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A trap must pass the condensate the equipment makes, plus a margin for cold-start loads that can be several times the running rate. Manufacturers rate traps in lb/h at a given differential pressure, and capacity falls as differential drops — so size at the lowest expected differential, not the boiler pressure.
- Load 300 lb/h, safety factor 3×.
- Required = 300 × 3 = 900 lb/h at operating ΔP.
Reference tables
Typical safety factors
| Application | Factor |
|---|---|
| Steam main drip | 2× |
| Process / heat exchanger | 2–3× |
| Modulating / low ΔP | 3× |
A number the tables do not give: sizing on running load alone starves the trap at startup, when condensate can spike to 2–3× the running rate.
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FAQ
Why a safety factor?
Startup and modulating loads produce far more condensate than steady state; the factor keeps the trap from backing up and water-logging the equipment.
Which differential do I use?
The lowest expected inlet-minus-backpressure differential, because trap capacity drops as ΔP falls — sizing at high ΔP undersizes the trap.
Which trap type?
Float & thermostatic for heat exchangers, thermodynamic or inverted bucket for mains — match the type to the load pattern, then size the capacity.
Does back pressure matter?
Yes — a lifted or pressurized return raises back pressure, lowering ΔP and required-capacity headroom; include it in the differential.
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