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Ammonia inventory determination — maximum intended inventory, determined correctly

Your ammonia inventory determines whether you're subject to OSHA PSM (29 CFR 1910.119) and EPA RMP (40 CFR Part 68). We perform a complete maximum intended inventory determination — accounting for every component in your system at actual operating conditions.

Maximum Intended InventoryEPA 40 CFR Part 68OSHA 29 CFR 1910.11910,000 lb Threshold

The threshold question has a right answer. Most facilities don't have it.

If your ammonia refrigeration system holds 10,000 lb or more of ammonia refrigerant, you are subject to OSHA PSM and EPA RMP — two of the most demanding regulatory programs in industrial safety. If you're below the threshold, you're not.

That number — 10,000 lb — is determined by a maximum intended inventory determination: a component-level calculation that accounts for every vessel, heat exchanger, and piping segment in your system at actual operating conditions. Not nameplate data. Not estimates. Actual thermodynamic calculations at real operating pressure and temperature.

Most facilities have never had this calculation done properly. Nameplate charges and rough estimates frequently undercount by hundreds of pounds — putting facilities at risk of operating a covered process without required permits, programs, and protections in place.

If you're within 2,000 lb of the threshold

Inventory near the 10,000 lb mark is not static — it migrates seasonally as operating conditions change. A facility at 9,200 lb on paper may regularly exceed 10,000 lb during peak summer operations. We identify and quantify this risk.

Regulatory thresholds

OSHA PSM29 CFR 1910.119
10,000 lb ammonia
EPA RMP40 CFR Part 68
10,000 lb ammonia
MII DeterminationComponent-level calc
Actual conditions

OSHA penalty exposure

Operating a covered process without a required PSM program exposes your facility to willful violations at $15,625 per day per violation. EPA RMP penalties run up to $70,117 per day.

Why most inventory numbers are wrong

Nameplate charges

Equipment nameplates list design charge, not actual operating charge. They ignore operating conditions and piping.

Estimating by system size

Rules of thumb like "2 lb per ton of refrigeration" can be off by hundreds of pounds for real systems.

Ignoring piping

In large systems, liquid and suction piping can hold 500–1,500 lb of ammonia that never appears in vessel-only calculations.

Wrong operating conditions

A calculation performed in spring underestimates summer inventory, when condensing pressure is high and the HP receiver is fuller.

A proper maximum intended inventory determination addresses all of these. It accounts for vessel geometry, operating pressure, saturation temperature, liquid density, vapor density, and piping volume — at actual conditions, not design conditions.

Everything needed for OSHA and EPA submissions

Component-level charge calculation for all vessels (HP receiver, LP receiver, intercoolers, surge drums, oil pots)
Evaporator charge accounting using coil volume and liquid fill fraction
Condenser charge including flood-back scenarios
All interconnecting piping — liquid lines, suction lines, discharge lines, hot gas lines
Corrected calculations for operating temperature and pressure conditions
Summary table with total system charge and regulatory threshold comparison
Formal report suitable for OSHA and EPA regulatory submissions
Recommendations for threshold management if approaching 10,000 lb
Note: Most facilities have never had a proper maximum intended inventory determination. Nameplate charges, general estimates, and simplified calculations frequently undercount by hundreds of pounds.

Download the example inventory determination spreadsheet

See exactly how a proper ammonia inventory determination works. This spreadsheet walks through a complete component-level calculation for a real cold storage system — vessels, heat exchangers, and piping — showing exactly how maximum intended inventory is determined.

NH3Edge_Ammonia_Inventory_Example.xlsx

MII determination · Vessels, HX & piping · Example cold storage facility

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Maximum intended inventory (MII)

EPA 40 CFR Part 68 requires covered facilities to report their maximum intended inventory — the largest quantity of a regulated substance you intend to have on-site at any one time. For ammonia refrigeration systems, this is not the same as your average operating inventory.

Maximum intended inventory must account for peak operating conditions — typically summer peak load at maximum condensing pressure — and any additional charge that could be added to the system for seasonal adjustments or makeup.

This number feeds directly into your worst-case and alternative release scenario calculations in your RMP submittal. Understating it reduces your apparent consequence distance — which can create compliance exposure if LEPC or EPA reviewers challenge your assumptions.

MII vs. operating inventory

01

Operating inventory

Actual charge at measured conditions

02

Maximum intended inventory

Largest quantity intended to be on-site

03

Worst-case scenario quantity

Used in RMP offsite consequence analysis

Our inventory determination reports include both your current operating inventory and a documented maximum intended inventory suitable for use in your RMP submittal.

Ready to know your actual inventory?

We'll review your system, perform a complete maximum intended inventory determination, and deliver a formal report ready for OSHA and EPA submissions.