are clearly and prescriptively outlined in OSHA 29 CFR § 1910.252. Two of the most frequently identified concerns for this element are failure to maintain or document a fire watch present for 30 minutes after any welding or cutting operations. The other is failure to post additional fire watches on multi-level worksites where falling sparks may be a concern or conduction, or radiation may pose a concern to combustibles that cannot be removed or protected. Emergency Response is an area where the PSM and RMP standards diverge to some extent, including the distinction between offensive and defensive responders. Compliance with the PSM Emergency Response element is relatively straightforward and largely covered in 29 CFR 1910.38 - Emergency action plans. Where concerns are more often identified is in the RMP Emergency Response element, where the outward-looking activities are not always in perfect order. For example, all affected public receptors may not be identified and documented in the site emergency procedures, and/or the contact information for those receptors may not be tested on a regular basis. While not specifically a PSM or RMP requirement, the incident management plans for some companies do not take advantage of structuring their incident management systems in accordance with the National Incident Management System (NIMS); there is valuable free training offered through FEMA which will qualify site personnel to act in standardized ICS roles and enable good coordination with outside agencies in the event of a serious incident. Audits are deserving of their own blog article ( which you can find here ). The most common audit element theme found at various facilities is an audit that does not dig deep enough into process safety programs and into the evidence of execution of each program element. Audits are overdue more frequently than you might anticipate as well. When a good-quality periodic audit with actionable recommendations is executed, that is not the end of the process. The recommendations or actions from that audit then need to be tracked to completion and documented as complete in a reasonable period of time, and that is unfortunately lacking at a variety of facilities. The Stakes The PSM and RMP regulations have proven over time that they are excellent practices to drive the reduction of serious process safety incidents. It is far better for a company and sites to find and correct their own PSM and RMP system deficiencies than for a serious incident to occur or for a regulatory agency to identify it. Are you positive that the commonly found concerns reviewed above are not present at your facility? So What? If you have not previously taken a deep dive into the assessment of the topics above at your site, now would be a good time to do so. If you do not have the right expertise in your staff to assess PSM and RMP compliance in these areas, consider selecting a process safety consultancy with deep experience and expertise to assist you. Their range of experience enables external auditors to share the general methods proven to drive good PSM and RMP compliance across industry. This independence from the site and company has the best probability of a careful assessment with fresh eyes on the relevant critical systems and leads to more efficient compliance with the necessary standards. Click here for more information on aeSolutions' PSM & RMP Audit Services In Part 2 will include a review of common deficiencies in the elements of MOC/PSSR, Process Safety Information, Operating Procedures, Mechanical Integrity , Process Hazard Analysis, and Training.

Updated - April 2026 - The ISA/IEC 61511 Safety Life Cycle starts with a Process Hazard Analysis (PHA) and a Risk Assessment. What is a PHA? Why do we do it? =================================================== Excerpt taken from the webinar: Choosing a Risk Assessment Methodology In the full recording the ANSI/ISA 61511 Safety Life Cycle is shown to start with a Process Hazard Analysis (PHA) and a Risk Assessment. This was the first webinar of our 3 part series and details the purpose of Risk Assessment and examines the advantages and limitations of various methodologies including Risk Graph, Layer of Protection Analysis (LOPA), Quantitative Risk Assessment (QRA) , and others. See all our full recent webinars on https://www.aesolutions.com/webinars As a supplier of complete process safety and risk management solutions, we pride ourselves on providing engineers from industry with design, maintenance, operating, and process safety backgrounds. Our specialists understand how plants operate because they have actually worked in covered processes and facilities. Learn more-- https://www.aesolutions.com/process-s...

