Author: Brian D. Chapin (Page 4 of 13)

Known as the "PSM Evangelist" and the "Jon Taffer of Ammonia PSM," I have taught over 1,000 people how to implement PSM/RMP in their Ammonia processes. It is my honor and privilege to work with the finest minds in the industry. I fuse Six Sigma / Lean / Kaizen philosophy with PSM/RMP to minimize compliance burdens and maximize the safety & efficiency gains of a properly implemented program.

Here are some highlights:

- Designed, Built and Continuously Improved OSHA Process Safety Management, EPA Risk Management and Process Hazard Analysis Programs for Industrial Ammonia Refrigeration systems all over the country.

- Comprehensively audited OSHA Process Safety Management, EPA Risk Management in facilities throughout the United States in facilities of all sizes from 10,000 pounds to over 300,000. Processes ranged from Ammonia Refrigeration to N02 reduction and Synthetic Rubber production.

- Lead Author and Project Manager for the book “Implementing Process Safety Management for Ammonia Refrigeration” used as the textbook for teaching PSM for over 100 companies a year.

- Through FOIA, I have read the citations, 1B's and narratives to every PSM citation issued by OSHA from 2008-2013.

- Managed Refrigeration Projects including Expansions, System Optimization and Capital Projects.

- Acted as HazMat Incident Commander and Team Member.

- Skilled in Incident Investigation and Root Cause Analysis.

- Background in Six Sigma, Lean and Kaizen implementation in manufacturing.

- Familiar with ISO 9000 & SQF programs.

- Organized CMMS (Computerized Maintenance Management System) Implementation.

- P&ID creation and modification.

- Completed many projects in Energy Conservation and System Optimization of Refrigeration Systems.

IIAR 2 202x Public Review 1

The IIAR has released a proposed draft of IIAR 2 Safety Standard for Design of Closed-Circuit Ammonia Refrigeration Systems for public review. Here’s the notice:

March 20th, 2020

To:

IIAR Members

Re:

First (1st) Public Review of Standard BSR/IIAR 2-202x, Safety Standard for Design of Closed-Circuit Ammonia Refrigeration Systems.

A first (1st) public review of draft standard BSR/IIAR 2-202x, Safety Standard for Design of Closed-Circuit Ammonia Refrigeration Systems is now open. The International Institute of Ammonia Refrigeration (IIAR) invites you to make comments on the draft standard. Substantive changes resulting from this public review will also be provided for comment in a future public review if necessary.

BSR/IIAR 2-202x specifies the minimum safety criteria for design of closed-circuit ammonia refrigeration systems. It presupposes that the persons who use the document have a working knowledge of the functionality of ammonia refrigerating system(s) and basic ammonia refrigerating practices and principles. This standard is intended for those who develop, define, implement and/or review the design of ammonia refrigeration systems. This standard shall apply only to closed-circuit refrigeration systems utilizing ammonia as the refrigerant. It is not intended to supplant existing safety codes (e.g., model mechanical or fire codes) where provisions in these may take precedence.

IIAR has designated the revised standard as BSR/IIAR 2-202x. Upon approval by the ANSI Board of Standards Review, the standard will receive a different name that reflects this approval date.

We invite you to participate in the first (1st) public review of BSR/IIAR 2-202x. IIAR will use the American National Standards Institute (ANSI) procedures to develop evidence of consensus among affected parties. ANSI’s role in the revision process is to establish and enforce standards of openness, balance, due process and harmonization with other American and International Standards. IIAR is the ANSI-accredited standards developer for BSR/IIAR 2-202x, and is responsible for the technical content of the standard.

This site includes links to the following attachments:

The 45-day public review period will be from March 20th, 2020 to May 4th, 2020. Comments are due no later than May 4th, 2020.

Thank you for your interest in the public review of BSR/IIAR 2-202x, Safety Standard for Design of Closed-Circuit Ammonia Refrigeration Systems.

There are MANY proposed changes. I’ll include a full list of the proposed changes at the end of the post, but here are some highlights:

  • Requirements for System Signage became a little simpler
  • Ammonia detection requirements have changed
    • Most installations now need two detectors in a machine room
    • Installation & Testing for detectors outside machine rooms now refer to external RAGAGEPs.
    • “Level 1” detection now requires liquid & hot gas shutoff at 150ppm
    • Requires AHJ approval if not installing ammonia detection in “Areas Other than Machinery Rooms”
  • New requirements for permanently installed Hoses and Corrugated Metal Fittings to ensure they meet ISO 10380 or ARPM IP-14

 

It’s important that YOU read these changes and make your voice heard if you have any input on them. 

 

Full change list of the normative sections of the standard below…


Continue reading

IIAR releases new ANSI/IIAR 9 standard

What you need to know about the new standard IIAR 9

IIAR 9-2020 has been officially released.

