Fugitive emissions are the leakage you don't see. Gas escaping past valve stems, gasket interfaces, and packing — small enough that nothing dramatic happens, large enough that across a plant it adds up to thousands of pounds per year. Regulators noticed. Now every spec sheet has an ISO 15848 line on it.

Here's what the standard actually requires, what the tightness classes mean, and how to spec without overpaying.

What ISO 15848 covers

ISO 15848 is split into two parts:

15848-1 is what you usually see on specs. The valve manufacturer takes a representative valve, instruments it, runs it through a defined number of mechanical and thermal cycles, and measures stem leakage. The result is a tightness class and an endurance class.

Tightness classes A, B, and C

Tightness is measured as helium leak rate per unit stem diameter, in millibar-liters per second per millimeter (mbar·L/s·mm). The standard defines three classes:

ClassMax leakage (helium)Use case
A (tightest)≤ 1×10⁻⁵ mbar·L/s·mmToxic, hazardous, regulated emissions service
B≤ 1×10⁻⁴ mbar·L/s·mmStandard hydrocarbon and chemical service
C≤ 1×10⁻² mbar·L/s·mmLess critical service — utility, water, non-VOC gases

For comparison, EPA Method 21 (the US-side equivalent test) uses ppm at the valve interface and is generally less strict than Class B. If your spec calls out "EPA fugitive emissions compliance," you're typically looking at something between Class B and Class C.

Endurance classes CO1, CO2, CO3

The other half of the qualification is how many cycles the valve can run while still meeting the tightness class. Three endurance classes:

A typical specification reads something like "ISO 15848-1, AH-CO2-SSA0-T(-29/200)". The pieces decode to:

What it actually takes to meet Class A

Class A on a control valve means most of the design effort goes into the stem packing system:

For ball valves, Class A typically requires double-stem-seal designs with a leak-detection chamber between them.

Common spec mistake Calling out Class A on a valve that doesn't need it. Class A packing systems run 15–30% more than standard fugitive packing, and the higher friction means larger actuators or more frequent recalibration. Spec Class A only where the service genuinely warrants it.

How to write the spec right

  1. Pick the right tightness class for the service. Toxic VOCs, HAPs, regulated hydrocarbons → Class A. General refinery and chemical → Class B. Utility services → Class C is fine.
  2. Pick the right endurance. ESD or control loops that cycle thousands of times per year → CO3. Block valves cycled monthly → CO1. Most general control duty → CO2.
  3. Specify the test temperature range. The valve's qualification only applies within the tested temperature window. Don't accept a -29/180°C qualification on a 230°C process.
  4. Require the type-test certificate. Not just a manufacturer claim of compliance — the actual ISO 15848-1 test report from an accredited lab.
  5. For Class A, require live-loading. If the spec says Class A and the supplier ships a single Belleville-stack design with a single packing follower, push back.

The bottom line

ISO 15848 isn't difficult, but it's where engineers either over-spec (and pay too much) or under-spec (and end up with measurable atmospheric leakage). Pick the class that matches the service, demand the actual test certificate, and pay attention to the temperature range it was qualified at.

If you've got a fugitive emissions spec to verify or you're not sure which class fits your service, send us the conditions. We'll review the qualification documentation against your operating window before you place the order.