CSB Investigation — Toxic Release — Ammonia Refrigeration
Cuisine Solutions Ammonia Release
Cuisine Solutions, Inc.
📍 Sterling, VA (Loudon County)
Incident Date: July 31, 2024  |  CSB Report Released: September 25, 2025
0
Fatalities
40
Injuries
Anhydrous
Ammonia (NH₃)
Chemical / Hazard
6
CSB Recommendations
📋 Incident Summary

On July 31, 2024, a hazardous ammonia release at the Cuisine Solutions food processing facility in Sterling, Virginia sent 40 people to hospitals — four were admitted, including one to the intensive care unit. The facility employed approximately 350 workers and operated large-scale ammonia refrigeration systems approximately 30 miles from Washington, D.C. The release occurred when an ammonia refrigeration system pressure relief device (PRD) discharged — but instead of releasing vapor only, it released liquid ammonia in a two-phase flow, creating a dense, ground-level ammonia cloud far larger and more hazardous than a vapor-only discharge.

The Emergency Action Plan (EAP) at Cuisine Solutions did not distinguish between indoor and outdoor ammonia releases — two scenarios requiring different responses. No ammonia-specific alarm existed to tell workers what to do. Workers evacuated through areas with elevated ammonia concentrations because the EAP lacked wind direction guidance, alternate routes, and shelter-in-place criteria. The confusion during the response converted a containable process safety event into a mass casualty incident.

The CSB's final report (released September 25, 2025) found that the pressure relief system for the horizontal surge drum was not designed to prevent liquid/two-phase discharge — a gap in both facility design and industry standards. Six recommendations were issued covering relief system redesign, emergency planning, and process data collection.

