Guide · Layer 2
Written for: seed / Series A scientist-founder
Don’t stop to perfect each box as you go. It’s usually faster to charge through end to end first — get a rough version of every unit connected and producing a number — then come back here to clean up, before the model gets too tangled to fix.
Closing the balance is that clean-up pass — it’s where the model’s mistakes tend to surface.
Make the streams reconcile — mass in = mass out — around each box and around the whole plant:
Put your attention on the biggest streams — an error in a major feed moves equipment size and consumption both; a trace stream rarely changes the answer. When the algebra tangles, find a tie component — a species that rides straight through untouched backs out an unknown flow in one division. And lay the balance out inside each box (input → mechanism → output), not as one wide stream table; if you keep a stream table, make it display-only — every number calculated elsewhere and referenced in.
The step up replaces proxies with real phase equilibria, kinetic reactor models that predict conversion instead of assuming it, and formal pinch analysis for heat integration — usually inside the same process simulator Layer 1 flagged for solving loops. It’s worth doing when a P/T-sensitive equilibrium won’t yield to a proxy, when conversion is the thing you’re trying to predict, or when detailed design or a counterparty’s diligence demands it.
Once the flows and duties are fixed, the next layer puts dollars on them: Layer 3 — Economic Layer, where each duty becomes an equipment cost and each consumption figure becomes a cost per tonne.