This is a new standard and it will require you to do certain things differently going forward.

 

What is it?

This document is a standard for minimum system safety requirements for existing closed-circuit ammonia refrigeration systems. The safety focus is on persons and property located at or near the premises where the refrigeration systems are located…

This standard provides a method to determine if existing stationary closed-circuit refrigeration systems using ammonia as a refrigerant comply with minimum system safety requirements.

For practical purposes it’s a way to deal with a system designed under an older RAGAGEP that doesn’t necessarily require you to update to the latest version of IIAR 2.

 

What’s the problem it’s solving?

How do you build a defensible case that your system built to an older code or standard is still designed, maintained, inspected, tested, and operating in a safe manner if it doesn’t meet the current code or standard? In PSM I refer to this issue as the d(3)(iii) trap. Here’s the relevant law:

1910.119(d)(3)(iii) For existing equipment designed and constructed in accordance with codes, standards, or practices that are no longer in general use, the employer shall determine and document that the equipment is designed, maintained, inspected, tested, and operating in a safe manner.

The way we traditionally did this is in the PHA where we either recommended the facility upgrade to conform to the latest version of the code or standard, OR has the PHA team build a defensible case that the alternative arrangement in the as-built / existing system was at least as safe as meeting the new code or standard. As you can imagine, this was not an easy thing to do.

 

How does this new standard affect me?

First, if you are already compliant with the current RAGAGEP (such as IIAR 2-2014a) then nothing much changes for you. If you are not compliant with the current IIAR 2 then it provides a different fallback position, because if you meet the requirements in IIAR 9, you now have an ANSI certified RAGAGEP that helps you defend the decision not to update to the current code or standard. Put another way: If your system is designed to IIAR 2-1999, then you might be able to use IIAR 9-2020 as an alternative to compliance with IIAR 2-2014a. 

Put in a flowchart, it looks like this:

Please note: this does not change NEW additions and systems – they are evaluated under current RAGAGEP. 

 

Is there anything else it requires?

The new standard requires an initial evaluation for IIAR 9 compliance within 5 years. It also requires that you re-evaluate that IIAR 9 compliance every 5 years thereafter.

 

How should I comply?

As with all compliance topics, there are lots of ways to get from here to there. I’m going with the EASIEST method which is: incorporate this analysis in your PHA. The requirements for evaluation methodology allow for a semi-quantitative technique for risk-ranking which is what you are already doing if you are using traditional IIAR PHA What-If / Checklist methodology.

To that end, I’ve converted every requirement in IIAR 9-2020 to a Checklist and included that checklist in with the existing PHA checklists for IIAR 2 compliance.

So, the next time you revalidate your PHA, if you use the new PHA templates you will automatically be performing this new required IIAR 9 evaluation. I’ve updated the PHA report template, the PHA worksheets, the PSI RAGAGEP letter templates, and the MI-EL1 to reflect these changes as well. Check the template change-log for details. 

Service Technician & PSM Coordinator Bulletin: COVID-19 and YOU!

I know you’re busy and probably a little concerned about this COVID-19 outbreak. It’s important that you understand a few things about it because YOU are on the frontlines of our economy while this is unfolding AND its recovery once this event passes. YOU keep the foods, beverages, and medicines our society relies on SAFE.

Because your time is valuable, I’ve assembled what you need to know in less than a five-minute read:

 

What it is:

A virus that is spread through close contact with infected persons or contaminated surfaces, and through the air by respiratory droplets produced during coughs and sneezes. As with seasonal “colds,” the most severe impacts seem to be to those with compromised immune systems, damaged lungs, and the elderly.

 

What are the symptoms:

Symptoms usually appear 2-14 days after exposure.

  • Fever
  • Cough (usually dry)
  • Shortness of breath.

 

Your action to take:

The CDC (Center for Disease Control) has issued guidance and they continue to update their guidance daily.

To protect yourself against infection, the World Health Organization (WHO) recommends:

  • Washing your hands regularly with soap and water for 20 seconds, and using alcohol-based sanitizer
  • Maintaining distance of at least 2 meters (6 feet) between yourself and anyone who is coughing or sneezing
  • Avoiding touching your eyes, nose and mouth
  • Seeking medical care immediately if you are showing symptoms (though some facilities ask that you call your medical facility for instructions before coming to their office).

 

When should I seek medical attention?

If you develop emergency warning signs for COVID-19 get medical attention immediately. Emergency warning signs include:

  • Difficulty breathing or shortness of breath
  • Persistent pain or pressure in the chest
  • New confusion or inability to arouse
  • Bluish lips or face

 

NOTE: This is NOT meant to be a comprehensive overview. It’s meant to provide clear, simple, actionable information for people that have other things to do with their lives. More information can be found at the CDC  and WHO.