December 2024 - Learn about six hidden pitfalls that undermine workplace safety culture and learn actionable strategies to foster a more resilient and safety-conscious environment. This article explores the following topics and more: Click here to read the full article on IEN.com Applicability of Process Safety Management (PSM) and Risk Management Program (RMP) Regulations : Many facilities neglect to assess whether these regulations apply to their operations, leading to unstructured safety processes. Mechanical Integrity : While fixed equipment like vessels and piping are usually well-managed, issues frequently arise with rotating equipment and control systems due to inadequate monitoring and maintenance. Management of Change (MOC) : Organizations often fail to implement robust MOC procedures, resulting in unassessed risks when changes occur in processes or equipment. Operating Procedures : Outdated or poorly documented operating procedures can lead to unsafe practices and increased risk of incidents. Training and Competency : Insufficient training programs contribute to a workforce that is ill-prepared to handle safety challenges effectively. Incident Investigation : A lack of thorough incident investigations prevents organizations from learning from past mistakes and implementing corrective actions. by Judith Lesslie, CFSE, CSP, CCPSC , Senior Principal Specialist at aeSolutions . Read the full article here: Safety Culture: Examining Common Shortcomings - IEN.com

Greenville, SC – February 1st, 2023 – Cigna has selected aeSolutions as a recipient of their Bronze level Healthy Workforce Designation for demonstrating a strong commitment to improving the health and well-being of its employees through a workplace wellness program. aeSolutions has shown a focus on the vitality & well-being of their workforce. This allowed employees to not only be healthier but to be more productive and engaged. “aeSolutions is driven by supporting every stakeholder in the pursuit of their full potential,” shared Ken O’Malley, President, and Founder. “This means we want our employees to thrive both professionally and personally. Providing a robust, year-round wellness program which supports and encourages the physical, mental, social, and financial health of not just our employees, but also their family members, is a critical component of our business’ success. I’m very proud that our results have been recognized and appreciated, by Cigna and by our team members.” Investing in an effective workplace well-being program drives value for employers. Senior executives surveyed as part of an Economist Impact study commissioned by Cigna reported greater productivity, stronger staff morale and motivation, and greater retention and loyalty as the most significant business outcomes of a healthy workforce. Additionally, a Gallup Report finds that on average, companies with high employee engagement are 23 percent more profitable. “As a consultative growth partner, Cigna knows that a healthy workforce is critical to business growth,” said Cindy Ryan, executive vice president and chief human resources officer. “We are honored to recognize organizations like aeSolutions who share our commitment to workplace wellness. Creating a healthy work culture is of critical importance, and many employers are seeing increased employee engagement, productivity, and retention as a result of whole person health wellness initiatives.” The Cigna Healthy Workforce Designation, formerly known as the Cigna Well-Being Award, evaluates organizations based on the core components of their well-being program, including leadership and culture, program foundations, program execution, and whole person health. Organizations recognized with this designation set the standard of excellence for whole-organization health. Cigna is proud to honor aeSolutions with the Bronze level designation for having made good progress towards a healthy work culture by establishing and growing their employee well-being and engagement program. About aeSolutions In business since 1998, aeSolutions is a consulting, engineering, and systems integration company that provides industrial process safety and automation products and services. They specialize in helping industrial clients achieve their risk management and operational excellence goals through expertise in process safety, combustion control and safeguarding, safety instrumented systems, control system design and integration, alarm management, and related operations and integrity management systems. For more information, visit www.aesolutions.com . Media Contact RedIron PR for aeSolutions Kari Ritacco kari@redironpr.com

