Field Development Planning - Concept Selection, FDP Structure, Pre-FEED to FEED, and Well Program Optimization
A Field Development Plan (FDP) is the master engineering and commercial document that defines how a discovered hydrocarbon accumulation will be developed, produced, and ultimately abandoned. It integrates every technical discipline subsurface, drilling, facilities, pipelines, export, and decommissioning - into a single coherent program whose execution will determine whether the field delivers its economic potential or falls short through poor concept selection, inadequate well count, undersized processing capacity, or suboptimal production sequencing. The FDP is not a static document written once and filed away: it is a living engineering baseline that is updated every 2-3 years as production data refines the reservoir model, as technology evolves, and as commodity price changes alter the economic boundary conditions that define which development options are viable. A company that treats its FDP as a regulatory submission document rather than an operational management tool will consistently underperform against the reservoir's potential, because every major investment decision - whether to drill an infill well, install compression, or extend field life with enhanced recovery - should be evaluated against the FDP baseline and updated within its framework. This guide covers the complete FDP development process from concept screening through pre-FEED to FEED to Final Investment Decision, with the quantitative tools that drive concept selection at each stage.
1. FDP Development Phases - From Discovery to FID
1.1 The Phase Gate Process
The FDP is developed through a structured phase gate process that progressively reduces technical uncertainty and increases engineering definition before each major capital commitment. Each gate is a formal decision point where the project team presents its work to senior management, who decide whether to proceed to the next phase, recycle back for additional work, or kill the project:
| Phase | Engineering Activity | Cost Estimate Accuracy | Typical Duration | Decision Gate |
|---|---|---|---|---|
| Appraisal / Concept Screening | Geological and reservoir characterization, identification of 3-5 concept alternatives, order-of-magnitude cost estimates, high-level NPV screening of each alternative | ±50% (Class 5) | 6-18 months | Gate 1: Select 2-3 concepts for pre-FEED. Kill clearly uneconomic options. Commit pre-FEED budget. |
| Pre-FEED (Preliminary Front End Engineering Design) | Concept definition for 2-3 alternatives, preliminary process design, well count and schedule, environmental impact assessment, detailed cost estimate, project risk register | ±30% (Class 4) | 6-12 months | Gate 2: Select preferred concept (Concept Select). Commit FEED budget (typically 3-5% of total project cost). |
| FEED (Front End Engineering Design) | Detailed engineering of preferred concept: P&IDs, equipment sizing, well design, procurement strategy, HAZOP, SIL assessment, detailed schedule. Basis for EPC contractor tenders. | ±15% (Class 3) | 12-24 months | Gate 3: Final Investment Decision (FID). Commit full development Capex. Award EPC contracts. |
| Execution (EPC + Drilling) | Construction, hook-up, commissioning of facilities. Drilling and completion of development wells. First oil/gas production. | ±5-10% (actual vs budget) | 2-5 years | Milestone: First oil. Benchmark against FDP production forecast. |
1.2 FDP Document Structure
A complete FDP for regulatory submission and internal approval typically contains the following sections, each of which represents a specific technical discipline's contribution to the integrated development plan:
Standard FDP document structure (DECC/NSTA format for UK North Sea):
Section 1: Executive Summary
Field name, location, operator, license number. Key economics: NPV, IRR, breakeven price, plateau rate, first oil date. Government take. Summary of concept selected and basis for selection.
Section 2: Reservoir Description and Resource Assessment
Geological model, fluid properties, pressure-volume-temperature (PVT) data. Volumetric estimates (STOIIP, GIIP). Recovery factor justification. Reserves classification per SPE-PRMS. Uncertainty range (P10/P50/P90 estimates).
Section 3: Development Concept
Description of selected development concept. Comparison against alternatives evaluated and reasons for selection. Production philosophy (natural flow, artificial lift, EOR). Processing concept overview.
Section 4: Well Program
Number, type, and location of development wells. Well design basis. Drilling and completion schedule. Hydraulic fracturing program (if applicable). Artificial lift design. Production surveillance philosophy.
Section 5: Production Forecast
Oil/gas/water production profiles by year for the P10/P50/P90 cases. Basis for decline curve parameters. Recovery factor sensitivity analysis.
Section 6: Facilities Description
Topsides processing design (separator train, gas treatment, water handling). Export system (pipeline, FPSO, truck loading). Utilities. Control and safety systems.
Section 7: Project Schedule
Gantt chart from FID to first oil and plateau. Critical path identification. Key milestones and deliverables. Long-lead item procurement schedule.