You can download this information in a one-page PDF for posting.

032120 Update: OSHA has published OSHA 3990, Guidance on Preparing Workplaces for COVID-19.

CSB’s NEW Chemical Incident Reporting Rule is FINAL

“U.S. Chemical Safety Board and Hazard Investigation Board (CSB) has approved a final rule on accidental release reporting. The CSB has posted a prepublication version of the final rule… The official version should be published early next week in the Federal Register.

The rule requires prompt reports to the CSB from owners or operators of facilities that experience an accidental release of a regulated substance or extremely hazardous that results in a death, serious injury or substantial property damage. The CSB anticipates that these reports will provide the agency with key information important to the CSB in making prompt deployment decisions…

The rule is required by the CSB’s enabling legislation but was not issued during the first 20 years of CSB operations. Last year, a court ordered the CSB to finalize a rule within a year. “

What it means: If the incident resulted in Death, Serious Injury or Substantial Property Damage ($1kk or more) then you have to report the incident to the CSB (via phone 202- 261-7600 or email [email protected]) within 30 minutes. The report must include:

1604.4 Information required in an accidental release report submitted to the CSB
1604.4 The report required under §1604.3(c) must include the following information regarding an accidental release as applicable:
1604.4(a) The name of, and contact information for, the owner/operator;
1604.4(b) The name of, and contact information for, the person making the report;
1604.4(c) The location information and facility identifier;
1604.4(d) The approximate time of the accidental release;
1604.4(e) A brief description of the accidental release;
1604.4(f) An indication whether one or more of the following has occurred: (1) fire; (2) explosion; (3) death; (4) serious injury; or (5) property damage.
1604.4(g) The name of the material(s) involved in the accidental release, the Chemical Abstract Service (CAS) number(s), or other appropriate identifiers;
1604.4(h) If known, the amount of the release;
1604.4(i) If known, the number of fatalities;
1604.4(j) If known, the number of serious injuries;
1604.4(k) Estimated property damage at or outside the stationary source;
1604.4(l) Whether the accidental release has resulted in an evacuation order impacting members of the general public and others, and, if known:
1604.4(l)(1) the number of persons evacuated;
1604.4(l)(2) approximate radius of the evacuation zone;
1604.4(l)(3) the type of person subject to the evacuation order (i.e., employees, members of the general public, or both).

The good news is that if you have to report the incident to the NRC then you can skip reporting all the above data and simply report the NRC case number you’re given during the NRC call.

This new requirement takes effect 30 days from the posting in the Federal Register so ACT NOW. It’s important that you update your program because there are enforcement penalties associated with not following this new rule…

1604.5(b) Violation of this part is subject to enforcement pursuant to the authorities of 42 U.S.C. 7413 and 42 U.S.C. 7414, which may include
1604.5(b)(1) Administrative penalties;
1604.5(b)(2) Civil action; or
1604.5(b)(3) Criminal action.

 

What should I do? 

If you use the template program, the hard work has already been done FOR YOU. Just open up the template directory on Google Drive and follow these steps for your program:

  • In \Reference\ add new directory \Reference\CSB\ and place “CSB Reporting Accidental Releases – prepublicationcopy 020320.pdf” in it. You can get it from the templates directory or from the EPA link.
  • In \Reference\CFR\ add “40CFR1604 – Hazardous substances Reporting and recordkeeping requirements.doc” from the templates directory.
  • Update the Incident Investigation element Written Plan to the 020720 version from the templates directory.
  • Update the \01 – EPA RMP\ Definitions file to the 020720 version from the templates directory.
  • Train all Responsible Persons and affected management on the new policies.
  • Document the changes in your DOC-Cert in accordance with the Implementation Policy: Managing Procedure / Document Changes found in the MOC/PSSR element Written Plan.

Note: If you have instructions for Agency Notifications somewhere outside your Incident Investigation plan, you’ll need to update them to include the CSB contact information there too. Feel free to use the text in the Incident Investigation element Written Plan, Implementation Policy: Agency Notifications.

 

A little help can go a long way!

Sometimes a little extra can go a long way to improve the effectiveness of your compliance efforts. I would like to show you how we used two simple, inexpensive laminated cards to improve the effectiveness of our APR inspections and Incident reporting / reactions.

APR Card

First, the APR issue:1910.134 has some requirements on inspections, cleaning, fit-check, etc. We require our service technicians to wear APR’s during Line-Opening. I created a small laminated card (about 5″x8″) that fits in their APR bag. With the included permanent marker, we can track the APR inspections for a year. The card also provides convenient information on the “Fit-Check” and “Monthly Inspection” procedures. Here’s the WORD document if you want to modify it for your use.