Introduction | What is UL 508A? November 2025 - Erich Zende —  Industrial control panels are the backbone of modern plants. When those panels are built and labeled to UL 508A, inspectors and insurers have a clear basis for acceptance, and your maintenance team gains documentation that simplifies future changes. This article explains what UL 508A covers, where it fits with NEC and OSHA rules, how Short-Circuit Current Rating (SCCR) is established, what regulations changed in 2025, and what to ask a UL 508A control panel fabrication shop before you place an order. UL 508A  is the North American product safety standard for industrial control panels used in ordinary (non-hazardous) locations, operating at 1000 volts or less. The standard defines construction methods, component suitability, spacings, markings, and required documentation so a panel can be evaluated as “suitable” by Authorities Having Jurisdiction (AHJ). In practice, UL 508A sits alongside the National Electrical Code and OSHA rules. NEC Article 409  requires industrial control panels to be marked, including a Short-Circuit Current Rating (SCCR), and be installed so that the available fault current does not exceed the marked value. OSHA 1910.303  requires electrical equipment to be “approved,” which is shown through listing, labeling, or a field evaluation by a Nationally Recognized Testing Laboratory.   What Does UL 508A Cover? Construction and wiring UL 508A prescribes wiring methods, spacings, and clearances that prevent shock and arcing. It defines when and how to use overcurrent protection, disconnecting means, and the enclosure types required for the environment. It also mandates that markings must be present on the nameplate and drawings. Component suitability Components inside the panel must themselves be suitable. UL 508A references a companion document, commonly called Supplement SA  (now published as a separate UL document), that lists acceptable component standards and conditions of acceptability. For example, UL 489  molded-case circuit breakers are permitted for branch protection, while UL 1077  supplementary protectors are not a substitute for branch circuit protection. Marking and documentation A UL 508A panel must include required markings  such as voltage, full-load current, and SCCR, and deliver drawings and a field wiring diagram the installer can follow. What UL 508A does not cover Some electrical assemblies look similar to control panels but fall under different standards. Examples include UL 891 switchboards, UL 845 motor control centers, and fire alarm control units covered by UL 864. Additionally, panels with intrinsically safe circuit extensions into hazardous locations will refer to UL 698A.   UL 508A in the Code Landscape NEC Article 409 Panels must be marked and installed per 409.110 and related sections . The installer must verify that the available fault current at the point of installation does not exceed the marked SCCR. Failure to match these values is a common reason for red tags. OSHA “approved” equipment OSHA 1910.303 requires equipment to be acceptable only if “approved,” which means listed, labeled, certified, or otherwise determined to be safe by a recognized body. AHJs and insurers often expect a listed panel or a field evaluation report.   SCCR: What It Is and How It Is Established Short-Circuit Current Rating (SCCR )  is the maximum fault current a panel can safely withstand. NEC 409 requires it to be marked on the panel. It is established by UL 508A Supplement SB, which provides the methodology. This typically involves: Identifying the weakest link among power circuit components. Applying tables and tested combinations to determine each component’s rating. Considering current-limiting devices that can raise the overall SCCR. Marking the resulting SCCR on the nameplate and drawings. Design strategies to Raise SCCR Common approaches include using current-limiting fuses, tested combination motor controllers, and terminal blocks meeting the appropriate use groups and spacing.   Component Selection Under UL 508A A compliant panel uses components that are UL Listed or UL Recognized, following the conditions given in the component’s file. Supplement SA explains which standards apply, such as UL 489 circuit breakers, UL 98 disconnects, UL 1059 terminal blocks, and the UL 60947 family for many motor controllers. Underwriter’s Laboratory’s Product iQ tool  can help you verify the status of parts and to capture the specific conditions of acceptability in your bill of materials.   What Changed in 2025: Key UL 508A Revisions On June 26, 2025, UL published a revision to UL 508A that introduces several notable updates: Control circuit voltage limits are now defined at 120 Vac and 250 Vdc, aligning with NFPA 79 practices. Emergency stop requirements were adjusted, making E-Stop a function that may be required depending on the control scheme. Disconnecting means requirements for industrial machinery sections were clarified. Table SB4.1 received a correction for controllers rated 601 to 1000 V. UL 1059 terminal block requirements and overload protection for group motor applications were updated. UL maintains a “ future effective dates ” page so designers can see when new provisions take effect relative to publication. How UL 508A Certified Panels Add Business Value Smoother inspections Panels built and labeled to UL 508A provide a recognized basis for acceptance by AHJs and insurers, which reduces project risk and rework. Risk reduction A correctly established SCCR and appropriate protective devices add resiliency to an operation and reduce the likelihood of catastrophic faults and extended downtime. Simpler maintenance Standardized markings and documentation help technicians troubleshoot and make changes with confidence.   