Section 8: Cost Estimate
Capex by work breakdown structure (WBS). Opex by category (fixed/variable). Abandonment cost estimate. Basis of estimate and contingency allocation.
Section 9: Economic Analysis
Full cycle cash flow model. NPV/IRR/breakeven at base case and sensitivity cases. Risk-weighted EMV. Government take calculation.
Section 10: HSE and Environmental Impact Assessment
HAZOP/HAZID summary. Emergency response philosophy. Environmental impact assessment. Decommissioning plan outline.
Section 11: Uncertainty and Risk Register
Technical, commercial, and execution risks. Mitigation actions. Contingency plans for key risk scenarios.
2. Concept Selection - The Most Important FDP Decision
2.1 Concept Alternatives and Selection Criteria
The development concept defines the physical infrastructure that will be built to produce the field - the type of production facility, the export route, the well architecture, and the artificial lift philosophy. Concept selection is the highest-value decision in the entire FDP process because it locks in cost and production performance for the 20-30 year life of the field. A suboptimal concept selection cannot be fully corrected by operational excellence during production:
Concept screening matrix - offshore gas-condensate field (450 MMstb condensate, 2.8 Tcf gas):
Concept A: Standalone FPSO with gas export pipeline
Capex: $3,850M
Plateau production: 85,000 bbl/day condensate, 750 MMscf/day gas
First production: 5.5 years from FID
NPV at 12%, $68/bbl, $4/Mscf: $1,250M
Breakeven oil price: $38/STB
Key risk: Gas monetization requires committed pipeline capacity (10-15 year offtake contracts needed)
Concept B: Tie-back to existing host platform (30 km):
Capex: $1,850M (no standalone processing needed)
Plateau production: 65,000 bbl/day condensate, 480 MMscf/day gas (limited by host capacity)
First production: 3.5 years from FID (faster - no new facility construction)
NPV at 12%, $68/bbl, $4/Mscf: $920M
Breakeven oil price: $28/STB
Key risk: Host platform availability and remaining life (12 years) limits field production life and recovery
Concept C: Phased development - early tie-back then standalone FPSO:
Phase 1 Capex: $1,850M (tie-back as Concept B)
Phase 2 Capex: $2,200M (standalone FPSO, 8 years into production)
Plateau production: 85,000 bbl/day ultimately (same as Concept A after Phase 2)
First production: 3.5 years (as Concept B)
NPV at 12%, $68/bbl, $4/Mscf: $1,480M
Breakeven oil price: $31/STB
Key risk: Phase 2 decision is optional - creates valuable deferral option if oil prices fall
Concept selection scoring matrix (weighted criteria):
Criterion - Weight - Concept A - Concept B - Concept C
NPV (30%) - A:5, B:3, C:5
Breakeven robustness (25%) - A:3, B:5, C:4
Schedule to first oil (20%) - A:2, B:5, C:5
Capital efficiency (15%) - A:3, B:5, C:4
Flexibility/optionality (10%) - A:2, B:2, C:5
Weighted scores:
Concept A: 5x0.30 + 3x0.25 + 2x0.20 + 3x0.15 + 2x0.10 = 1.50+0.75+0.40+0.45+0.20 = 3.30
Concept B: 3x0.30 + 5x0.25 + 5x0.20 + 5x0.15 + 2x0.10 = 0.90+1.25+1.00+0.75+0.20 = 4.10
Concept C: 5x0.30 + 4x0.25 + 5x0.20 + 4x0.15 + 5x0.10 = 1.50+1.00+1.00+0.60+0.50 = 4.60
Concept C scores highest: highest NPV combined with faster first oil and maximum flexibility through the Phase 2 deferral option.
The $230M higher NPV of Concept C vs Concept B is driven by two factors: the higher ultimate plateau rate (85,000 vs 65,000 bbl/day after Phase 2) and the acceleration benefit of earlier first production vs Concept A (2-year earlier start worth ~$180M NPV at this production scale).