 

Leak Investigation / Incident Reporting

Our technicians are often called to look into reported ammonia odors. We’ve established a policy on doing this in compliance with 1910.119(n) concerning “handling small releases.” We also conduct Incident Investigations to meet the requirements of 1910.119(m). Again, I created a small laminated card (about 5″x8″) that fits in their APR bag.  It provides a quick-reference to the investigation procedure, as well as reminders of the information we’ll be asking them for. Contact numbers for company safety/compliance resources are also included. Here’s the WORD document if you want to modify it for your use.

 

Little items like this can reinforce your training. The easier “being compliant” is, the more likely it is to happen in the field! 

p.s. The Word documents are meant to be printed double-sided. I use 32# paper, trim, then seal with 5mil clear laminating envelopes. 

Why use the “buddy system” during Line Openings?

Most LEO (Line & Equipment Opening) policy a.k.a. “Line Break” policies require a second person away from the work but in the immediate area. It is reasonable to ask why the procedure demands this.

Put as simply as possible:

  1. PSM/RMP and IIAR 7 require procedures for Line & Equipment Openings. (or IIAR 7 alone if you have under 10k pounds)
  2. The PHA asks questions that identify hazards which result in administrative controls aka procedures. Those procedures will have to control the unique hazards identified in the PHA.
  3. RAGAGEP for procedures (such as IIAR 7) require the buddy system be addressed in Line & Equipment Opening procedures.
  4. HazMat & Firefighting history show it is useful.
  5. Human Nature tells us that people tend to hold each other accountable.

 

Let’s work through this step-by-step

1. PSM/RMP requires us to have a procedure:

1910.119(f)(4) The employer shall develop and implement safe work practices to provide for the control of hazards during operations such as lockout/tagout; confined space entry; opening process equipment or piping; and control over entrance into a facility by maintenance, contractor, laboratory, or other support personnel. These safe work practices shall apply to employees and contractor employees.

Put another way: We have to develop a written procedure on Line & Equipment Openings which everyone must follow.

 

2. Hazards identified during a PHA are often controlled with Administrative controls, such as SOPs. SOP content therefore must address the hazards identified in the PHA. Some examples:

…the Ammonia exposure increases while the operator is using an APR/SCBA? (II.8) This is what makes us mandate the use of a personal NH3 detector during line openings and leak investigations.

…there is inadequate isolation prior to maintenance? (HF.3) …the Ammonia pump-out for a length of piping or for a piece of equipment is incomplete? (PO.1) This is why SOPs include a pressure check to confirm pumpdown. This is also why the LEO procedure (and permit) require a written SOP & permit to check the effectiveness of the procedure.

…an injured worker is unable to summon assistance? (HF.56) This (among other reasons) is why we require a Buddy System. The LEO policy, in the General Precautions section, states “A buddy-system is used for all LEO procedures. The second person must be trained to initiate emergency action and must be stationed close enough to observe the activity but far enough away to ensure that they would not be endangered by an accidental release.”

 

3. The RAGAGEP for procedures IIAR 7-2019 has this requirement:

4.4.2 Buddy System. Operating procedures shall indicate when the buddy system shall be practiced in performing work on the ammonia refrigeration system

A4.4.2-The buddy system should be practiced for operations where there is the potential that ammonia could be released, for example, operations which involve opening ammonia refrigeration equipment or piping. The buddy system should also be practiced during emergency operations involving ammonia releases.

 

4. HazMat & Firefighting history: Hazardous Materials teams and Firefighters have long used a 2-person team for increased safety. To some degree, this is enshrined in OSHA rules in 1910.134(g)(3)…

1910.134(g)(3) Procedures for IDLH atmospheres. For all IDLH atmospheres, the employer shall ensure that:

1910.134(g)(3)(i) One employee or, when needed, more than one employee is located outside the IDLH atmosphere;

1910.134(g)(3)(ii) Visual, voice, or signal line communication is maintained between the employee(s) in the IDLH atmosphere and the employee(s) located outside the IDLH atmosphere;

While we don’t INTEND to work inside a IDLH atmosphere during a LEO procedure, the possibility certainly exists if something goes wrong. The “buddy system” allows the person performing the LEO to focus on the work while the second person remains in the area situationally aware and ready to respond in the event that the situation changes or something goes wrong.

 

5. Human Nature: The LEO policy is written around accountability. The policy requires that we demonstrate to a second person that we’ve followed the policy and adequately prepared for the work before the LEO occurs.  The “buddy system” tends to keep the actions “in-line” during the actual work.

Note: While it’s certainly possible  – from a regulatory view – that you could have certain specific LEO procedures that did not require a “buddy,” you would have to be able to document how you managed to address all of the issues outlined above without the second person.

Thanks to Bryan Haywood of SaftEng.net and Gary Smith of ASTI (Ammonia Safety Training Institute) for their time and thoughts in helping review this post.

OSHA fines getting more expensive again!