UL 508A in Fire and Gas Applications Panels that host Fire and Gas instrumentation , shutdown logic, and alarm interfaces are often constructed to UL 508A when they are installed in ordinary locations. If your design extends intrinsically safe circuits into hazardous areas, evaluate UL 698A for the related panel requirements. For dedicated fire alarm control units and accessories, reference UL 864. It is important to remember that functional safety for Safety Instrumented Systems is addressed by standards like IEC 61511; UL 508A covers panel construction and does not confer a SIL.   Understanding UL 508A Specification Language A typical clause example for a UL 508A specification will often read similar to this example: “Industrial control panels shall be UL 508A Listed. Provide nameplate marking with SCCR ≥ 65 kA at the service entrance. Enclosures shall meet NEMA 4X. Use UL 489 for branch protection and a UL 98 main disconnect. Use UL 1059 terminal blocks rated for field wiring. Provide documentation and labeling per NEC 409.110.”     Common Pitfalls to Avoid Treating UL 1077 supplementary protectors as branch circuit protection. Leaving the SCCR blank or below the available fault current at the installation point. Using terminal blocks that do not meet the correct use group for field wiring or spacing.   UL 508A Control Panel Deliverables Checklist Example Nameplate with SCCR and required electrical data Field wiring diagram and complete schematics Torque charts, conductor sizes, and protective device settings Bill of materials with component standards and conditions of acceptability   What to Ask a UL 508A Certified Panel Fabrication Shop Before Purchase When you engage a UL 508A panel fabricator , confirm both certification and methodology. Additional questions that are worth asking could include: What is your UL 508A shop file number and audit cadence under the Industrial Control Panel Shop Program? Do you have experience with NFPA 79 panels and, when relevant, UL 698A work for hazardous interfaces? How do you establish and document SCCR and what strategies do you use to reach higher ratings when the site’s available fault current is high? How do you track component suitability and conditions of acceptability, and how are those captured in the BOM and drawings? Can you support AHJ field evaluations when a listed panel needs on-site verification?   Designing for High SCCR and Maintainability Designing for high SCCR and maintainability begins with using current-limiting fuses and tested combination motor controllers to raise the panel’s SCCR without oversizing the assembly. Specify UL 1059 terminal blocks with the correct use groups and spacing and lay out the enclosure so power and control sections are separated, heat is managed, and service access is clear. These practices help reduce downtime throughout the panel’s life. Common Mistakes That Lead to Red Tags, Rework, or Downtime Marking an SCCR that is lower than the available fault current at the installation point. Misapplying supplementary protectors in place of branch protection. Using components without verifying their conditions of acceptability in Product iQ. Relying on outdated tables or assuming IEC ratings are equivalent to UL requirements in North America.   UL 508A vs Related Standards Topic Primary UL or IEC Standard When It Applies Industrial control panels in ordinary locations UL 508A General ICP product standard in North America Switchboards UL 891 Power distribution switchboards Motor control centers UL 845 MCC lineups Fire alarm control units UL 864 Life safety fire alarm equipment Panels with intrinsically safe circuit extensions into hazardous locations UL 698A ICPs related to hazardous locations Assemblies in IEC markets IEC 61439 Low-voltage switchgear and control gear assemblies Industrial machinery installation NFPA 79 / IEC 60204-1 Electrical equipment of machines   Frequently Asked Questions about UL 508A What does UL 508A mean? It is the safety standard used to evaluate industrial control panels for ordinary locations at 1000 V or less, including construction, components, markings, and documentation. Is UL 508A mandatory in industrial settings? There is no blanket federal law that makes it mandatory. In practice, AHJs and insurers often require listed equipment or a field evaluation. NEC 409 requires SCCR marking, and OSHA 1910.303 requires equipment to be “approved.” What is a UL 508A control panel? An assembly containing power and control components evaluated to UL 508A, installed in ordinary locations. It is not the same as a switchboard or Motor Control Center (MCC). What are the requirements for UL 508A certification? Use suitable components per Supplement SA, meet construction and spacing rules, establish SCCR per Supplement SB, apply required markings, and maintain documentation. Shops that participate in the Industrial Control Panel Shop Program  are audited and trained to apply the standard. What components are permitted in a UL 508A listed panel? Components must be UL Listed or UL Recognized