TEA Handbook

Concept

Sizing scalars (by equipment class)

economic

Overview

Sizing scalars are the small reference set that pairs each class of process equipment with the two things needed to scale its cost: the size measure that governs the item’s cost, and the cost-scaling exponent for the six-tenths rule. They’re the lookup table the scaling rule reads from — so a whole plant’s equipment can be costed from a handful of classes, not item by item.

Body

What a scalar records. For each equipment class:

The six-tenths rule supplies the form; the scalar supplies the n and the S.

Keep the classes few — ~5–6. Group equipment into a handful of classes (e.g. compressors, heat exchangers, pumps, pressure vessels / columns, reactors, and a catch-all). Each carries one representative exponent and size measure. Resolving more is false precision: because cost is only mildly sensitive to the exponent (see Limits), splitting sub-types buys accuracy the rest of the estimate can’t match.

Representative exponents. Class values cluster around the ~0.6 aggregate but spread across roughly 0.4–0.9 — compressors and many vessels toward the high end, pumps and small items toward the low. They come from cost-engineering references (Turton, Towler/Sinnott) and are stable across time and place; the generic 0.6 is the fallback for a class with no better figure. The exponent is the transferable half of a costing anchor — far more portable across years and locations than the reference cost it multiplies.

How it’s used. A sized item’s class fixes both which S to scale on and which n to use; the six-tenths rule returns the scaled cost, which aggregates into capex. A size beyond the class’s largest standard unit moves into numbering up / down.

Limits & typical error

Mini-example

Costing the ammonia synthesis loop draws on two class scalars at once. The syngas compressor sits in the centrifugal-compressor class — measure power, n ≈ 0.62 — so its $2.0M / 5 MW reference scales to ~$2.7M at 8 MW (the six-tenths worked case). The ammonia reactor sits in the pressure-vessel / reactor class — measure volume, n ≈ 0.6 — scaling on the vessel volume sizing set from the ~20% per-pass residence time. Two items, two class scalars, each picking the measure and exponent its class is defined on.

Edge case: the same reactor scalar applied across a switch from carbon steel to a high-alloy vessel would fold a metallurgy cost step into what looks like a volume effect — the exponent describes scaling within one material family, not a jump between families.

See also