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Stream List Assistant — Draft Preview

ProcessEngineer.io · First-pass stream lists from real P&IDs

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Step 1 — Pick a drawing

Three real P&IDs, drafted end to end

Tags, sources, destinations, line sizes, and pipe classes are pulled directly from the drawings. Operating data not on the page — temperature, pressure, mass flow, density — is filled with flagged assumptions, ready for the engineer to red-line.

Sheet · DD-10-01-FEED

Feed Preparation

Streams total
31
In preview
7
Extracted
2
Assumed
5

How to read the table

  • Extractedvalues were read directly from the P&ID — the drawing actually shows this number.
  • Assumedvalues were inferred from process context (service, line size, neighbouring streams). Never blank — always a flagged starting point.

Step 2 — Inspect the draft

Streams · DD-10-01-FEED

StreamFrom → ToServicePhaseLineClassTPMass flowDensitySource
N2-10-01-80Nitrogen Inlet Feed (battery limit) MX-10-03-80 tie-in (downstream HV-101)NitrogenVapor80P1A (process)25 °C20 bara28,000 kg/h12 kg/m³Extracted
H2-10-02-80Hydrogen Inlet Feed (battery limit) C-101 suctionHydrogenVapor80P1A (process)29 °C8 bara28,000 kg/h12 kg/m³Extracted
MX-10-03-80C-101 discharge C-102 suctionH2/N2 mixed gasVapor80P3H (H₂/N₂)40 °C30 bara9,600 kg/h12 kg/m³Assumed
MX-10-05-80C-102 discharge / E-102 C-103 suctionH2/N2 mixed gasVapor80P3H (H₂/N₂)45 °C60 bara9,600 kg/h12 kg/m³Assumed
MX-10-12-80HV-104 Bottom train tie-in (to MX-10-13-100 area)H2/N2 mixed gasVapor80P3H (H₂/N₂)40 °C100 bara9,600 kg/h12 kg/m³Assumed
MX-10-19-100C-107 discharge E-101 inletH2/N2 mixed gasVapor100P3H (H₂/N₂)95 °C200 bara12,000 kg/h12 kg/m³Assumed
CWS-10-21-25CWS header E-102 shell-side inletCooling water supplyLiquid25C2A (CW)25 °C4 bara22,500 kg/h995 kg/m³Assumed
Showing 7 of 7 preview rows from drawing DD-10-01-FEED (31 total in the full draft). Mass flow and density on assumed rows are inferred from service descriptions; engineer-confirm before issue.