for the intended use with appropriate conditions. Examples include UL 489 circuit breakers, UL 98 disconnects, UL 1059 terminal blocks, and UL 60947 motor controllers. What is SCCR and how is it established? SCCR is the panel’s withstand rating for short-circuit events. It is established using UL 508A Supplement SB tables and tested combinations, then marked per NEC 409. What are the benefits of using UL 508A listed panels? They streamline inspections, reduce risk through appropriate protective coordination and SCCR, and provide clear documentation for maintenance. What are the benefits of working with a UL 508A certified panel fabricator? Panel shops in the UL program have been audited and trained to apply the standard and can apply the UL certification mark under general coverage. What recent changes have happened in UL 508A? The June 26, 2025 revision adds control circuit voltage limits at 120 Vac and 250 Vdc, adjusts E-Stop expectations, clarifies disconnecting means for industrial machinery, corrects Table SB4.1, and updates terminal block and group motor overload provisions. What is the difference between UL and ISO? UL publishes and administers product safety standards and certifications for equipment. ISO publishes management system and other international standards that focus on how organizations operate. Ultimately, they address different scopes. What is the difference between IEC and UL 508A? IEC 61439 covers assemblies in IEC markets and IEC 60204-1 covers machinery. UL 508A is the North American product standard for ICPs. There is no one-to-one equivalency, so designs often need adaptation for each regime. What is the difference between UL 589 and UL 508A? UL 589, in its current joint form with ULC as CAN/ULC 589, covers single and multiple station heat alarms. It is unrelated to industrial control panel construction, which is covered by UL 508A. How do UL 508A and NFPA 79 interact? UL 508A governs panel construction and evaluation. NFPA 79 governs the electrical equipment of industrial machinery as installed and operated. Both are commonly applied . How do I verify a shop’s UL 508A capability or a component’s status? Ask for the shop’s UL file number and check UL Product iQ , which is the certification database used by engineers and AHJs.   What to Prepare Before You Talk to a UL 508A Control Panel Fabrication Partner Having the following items on hand before reaching out to a UL 508A certified control panel fabricator  can make the process both smoother and less time consuming.   Available fault current at the planned installation point and any utility short-circuit study excerpts. Target SCCR for the panel and any upstream device limitations. Environmental rating needs such as NEMA 4X, corrosion resistance, or temperature requirements. One-line diagram or power distribution sketch. Motor and heater loads, starting methods, and protective device preferences. Control circuit voltages and any safety relays or networked I/O. Interfaces to Fire and Gas, building fire alarm, or intrinsically safe circuits. Preferred vendor lists for breakers, disconnects, terminals, and PLC hardware.   The Takeaway If your industrial facility needs to procure or specify industrial control panels in North America, UL 508A is the product standard that aligns your design with the NEC and gives AHJs a clear basis for acceptance. Getting SCCR right, selecting suitable components, and understanding the 2025 updates reduces risk and smooths inspections. If you need a UL 508A-certified panel fabrication shop, aeSolutions maintains that capability and can integrate panels with Fire and Gas systems and other safety-critical applications, while keeping the focus on code compliance, maintainability, and operational resilience.

aeSolutions Erich Zende helps his FIRST Robotics Team with their robot. Nice pants Erich! Pictures courtesy of FRC Flash 1319 As insightful as conventional high school career aptitude surveys with pen and paper can be — hands-on, real world experience is instrumental in shaping capable young minds. Add high stakes adrenaline and stiff competition to the equation, and FRC Flash 1319 Robotics Team emerges as a fusion between the three. This FIRST (For Inspiration and Recognition of Science and Technology) Robotics team hails from Greenville, SC and competes in state and national level field games under the adept guidance of mentor and aeSolutions SIS FEL Specialist, Erich Zende. We conducted an informal interview with Erich at the close of the team’s regular season to discern a better understanding of the year-round volunteer effort he lends so much of himself to . aeSolutions: What is your role on the FRC Flash 1319 team? Erich Zende: I am the Lead Mechanical Design Mentor and Drive Team Coach for the robotics team. I lead the students through the design, prototype, and build phases during a six-week build season, and I also advise students on the safe use of tools and other safety procedures. Pictures courtesy of FRC Flash 1319 aeSolutions: The advisory role concerning proper tool usage and safety procedures makes sense, given that safety is one of the fundamentals that embodies the