3. Well Program Design - Optimizing the Drilling Schedule
3.1 Well Count Optimization
The number of development wells required is determined by the production plateau target, the individual well deliverability (PI x drawdown), and the reservoir areal extent that must be drained to achieve the target recovery factor. More wells than necessary wastes capital; fewer wells than necessary leaves production rate below the plateau target and may result in pressure depletion in some areas before drainage in others:
Well count calculation - reservoir engineering basis:
Plateau rate requirement: 85,000 STB/day condensate (Concept C)
Individual well deliverability estimate:
Reservoir permeability k = 85 md, net pay h = 38 ft
Productivity Index (Darcy flow, no skin): PI = kh / (141.2 x Bo x mu_o x (ln(re/rw) - 0.75 + S))
Where: Bo = 1.38 RB/STB, mu_o = 0.42 cp, re = drainage radius = 2,640 ft (320-acre spacing), rw = 0.354 ft, S = skin = +5 (estimated for initial wells)
ln(re/rw) = ln(2640/0.354) = ln(7,458) = 8.917
PI = (85 x 38) / (141.2 x 1.38 x 0.42 x (8.917 - 0.75 + 5))
= 3,230 / (141.2 x 1.38 x 0.42 x 13.167)
= 3,230 / (141.2 x 0.5796 x 13.167)
= 3,230 / 1,077.9 = 2.996 ≈ 3.0 STB/day/psi PI per well
Expected drawdown at plateau:
Reservoir pressure Pr = 4,850 psi
Minimum Pwf (above bubble point 3,200 psi): Pwf_min = 3,300 psi
Maximum drawdown = 4,850 - 3,300 = 1,550 psi
Maximum individual well rate = PI x drawdown = 3.0 x 1,550 = 4,650 STB/day per well
Number of wells required for plateau:
N_wells = Plateau_rate / q_per_well = 85,000 / 4,650 = 18.3 → 19 production wells
Add water injection wells (1 injector per 2 producers for peripheral injection pattern): 10 injection wells
Total development wells: 29 wells (19 producers + 10 injectors)
Well count sensitivity to permeability uncertainty:
At k = 55 md (P10 case): PI = 1.94 → q_per_well = 3,007 STB/day → N_wells = 28 producers
At k = 125 md (P90 case): PI = 4.42 → q_per_well = 6,851 STB/day → N_wells = 13 producers
The P10 case requires 28 producers vs 13 in the P90 case - a 115% variation in well count driven entirely by permeability uncertainty. This range must be reflected in the Capex uncertainty range (±40-50% for well program cost alone) and justifies early pilot wells to constrain permeability before committing to the full 29-well program.
3.2 Well Scheduling - Optimizing First Oil Date and Production Ramp-Up
Drilling schedule optimization - rig count vs time-to-plateau trade-off:
Single rig scenario:
Wells per year (1 rig): 6 wells/year (60 days per well average including mobilization)
Time to drill all 19 producers: 19/6 = 3.17 years
Facilities ready: Year 3.5 from FID (Concept C tie-back phase)
First oil: Year 3.5 (6 wells drilled = 27,900 STB/day ramp-up production)
Plateau achieved: Year 6.7 (all 19 producers drilled)
Two rig scenario:
Wells per year (2 rigs): 12 wells/year
Time to drill all 19 producers: 19/12 = 1.58 years
First oil: Year 3.5 (same - limited by facility readiness, not drilling)
Plateau achieved: Year 4.5 (all producers drilled before full facility completion)
Value of plateau acceleration (2 rigs vs 1 rig):
Plateau rate: 85,000 STB/day
Ramp-up period savings: 2.2 years earlier plateau x average 40,000 STB/day incremental during ramp-up
Incremental production accelerated: 40,000 x 365 x 2.2 = 32.12 MMstb
NPV of acceleration: 32.12 MMstb x $32.50/STB net x PV_factor_avg
PV_factor at Year 5 avg: 1/(1.12)^5 = 0.567
NPV_acceleration = 32.12 x $32.50 x 0.567 = $592M x 0.567 = $591M... let me recalculate
More carefully: Net revenue = $32.50/STB
32,120,000 STB x $32.50 = $1,043,900,000 undiscounted
Discounted at 12% with 5-year average timing: $1,043.9M x 0.567 = $591.9M acceleration value
Second rig cost premium: ~$45M/year x 2.2 years = $99M additional drilling cost
NPV of second rig = $591.9M - $99M = $492.9M positive NPV from second rig investment
Conclusion: The second rig generates $492.9M NPV from production acceleration at a cost of $99M. ROI = 5:1. The second rig is the highest-return investment in the entire development program.