The Obama administration signed the Federal Civil Penalties Inflation Adjustment Act Improvements Act of 2015 which requires OSHA to adjust their fine amounts for inflation. 2020’s numbers are in: OSHA will adjust the fines by the  Consumer Price Index cost-of-living adjustment multiplier of 1.01764 which turns into a $230 increase for Serious and a $2300 increase for Willful / Repeat. The table below shows the new penalty amounts.

 

 

Memo File:  2020 OSHA Annual Adjustments

Trump EPA goes LIVE with new RMP rule: Is this finally the end of the saga?

The story so far…

Dec 2016: Outgoing Obama EPA releases changes to the RMP rule on the way out the door.

Apr 2017: Incoming Trump EPA puts the RMP rule changes on hold.

Jun 2017: Trump EPA further delays the RMP rule changes.

May 2018: Trump EPA proposes new RMP rule changes, reversing Obama changes.

Aug 2018: DC District Court reverses Trump Rule and re-instates Obama rule essentially making it the existing rule with compliance dates in the past. Trump EPA is basically told that it can change the rules, but it needs to follow different procedures to do that. Trump admin appeals and the rule changes are put on hold.

Sep 2018: Trump admin loses appeals. Obama RMP rule changes are officially LIVE. Trump EPA announces that they will follow the different procedures and change the rule the right way. (Not-so-secretly, the entire EPA is told NOT to enforce the new rule, but out of an abundance of caution, most RMP adherents implement the changes anyway. After all, it IS the law.)

Dec 2019: Trump EPA officially posts the new rule and places it in the CFR making it LIVE on 12/19/19. (See links at the end of the post)

 

So, where do we stand now?

Ok, we’ve got a new RMP rule. It appears to have gone through the correct rulemaking process. It’s been published in the Federal Register making it the law of the land.

 

So, what do we do now?

Well, let’s be honest; the Trump administration IS GOING TO GET SUED over this. What happens then? Who knows!? If you follow the courts in modern America, you know there is very little that can be accurately forecasted.

What we do know is that we have a new rule. The new rule appears to have been done correctly with sound documentation as to the reasoning for the changes. In my opinion, the new rule will LIKELY hold up in court. Even if it doesn’t, it is highly unlikely the EPA could get away with fining / citing people for not following a court-reinstated rule under such a cloud of confusion.

In any case, the new rule is easier to follow and makes more sense than the Obama EPA rule changes did. It reverts the majority of the RMP rule to match the PSM rule where they SHARE jurisdiction. The only substantive changes are to the EPA-specific areas where the EPA alone holds jurisdiction.

 

Ok, so how do I comply with this new rule?

If you do use our template system, I’ve got some good news for you! This is where using a set of open-sourced, professionally curated templates really shines. ALMOST ALL THE WORK has been done FOR YOU!

  • To improve your understanding of the new rule, read how we changed the program to meet the new requirements. This will help you to train your colleagues on them.
  • Replace existing copies of the affected Written Plans / Forms, taking a moment to look at the changes between the older versions and the new ones.
    1. Implement new EAP-C form.
    2. Modify the MI-EL1 EAP/ERP line to reflect the new text.
  • Train all Responsible Persons and affected management on the new policies.

Note: Estimated time for the above is about 2-4 hours depend on how well you know your PSM/RMP program.

 

On the other hand, If you don’t use our template system, you’re going to have to re-create the work I’ve already done:

  • Skip to the end of this article to get the links to the new information.
  • Read the 83-page Federal Register notice and make a series of notes about the new requirements. You can probably skip the 109 footnotes for now.
  • Compare those new requirements to the version of the RMP rule your program is CURRENLY written to comply with; whether that’s the pre-Obama, Obama, or Trump proposed version.
  • Starting at the beginning of your program, read through each of your Element Written Plans and see what changes have to be made. Refer to your notes from the first step. (You may wish to read how we changed our program to meet the new requirements)
  • Update / alter your program to meet these new requirements.
  • Train on these new changes

Note: Estimated time for the above is about 40-80 hours depend on how well you know your PSM/RMP program and the EPA RMP rule.

 

Template Program changes in detail

Please note, where not specifically shown below all affected Element Written Plans had their CFR section updated to the current 12/19/19 CFR.

