Engineering Facilities
Engineering Facilities interview prep.
The library content Coach uses to tailor reports for this role. Generated reports personalise this against the candidate's CV + the firm's context.
Behavioural questions to expect
- Walk me through your background + engineering + project experience.
- Tell me about a design or capital project you've led or been part of.
- Why midstream engineering vs upstream / downstream / chemicals?
- Why this asset type - liquids pipeline / gas transmission / compressor + pump station / terminal / LNG?
- Why the firm?
- What's your read on our asset footprint + active capital programme?
- Tell me what you understand about how we execute capital projects.
- Walk me through a major design decision you've made on a pipeline, station, or facility.
Technical concepts to master
Pipeline + facility design
Design basis + Class 1-4 (gas) / High-consequence routing · Wall thickness + materials selection (Barlow + API 5L) · Compressor + pump station layout · Cathodic protection + AC mitigation · Coating systems
Hydraulics + compression + pumping
Steady-state hydraulics · Transient + surge analysis · Compressor sizing - polytropic head + power · Pump sizing - TDH + NPSH · Pigging + facility design for pigs
Project stage gates + AFE discipline
FEL 1 (Appraise / Concept) · FEL 2 (Select) · FEL 3 / FEED (Define) · AFE (Authorisation for Expenditure) · Detail design + construction
Safety-in-design + commissioning
HAZOP (Hazard + Operability) · LOPA (Layer of Protection Analysis) · SIS + SIL (Safety Instrumented Systems / Safety Integrity Level) · PSSR (Pre-Startup Safety Review) · MOC (Management of Change)
Practical drills
- You're sizing a 50-mile natural gas transmission line, 24 inch nominal, MAOP 1440 psig, Class 2 location, API 5L X65. Walk through wall thickness selection, hydraulic profile considerations, and one or two key trade-offs.
- You're leading a HAZOP for a new compressor station - one node is the discharge of a centrifugal compressor. Walk through how you'd identify hazards + apply LOPA for one high-consequence scenario.
- You're 70% through FEED on a new LNG truck loading facility. Operations team requests adding a third loading bay (originally two-bay design). Walk through your decision.
Smart-question anchors
- Asset footprint + active capital programme - announced projects, FERC certificates
- Engineering execution model - in-house vs EPC, FEL discipline maturity
- Recent project track record - on-time / on-budget, lessons-learned commentary
- Design + integrity choices - coatings, CP, AC mitigation, high-strength steel use
- Regulatory engagement - PHMSA design, FERC, state PUC, environmental permitting
Sourced from
PHMSA 49 CFR Parts 192 / 193 / 195 · ASME B31.4 + B31.8 pipeline design codes + B31G integrity · API standards - 2510, 650, 620, RP 1102, RP 1117, 5L · NFPA 59A LNG standard + NACE SP0169 / SP0286 cathodic protection · AACE International cost estimate classification + stage-gate practice + CCPS safety-in-design
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