🔎 Key Findings
Finding 1
Two-Phase PRD Discharge
The ammonia refrigeration surge drum's pressure relief device discharged liquid ammonia (two-phase flow) rather than vapor only. This created a dense, ground-level ammonia cloud covering a much larger area than a vapor discharge would have.
Finding 2
Surge Drum Geometry Created High-Liquid Risk
The horizontal surge drum, containing saturated liquid ammonia with minimal vapor space, had a high liquid level/boiling overpressure scenario that led to liquid carrying over into the relief discharge — a scenario not adequately addressed in the relief system design.
Finding 3
EAP Did Not Distinguish Indoor vs. Outdoor Releases
The Emergency Action Plan did not address indoor and outdoor ammonia releases separately. These are fundamentally different emergencies: indoor releases may require shelter-in-place while outdoor releases require upwind evacuation.
Finding 4
No Ammonia-Specific Alarm
No alarm specific to ammonia releases existed. Workers heard a generic alarm signal and were uncertain whether to evacuate or shelter-in-place — and some exited through paths with elevated ammonia concentrations.
Finding 5
No Process Data Historian
No electronic data historian recorded refrigeration system parameters. The CSB could not fully reconstruct the event sequence, and the facility had no early warning data for operators during the incident.
Finding 6
Industry Standard Gap
ANSI/IIAR 2 — the primary ammonia refrigeration equipment standard — contained no specific guidance on preventing liquid/two-phase PRD discharges or assessing whether PRD discharge locations were safe.
🔍 Root Causes
1
Liquid/Two-Phase PRD Discharge
The ammonia relief system was not designed to prevent liquid carry-over during a high liquid level or boiling overpressure event on the horizontal surge drum. The design did not account for this scenario.
2
Inadequate Emergency Action Plan
The EAP was insufficient for ammonia-specific releases — it lacked indoor/outdoor distinctions, wind direction guidance, shelter-in-place criteria, and ammonia-specific alarm procedures.
3
No Chemical-Specific Alarm
Without an ammonia-specific alarm, workers had no way to understand the nature of the emergency or what protective action was appropriate when the event occurred.
4
No Process Data Logging
The absence of a process data historian meant there was no continuous monitoring of refrigeration system parameters, no early warning capability, and no post-incident data for investigation.
☑ CSB Recommendations
→ Cuisine Solutions Inc.
Identify liquid or two-phase PRD discharge scenarios, especially for horizontal surge drums. Implement engineering controls to reduce the likelihood of high liquid level/overpressure. Conduct a third-party audit of all ammonia pressure relief systems.
→ Cuisine Solutions Inc.
Implement an electronic process data historian for the ammonia refrigeration system, enabling continuous monitoring, early warning capability, and post-incident reconstruction.
→ Cuisine Solutions Inc.
Update the Emergency Action Plan to address indoor and outdoor releases separately, specify evacuation routes with alternate paths, provide windsock-based wind direction guidance, define shelter-in-place criteria, and require annual ammonia-specific drills for all personnel.
→ Cuisine Solutions Inc.
Add ammonia-specific alarm(s) with documented responses in the EAP, including distinct signals for shelter-in-place and evacuation scenarios.
→ International Institute of Ammonia Refrigeration (IIAR)
Update ANSI/IIAR 2 to include guidance on preventing liquid/two-phase PRD discharges for horizontal surge vessels and other at-risk configurations, including mitigative safeguards.
→ International Institute of Ammonia Refrigeration (IIAR)
Update ANSI/IIAR 2 to require dispersion analysis to verify that PRD discharge locations are safe for nearby personnel.
💡 Lessons Learned
⚠ Pressure relief devices can discharge liquid, not just vapor — especially from horizontal vessels with high liquid levels or saturated liquids. The hazard zone for liquid discharge is dramatically larger.
⚠ An Emergency Action Plan that does not specifically address your hazardous chemicals is not a PSM-compliant EAP. Generic fire evacuation plans do not address ammonia, HF, chlorine, or other toxic release scenarios.
⚠ Workers need to know what to do from the alarm signal alone. If the alarm doesn't tell them what kind of emergency it is and what protective action to take, the EAP has failed before anyone moves.
⚠ Process data historians are not optional for complex process systems. Without continuous data logging, you cannot detect developing problems early, and you cannot investigate incidents after the fact.
⚠ Shelter-in-place and evacuation are not interchangeable. Depending on the release type and location, evacuating can route workers directly into a chemical plume. Your EAP must specify which response applies to which scenario.
PSM Elements: PSI · MI · EAP · SOP · PHA
🔨 Safety Meeting Toolbox Talk
Topic: Ammonia Refrigeration Safety & Emergency Response
💬Does our Emergency Action Plan distinguish between indoor and outdoor ammonia releases? Do you know which response applies to each scenario?
💬Where are the windsocks at this facility, and do you know how to use them to identify which evacuation route keeps you upwind of a release?
💬What alarm sounds for an ammonia release at this facility — and what does that specific alarm tell you to do?
💬Have you reviewed the pressure relief discharge points for our ammonia system? Do any of them discharge over occupied areas or have potential for liquid carry-over?
💬What are the IDLH, TLV-TWA, and TLV-STEL for ammonia? What concentration would you begin to smell it versus the concentration that becomes dangerous?
💬When did we last conduct an ammonia-specific emergency drill — one that tested the actual alarm, evacuation routes, shelter-in-place decision, and muster point headcount?
✎ Team Action Items
✓Locate and review your facility's ammonia-specific Emergency Action Plan — confirm it has distinct procedures for indoor vs. outdoor releases
✓Identify your ammonia relief device discharge points and determine whether they could discharge over occupied areas
✓Verify that your personal ammonia detection equipment is functional and calibrated, and confirm alarm setpoints
✓Walk the evacuation routes from your work area and identify the alternate routes in case the primary path is upwind of a release
🔗 PSM Failures Behind This Incident

This incident traced to breakdowns across 5 PSM elements (PSI · MI · EAP · SOP · PHA). Each represents a documented gap that process safety documentation and consulting can close before a similar event occurs at your facility.

Process Safety Information (PSI)
Accurate, complete Process Safety Information is the foundation every other PSM element depends on. When PSI is missing or wrong — chemistry data, equipment specs, P&IDs — the entire hazard analysis is built on a flawed base.
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Mechanical Integrity (MI)
Equipment must be designed, inspected, and maintained to operate safely in its intended service. Mechanical integrity failures — degraded equipment, missed inspections, deferred repairs — contributed to loss of containment here.
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Emergency Planning & Response
When process safety barriers fail, emergency response capability determines whether the outcome is controlled or catastrophic. Gaps in emergency preparedness amplified the consequences here.
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Operating Procedures (SOPs)
Operators cannot reliably hold safe operating limits without clear, current, enforced procedures. Deviation from acceptable operating conditions — a root cause here — is a direct consequence of SOP failure.
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Process Hazard Analysis (PHA)
A structured PHA or HAZOP study exists to identify exactly these scenarios before they occur. When PHA is absent, superficial, or overdue for revalidation, hazards operate unseen until they kill someone.
Supporting documents in our library →
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