Element What Changed Changes to Program Templates
01 – RMP
  1. A few definitions were deleted
  2. Some compliance dates and RMP references were changed
  3. Various Program 2 Changes
  4. Public meetings changes
  5. RMP Filing changes regarding 3rd party compliance audits, public meetings, etc.
  6. Removed significant amounts of publicly available information
  1. As our definition file isn’t limited to EPA sources, no changes were made to the template program documents.
  2. Previously there were sections about the Obama-era law that had a 2021 date tag – these sections were either deleted (because they were removed) or the date tag was removed.
  3. The element written plans are designed around Program 3, so no changes were made in them however all relevant CFR sections were updated.
  4. Updated the Element Written Plan to address these issues
  5. Updated the CFR to reflect the changes.
  6. Updated the Element Written Plan to address these issues
02 – EP N/A None
03 – PSI
  1. Removed the explicit requirement to keep PSI up to date.
  1. While we updated the CFR text, this is sort of implicit in the MOC/PSSR program and the very nature of PSM, so no changes made to the Element Written Plan.
04 – PHA
  1. Removed a nebulous requirement to look for “any other potential failure scenarios”
  2. Removed a section on alternative risk management for chemical / petro plants.
  1. While we updated the CFR text, this is sort of implicit in the idea of a PHA, so no changes were made in the Element Written Plan.
  2. These changes did not cover the NH3 refrigeration industry, so no changes were needed in the Element Written Plan.
  3. Since the explicit PSI “up to date” requirement was removed from the PSI section, it was removed from the PSI checklist in the PHA What-If checklists.
05 – SOP N/A None
06 – OT
  1. Removed an explicit requirement that “supervisors with process operational responsibilities” were covered under this program.
  1. We believe that operators under this element are defined by their function not their title / job position, so no changes were needed in the Element Written Plan.
07 – CQ N/A None
08 – MI No changes to RMP requirements
  1. The MI-EL1 section covering recurring PSM tasks in EAP/ERP was updated to remove the 2021 date codes. While the 10yr Field Exercise frequency is now just a suggestion (rather than a mandate) we’ve kept it in as a good practice.
09 – HW N/A None
10 – MOC / PSSR No changes to RMP requirements
  1. The procedural section “Implementation Policy: Managing Equipment / Facility Changes and using form MOC-1” includes a chart on possible changes to RMP-required information based on an MOC. The reference to “public information” has been removed from this chart.
11 – II
  1. Removed explicit requirements for incident location, time, all relevant facts, chronological order, amount released, number of injuries, etc.
  2. Removed a requirement that Incident Investigations be completed within a year
  1. While we removed these requirements from the CFR section, we believe they are still important for Incident Investigations and they’re already required by relevant RAGAGEP, so no changes were made to the Element Written Plan, the investigation instructions, or the Form-IIR Incident Investigation form.
  2. While we can’t imagine this wouldn’t occur naturally in a functioning process safety program, we removed the requirement. The program – as written – already suggests interim reports when investigations are lagging.
12 – EPR
  1. Lots of changes here: Modified information sharing requirements with responders, modified frequency of field exercises, modified scope of field and tabletop exercises, documentation requirements, compliance dates, etc.
  1. These changes were all incorporated in the Element Written Plan.
  2. To improve program performance, a new form was created “EAP-C Local Authority Coordination Record.” This form was also included in the Element Written Plan.
13 – CA
  1. Removed requirements for 3rd party audits
  1. These changes were all incorporated in the Element Written Plan.
14 – TS
  1. Modified text in the “CBI” section to reflect new wording in the updated rule.
  1. While it’s been changed in the CFR text, it requires no change to the Element Written Plans.

Item-by-Item changes:

  • Reference\EPA Reference\ has been updated with a PDF of the Register Notice.
  • Reference\CFR – Text of Federal Rules\ has been updated with a complete and formatted CFR reflecting the new changes.
  • The various element affected template directories have been updated with Element Written Plans that incorporate the new CFR text AND modified policies to comply with the rule changes
    • 01 – EPA RMP
      • Element Written Plan – REPLACE
    • 03 – Process Safety Information
      • Element Written Plan – REPLACE
    • 04 – Process Hazard Analysis
      • Element Written Plan – REPLACE
      • PHA Worksheet Template – REPLACE
    • 06 – Operator Training
      • Element Written Plan – REPLACE
    • 08 – Mechanical Integrity
      • MI-EL1 Form updated. You may just wish to modify the EAP/ERP line to reflect the new text rather than re-create the form.
    • 10 – Management of Change and PSSR
      • Element Written Plan – REPLACE
    • 11 – Incident Investigation
      • Element Written Plan – REPLACE
    • 12 – Emergency Planning and Response
      • Element Written Plan – REPLACE
      • NEW Form EAP-C – Implement
    • 13 – Compliance Audits
      • Element Written Plan – REPLACE
      • Optional Combined PSM RMP Compliance Self-Audit Checklist – REPLACE
    • 14 – Trade Secrets
      • Element Written Plan – REPLACE

 

EPA links for new information:

  • Updated CFR (aka “law”) from eCFR: link (37 Pages)
  • Federal Register Notice including reasoning for changes: link (83 Pages)

New Year, “New” SOP Format

The spirit of Christmas may be behind us, but the spirit of Continuous Improvement never leaves us alone. (for better or worse, lol)

After months of minor changes and revisions off-line, the 2020 SOP templates have been released. Please note: These are IMPROVEMENTS, not compliance or safety-critical changes. As such, there is no need to go back and change your existing SOPs. We would, however, suggest you use these new formats as you implement new SOPs. Of course, it’s possible, you may want to take advantage of some of the features of these new SOP templates, and you’re welcome to convert to them if you have the time.

