TEA Handbook

Concept

Engineering proxies & shorthands

mass-energyeconomic

Overview

An engineering proxy is a simplified stand-in — a typical value, a rule of thumb, a factored estimate, a generic scaling exponent — used in place of a rigorously derived figure when better data is unavailable or not worth the effort to obtain. Filling a model’s many unmeasured parameters with defensible proxies is the normal way an early-stage TEA gets built; the discipline is to use a class-appropriate proxy, state it as a modeling choice, and track the error it carries.

Body

What a proxy is. A proxy is a defensible placeholder for a quantity there is no first-principles data for. The corpus already runs on them: the six-tenths cost exponent ~0.6, the installation factor that turns purchased into installed cost, maintenance as a percentage of ISBL, a typical per-pass conversion, an equipment design margin of ~10–20%, a residence-time rule that fixes a vessel volume. Each replaces a calculation that would otherwise need data the estimate does not have.

Why proxies are legitimate here. The estimate’s accuracy class is wide (an order of ±30%, FEL-1/2 grade), so deriving every parameter rigorously buys precision the overall number cannot carry. A good proxy lands inside that band in minutes rather than weeks — which is exactly the deterministic, proxy-grade modeling the maturity anchor calibrates to.

The discipline that keeps a proxy honest. A proxy is not a guess. Using one well means:

Where they live. Proxies pervade both the physical and the cost sides: sizing scalars and exponents, installation and Lang factors, factored opex, typical conversions, efficiencies, and split fractions. They are the raw material of parameterizing a unit operation and of the capex build, and the decision to omit non-binding pressure and temperature is itself a proxy choice.

Limits & typical error

See also

Mini-example

Sizing the ammonia synthesis reactor with proxies instead of a kinetic model: take a typical per-pass conversion (~20%, the running-example value), a nominal catalyst residence time to fix the vessel volume, and a generic vessel cost exponent (~0.6 from sizing scalars). Three class-appropriate proxies, each stated as a modeling choice rather than a derived value, put the reactor’s size and cost in the right range in minutes — without a reaction-engineering study the estimate’s accuracy would not justify.

Separately, to show where a proxy bites: because per-pass conversion sets the recycle flow and therefore the loop equipment, the answer is sensitive to it — so the generic ~20% carries its whole error into the loop sizing, whereas the generic ~0.6 exponent on a non-dominant vessel passes only a small error through. The same quality of proxy matters very differently depending on what it feeds.

See also