spirit of aeSolutions. How much of your personal resources (time, money, energy) do you invest per season? Erich Zende: During the build season I meet with the students for roughly 30 hours a week, for six weeks, and during the weeks leading up to the competitions I meet with students somewhere between 20-30 hours. The majority of this time is spent practicing with a prototype robot along with packing spares and tools for the competition, as well as going over the presentations prepared by students for the judged technical awards at completion. Typically, FRC Flash 1319 competes at 2 or 3 select events. In total, I contribute an overall average of 250 hours give or take. In order to mentor to my fullest ability, I contribute 8-10 days of my time- off-with-pay, my hotel rooms expenses, occasional robot parts, and a trailer to transport the team’s robot. Pictures courtesy of FRC Flash 1319 aeSolutions: It goes without saying that you volunteer in multiple capacities. In regards to the season ending though, what does the “off-season” look like when the team isn’t gearing up for the building phase and qualifier competitions? Erich Zende: In the time period that we refer to as the “off-season,” I focus my time on recruiting and training new members. In regards to a combined effort, the team attends outreach events in addition to hosting several Lego League tournaments for the younger students interested in S.T.E.M. activities. Recently we hosted an event with one of our sponsors, the Synnex Corporation, to put on a STEAM (Science, Technology, Engineering, Arts and Math) Girls Night Out. This was a Makerspace event created to inspire, empower and engage girls in grades 3rd to 8th in Greenville County. The goal was to help foster young girls’ appreciation for STEAM and raise STEAM awareness among parents. The event boasted an overall attendance exceeding 350 students. Aside from requested team demonstrations at Roper Mountain Science Center, we also take part in the IMAGINE Upstate Annual Festival; which showcases pre-K through 12th grade education and STEAM career pathways centered on having fun and hands-on learning. Pictures courtesy of FRC Flash 1319 aeSolutions: Given what you’ve told me, the season isn’t necessarily limited to building and competing for a span of a few months but rather it’s a year-round effort of recruiting, team building and spreading awareness. It’s clear what you give to the program and the impact you have on the malleable futures of these students, but what do you get out of this exactly? What keeps you coming back year after year? Erich Zende: There are many reasons why I continue to mentor. Although challenging for a variety of reasons, the rewards generally make it all a worthwhile endeavor each and every year. Speaking of years, this will be my 16th year as a mentor and 20th year participating in FIRST Robotics. To be more specific: I mentor because others mentored me. I mentor to hopefully aid and impact future generations of students who will be contributing members of our society. I learn something new every year, and I enjoy the competitive experience. I mentor because the robotics team is a creative outlet outside of my day job. And truly, I mentor because I yearn for my daughter to have a long-standing and well-developed STEM program to be a part of when she is older. Pictures courtesy of FRC Flash 1319 aeSolutions: Well said. Special thanks to Erich Zende for the continued efforts and contributions to this FIRST Robotics team. You have not only gone above and beyond for the robotics team, but you have also created a praiseworthy legacy that speaks to the very core of this company. More information on FIRST Robotics Click here to keep up with Erich Zende and the FRC Flash 1319, visit the team website Or follow them on social media: https://www.facebook.com/pg/FRCFlash1319 https://twitter.com/FRCFlash1319 https://www.instagram.com/frcflash1319/ https://www.youtube.com/channel/UCG40LSBnquEsIMQ2hyiyv8w #aesolutions

There are many devices (sensors, logic solvers and final elements) used in safety instrumented systems  that are independently certified for use in safety applications to different safety integrity levels (SIL). There is considerable debate however whether fire and gas system hardware should have SIL ratings at all. Vendors are naturally interested in promoting independently certified hardware in order to differentiate their products. Considering the differences between safety instrumented systems and fire and gas systems, focusing on the SIL rating or performance of the actual fire and gas hardware  alone is considered by some to be a misleading and questionable practice. This paper reviews a) the differences between safety instrumented systems and fire and gas systems, b) how typical voting of fire and gas sensors not only reduces nuisance trips (which is desirable) but also reduces the likelihood of the system actually responding to a true demand (which is not desirable), and c) why concepts and standards that apply to safety instrumented systems (e.g., SIL ratings) may not be appropriate for fire and gas systems . Click here for the complete whitepaper ​