Changes to ALL SOP Templates:

  1. Moved “Covered Equipment” to “Objective” section which eliminates Document Info section.
  2. Moved “Related Documents” to “Objective” which eliminates Related Documents section.
  3. Removed “SOP Objective” from first section as the objective is repetitive and explained clearly in the Written Plan. (It’s the first text box of the SOP so it’s fairly obvious what the function is!)
  4. Made Safety Warning triangle smaller and made the warning RED. This change (among others) frees up a bit of room for the Safety, Health, Environmental and Equipment Considerations section
  5. Moved the Operator Requirements concerning authorization to the top of the Safety, Health, Environmental and Equipment Considerations section thus eliminating the Operator Requirements section. Also provided a callout to the operator to check their OT1 to ensure they’re qualified to perform the procedure.
  6. Modified the Operating Phase flowchart section layout to take up less space.
  7. Minimized the left-hand column which shows what “Section” you are in to 1” width to take up minimal space. Centered the section text.
  8. Placed Headings between sections. This required splitting up the various Operating Phase / Procedural sections but makes navigation much easier if being used in WORD or PDF format.
  9. Added complementary color to enlarged text “body” sections of Operating Phase / Procedural Sections.
  10. Valve / Component List given a header. Sub-header appropriately colored.

Why did we make those format changes?

  1. Those changes yield a slightly shorter SOP format (average 1 page loss per SOP)
  2. These are collections of various suggestions we’ve received over the past year from end-users.
  3. The resulting SOPs are much more visually appealing, especially on tablets.
  4. The resulting SOPs are much easier to navigate on tablets, which alot of users are implementing for their technicians.

 

Additional changes were made to some other SOP templates:

  1. HPRTSR: Updated the System Charging procedural section based on user feedback.
  2. HPR: Added a Cylinder Charging procedural section for those users that want that option.
  3. LEO: Traditional Permit LEO was simplified and now only has “Existing SOP,” “With Drain Valve,” and “Without Drain Valve” sections. The previous 4 possibilities was confusing to some and this one seems to be easier to understand.

Direct Replacement, Replacement in Kind and Management of Change

Of all the PSM/RMP requirements, the Management of Change element is the most consistently problematic. Most of the difficulty is in answering two questions:

  • The compliance question: Does the change you considering count as a “change” per the PSM/RMP rule.
  • The safety question: Does the change you are considering have the potential to affect the safety of the process?

Note, it is quite possible that you answer NO to the first question and YES to the second question.

 

The text of the Rule

1910.119(l)(1) – The employer shall establish and implement written procedures to manage changes (except for “replacements in kind”) to process chemicals, technology, equipment, and procedures; and, changes to facilities that affect a covered process.

From a compliance perspective, how broadly you interpret the “…changes to facilities that affect a covered process” portion dictates how many changes will be subject to this element.

Of course, there’s also a little window that allows you to avoid the MOC element if you classify the change as a “replacement in kind.” The rule provides a fairly useless definition of Replacement in Kind:

1910.119(b) …Replacement in kind means a replacement which satisfies the design specification.

The “replacement in kind” exception is routinely abused to avoid MOC. To understand this element better, let’s consider a few scenarios: Replacing a Valve, replacing a Motor, replacing an Ammonia Detector, and replacing a Condenser.

 

Example: Replacing a Valve

In this example, we’re replacing a valve with the same model, size, etc. Is this a change? Some people would call this a Replacement in Kind, but I would not. I would call this a Direct Replacement. It’s not kind of like the valve we’re replacing, it’s exactly like it. Such a change is outside the scope of the MOC element entirely.

What if we were replacing the valve with a different brand or model? Then we don’t know if it is a Replacement in Kind until we ask enough questions to assure ourselves that it satisfies the design specification. Some questions we might ask are:

  • Is it made of the same materials?
  • Does it have the same flow ratings / capacity?
  • Does it have the same mode of operation in manual and automatic?
  • Does it have the same Mechanical Integrity requirements?
  • Does it affect the PHA section that this equipment belongs to?

It’s quite possible that you answer enough questions to assure yourself that the replacement valve satisfies the design specification making it a Replacement in Kind. While this means it is outside of the MOC element for compliance purposes, we’d still recommend you document the rationale you used to determine that it meets these design specifications. You could even take this documentation one step further and declare that in the future all replacements of Brand A Model X valve with Brand B Model Y valve can be considered a Direct Replacement in this application.

