Engineering Facilities interview prep.
Facilities engineers, project engineers, pipeline + station design leads, compressor + pump engineers, terminal + LNG facility engineers, integrity engineers on capital projects.
What interviewers look for
- Can the candidate design pipelines + stations per ASME B31 + API + PHMSA codes (192 / 193 / 195)?
- Do they have hydraulics + compression / pumping fluency - sizing, MAOP, NPSH, head + power calcs?
- Are they fluent in FEL / FEED / detailed-design stage-gate discipline + AFE cost + schedule control?
- Can they navigate HAZOP + LOPA + PSSR + safety-in-design + 1910.119 / RMP boundaries?
- Do they understand materials + corrosion + cathodic protection + integrity considerations from design forward?
- Are they grounded in commissioning + handover to ops + start-up safety?
- Long-game fit - project engineer / lead / senior / principal / engineering manager trajectory?
Behavioural questions to expect
Walk me through your background + engineering + project experience.
What it tests: Story arc - training, design + project experience, safety + regulatory exposure - so the interviewer can place you on the FEL/FEED/detail/construction spectrum.
Tell me about a design or capital project you've led or been part of.
What it tests: Engineering rigor - design discipline, cross-discipline coordination, project economics, safety integration.
Why midstream engineering vs upstream / downstream / chemicals?
What it tests: Authentic alignment - infrastructure permanence, design + integrity discipline, project execution rhythm.
Why this asset type - liquids pipeline / gas transmission / compressor + pump station / terminal / LNG?
What it tests: Specificity. Generic 'I like midstream' answers fail. Asset type + code regime differ materially.
Why this firm?
What it tests: Real homework - assets, capital programme, engineering model - not name-drop.
What's your read on our asset footprint + active capital programme?
What it tests: Industry literacy - asset mix, recent + planned projects, FERC + PHMSA posture.
Tell me what you understand about how we execute capital projects.
What it tests: Engineering-model fluency - self-perform vs EPC, FEL discipline, recent on-time / on-budget track record.
Walk me through a major design decision you've made on a pipeline, station, or facility.
What it tests: Design fluency - code interpretation, materials + sizing + safety trade-offs, decision authority.
Technical concepts to master
Pipeline + facility design
- Design basis + Class 1-4 (gas) / High-consequence routing
- Foundational design document - product, MAOP / MOP, design factor, location class, route, ambient + soil conditions.
- Wall thickness + materials selection (Barlow + API 5L)
- Wall thickness from Barlow formula given pressure, diameter, SMYS, design factor; materials chosen for service + cost.
- Compressor + pump station layout
- Station layout for gas (centrifugal / reciprocating compression + driver + cooling + scrubbing) or liquids (centrifugal / PD pumping + filter + meter).
- Cathodic protection + AC mitigation
- External corrosion control - impressed current + galvanic CP per NACE SP0169; AC mitigation where pipelines parallel HV powerlines.
Hydraulics + compression + pumping
- Steady-state hydraulics
- Pressure + flow + temperature profile along pipeline at design conditions - drives compressor + pump station spacing + sizing.
- Transient + surge analysis
- Dynamic pressure response to valve closure, pump trip, compressor trip - waterhammer + surge mitigation design.
- Compressor sizing - polytropic head + power
- Polytropic head from inlet / outlet pressure + temperature + gas properties; brake power = head x mass flow / efficiency.
- Pump sizing - TDH + NPSH
- Total Dynamic Head from suction / discharge / friction + static; NPSH available > NPSH required to avoid cavitation.
Project stage gates + AFE discipline
- FEL 1 (Appraise / Concept)
- Concept screen - business case, asset class, rough capacity, order-of-magnitude cost (-30 / +50%).
- FEL 2 (Select)
- Concept selection - preferred option, basis of design, preliminary layout, AACE Class 4 estimate.
- FEL 3 / FEED (Define)
- Front-end engineering design - detailed basis, P+IDs, equipment list, AACE Class 3 estimate (-10 / +25%).
- AFE (Authorisation for Expenditure)
- Capital project funding request - scope, cost, schedule, economics, risk - approved before construction sanction.
Safety-in-design + commissioning
- HAZOP (Hazard + Operability)
- Systematic guide-word review of design - node by node, parameter by parameter (more / less / no / reverse) - identifies hazards + operability concerns.
- LOPA (Layer of Protection Analysis)
- Semi-quantitative analysis - scenario frequency x consequence vs target risk; IPL credits reduce frequency.
- SIS + SIL (Safety Instrumented Systems / Safety Integrity Level)
- Safety Instrumented Systems with SIL 1-3 rating per IEC 61511 - PFD avg target by SIL level.
- PSSR (Pre-Startup Safety Review)
- Formal verification before hydrocarbon introduction - built per design, procedures in place, training complete, PHA actions resolved.
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
Related roles
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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