Oil & GasShell & Tube Heat Exchangers in Oil & Gas: Sour Service, Fouling and Fast Turnarounds
How NACE MR0175 material selection and API 660 design decide whether an exchanger survives sour hydrocarbon service for two years or twenty.
Read MoreRashid Al Mansoori
Lead Process Engineer · 8 min read

An EPC heat exchanger scope runs through five phases that look sequential on a project schedule but are, in practice, tightly coupled — a late change in one phase can ripple into every phase downstream of it. Understanding where that coupling is tightest is what separates a project that holds its schedule from one that doesn’t.
Fabrication shop capacity is rarely the binding constraint on an EPC exchanger schedule — long-lead material, particularly exotic alloy plate and tube for duplex or titanium services, is. Procurement needs to start the moment thermal and mechanical design fix material grade and thickness, which means any late-stage process data change that alters material selection has a schedule cost far larger than its engineering cost alone.
“On an EPC exchanger schedule, the mill order date matters more than the fabrication start date.”
Thermal design in HTRI fixes geometry — tube count, length, pitch, baffle spacing — that mechanical design in PV Elite then has to accept as a constraint while solving for pressure-retaining thickness and nozzle reinforcement. A clean handoff between the two disciplines, with no unresolved geometry assumptions, is what keeps mechanical design from discovering a conflict late enough to force a re-run of the thermal model.
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