 

 

Example: Replacing a Motor

A motor might be considered by some (incorrectly) to be outside of the MOC element because it doesn’t (usually) contain ammonia, but this is short-sighted. Remember, the MOC element is about Changes to…equipment…that affect a covered process. A motor for equipment that is part of your covered process would certainly fall within the scope of the element for consideration.

Ideally, we’re replacing the motor with the exact some one – a Direct Replacement that would place it outside the MOC element. But, if we are replacing it with another motor, we will be looking to prove that it satisfies the design specification so we can consider it a Replacement in Kind. Again, we need to ask questions:

  • Does it have the same electrical requirements (phase, voltage, etc.)
  • Does it have the same frame size?
  • Does it have the same RPM, duty rating, capacity, etc?
  • Does it affect the PHA section that this equipment belongs to?

Just like earlier in our valve example, it’s quite possible that you answer enough questions to assure yourself that the replacement motor satisfies the design specification making it a Replacement in Kind. While this means it is outside of the MOC element for compliance purposes, we’d still recommend you document the rationale you used to determine that it meets these design specifications. You could even take this documentation one step further and declare that in the future all replacements of Brand A Model X motor with Brand B Model Y motor can be considered a Direct Replacement in this application.

 

 

Example: Replacing an Ammonia Detector

Like earlier, with the motor example, a change to an ammonia detector might be considered by some (incorrectly) to be outside of the MOC element because it doesn’t (usually) contain ammonia, but this is short-sighted. Remember, the MOC element is about Changes to…equipment…that affect a covered process. You definitely consider these detectors as safeguards in your PHA, so we need to exercise some caution on this change.

If we’re replacing the detector with the exact same one, then it’s a Direct Replacement. If we’re replacing it with a different detector, we need to assure that it satisfies the design specification so we can consider it a Replacement in Kind. Again, we need to ask questions:

  • Does it have the same electrical requirements?
  • Does it have the same output signal / alarm outputs?
  • Does it have the same sensitivity?
  • Does it have the same Mechanical Integrity requirements? The same calibration equipment, schedule and calibration procedure?
  • Does it affect the PHA section that this equipment belongs to?

In my experience, unless you are dealing with a Direct Replacement, no detector meets the requirements for a Replacement in Kind because they almost all fail the last question on calibration equipment, schedule and procedure. That means such a change would require the implementation of a Management of Change procedure.

Here’s where we can get a little clever. The PSM/RMP rules require that we “establish and implement written procedures to manage changes” but they don’t require that we use the same procedure for every change! If we sit down and think through all we need to do to successfully change from Brand A Model X NH3 detector to Brand B Model Y NH3 detector, we could establish a standard procedure for doing so. That means that in a facility with, say, 45 detectors that you are changing over a period of time, you have a Single MOC (to establish the new procedure) and then simply implement the new NH3 Detector Change SOP 45 times as the changes occur.

 

 

Example: Replacing a Condenser

In this example we’re replacing a brand A evaporative condenser with 500 tons of capacity with a brand B evaporative condenser with 500 tons of capacity. Note: this would work the same with if you were replacing it with a different model of brand A as well. Also, if you were replacing a condenser with an exact duplicate, then theoretically you may be able to get by with a PSSR, but that assumes you don’t need any non-standard operating modes during the change-out.

First question: Is it a change to equipment which satisfies the design specification? Answer: Well, I don’t know because there is a lot that goes into that determination. But every part of a condenser changeout has the potential to affect the safety of your system. Questions you should ask include:

  • Does it have the same electrical requirements (phase, voltage, amp draw, etc.)
  • Is it have the same size and weight?
  • Is it made of the same materials?
  • Does it have the same flow ratings / capacity?
  • Does it have the same mode of operation in manual and automatic?
  • Does it have the same Mechanical Integrity requirements?
  • Does the P&ID need to be updated?
  • Does the SOP need to be updated?
  • Does it affect the PHA section that this equipment belongs to?
  • …and the list goes on.

While it is technically possible that you could ask these (and 100 other) questions concerning a condenser replacement in such detail that you ensure it satisfies the design specification, you are going to want to document all that work. I’ve personally never seen it happen unless it was the same make and model. In our opinion, the best way to document all that work is by following the Management of Change procedure.

 

Closing Thoughts

Management of Change is a difficult element. But by working this element, you can find and address hazards before they are introduced to your process. There’s very little that can be said about it better than this advice from the Petroleum NEP:

OSHA’s MOC requirement is prospective.

The standard requires that an MOC procedure be completed, regardless of whether any safety and health impacts will actually be realized by the change. The intent is, in part, to have the employer analyze any potential safety and health impacts of a change prior to its implementation. Even if the employer rightly concludes there would be no safety and health impacts related to a change, 1910.119(l)(1) still requires the employer to conduct the MOC procedure.

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