4. Production Forecast - Integrating Reservoir Simulation with FDP Economics
4.1 Production Profile Construction
FDP production profile construction methodology:
Phase 1: Facility-limited ramp-up (Years 1-3)
Production limited by number of wells drilled and facility capacity ramp-up
Year 1: 6 wells x 4,650 STB/day = 27,900 STB/day
Year 2: 12 wells x 4,200 STB/day (slight decline from early wells) = 50,400 STB/day
Year 3: 19 wells x 4,000 STB/day = 76,000 STB/day (approaching plateau)
Phase 2: Plateau production (Years 4-8)
Production maintained at plateau by:
- Natural pressure support from aquifer and/or gas cap expansion
- Water injection maintaining reservoir pressure
- New wells replacing natural decline in existing producers
Plateau rate: 85,000 STB/day (limited by facility capacity)
Phase 3: Decline (Years 9-25)
After plateau: Natural production decline as reservoir pressure depletes
Apply field decline rate: 12% per year (from reservoir simulation P50 case)
Year 9: 85,000 x (1-0.12) = 74,800 STB/day
Year 10: 74,800 x 0.88 = 65,824 STB/day
Year 15: 85,000 x (0.88)^7 = 85,000 x 0.409 = 34,765 STB/day
Year 20: 85,000 x (0.88)^12 = 85,000 x 0.222 = 18,870 STB/day
Year 25: 85,000 x (0.88)^17 = 85,000 x 0.120 = 10,200 STB/day → approaching abandonment rate
Cumulative production (total field life):
Ramp-up (3 years): approximately 55 MMstb
Plateau (5 years): 85,000 x 365 x 5 = 155.1 MMstb
Decline (17 years): approximately 200 MMstb (declining from 74,800 to 10,200 STB/day)
Total field EUR: approximately 410 MMstb condensate
Recovery factor: 410/450 STOIIP = 91.1% - very high, justified by strong aquifer support and good vertical sweep
P10/P50/P90 production profile range:
P90 (optimistic): 450 MMstb EUR, plateau rate 95,000 STB/day
P50 (base case): 410 MMstb EUR, plateau rate 85,000 STB/day
P10 (pessimistic): 310 MMstb EUR, plateau rate 65,000 STB/day (aquifer weaker than expected)
5. FDP Economics - Integrating All Components
5.1 Full FDP Cash Flow Model
| Cost/Revenue Category | Amount ($M) | Timing | Notes |
|---|---|---|---|
| Phase 1 Capex (tie-back) | -$1,850M | Years -3 to 0 | Subsea infrastructure, Phase 1 wells (12 wells x $55M), host platform modifications |
| Phase 2 Capex (FPSO) | -$2,200M | Years 5-8 | FPSO procurement and installation, additional wells (7 wells), gas pipeline to shore |
| Peak annual revenue | +$2,109M | Years 4-8 | 85,000 STB/day x 365 x $68/STB = $2,109M/year gross |
| Peak annual Opex | -$485M | Years 4-8 | 85,000 x 365 x $15.6/STB = $485M/year (offshore Opex) |
| Abandonment | -$380M | Years 23-26 | 29 well P&A + FPSO removal + subsea infrastructure removal |
| Total Capex | -$4,050M | Full field life | Phase 1 + Phase 2 + Abandonment |
| Total gross revenue | +$27,880M | Years 1-25 | 410 MMstb x $68/STB |
| Total Opex | -$6,396M | Years 1-25 | 410 MMstb x $15.60/STB |
| Total fiscal payments | -$8,350M | Years 1-25 | ~39% effective government take on net revenue |
| IOC net undiscounted cash flow | +$9,084M | $27,880 - $6,396 - $8,350 - $4,050 = $9,084M | |
| IOC NPV at 12% discount rate | +$1,480M | Full cycle NPV from pre-FEED through abandonment. Matches Concept C pre-FEED estimate - validates concept selection. |
5.2 FDP Risk Register - Key Development Risks
| Risk | Probability | NPV Impact | Expected Value Impact | Mitigation |
|---|---|---|---|---|
| Reservoir permeability P10 case (k=55 md) → 28 producers needed | 20% | -$520M (9 additional wells) | -$104M | Drill 3 pilot wells before committing to full program. Expandable well slot design. |
| Aquifer weaker than modeled → recovery factor 75% vs 91% | 25% | -$680M (65 MMstb less EUR) | -$170M | Design water injection capacity into Phase 1 facilities (headered but not initially installed). |
| Phase 2 FPSO cost overrun +25% | 30% | -$550M additional Capex | -$165M | Lump-sum EPC contract with performance bonds. Fixed-price bidding from ≥3 qualified contractors. |
| Oil price falls to $45/bbl at Phase 2 decision point | 20% | Phase 2 deferred → -$380M NPV | -$76M (but deferral option limits downside) | Concept C deferral option: Phase 2 FID only if oil price >$42/bbl breakeven. Do not commit Phase 2 at Phase 1 FID. |
| Host platform life extension denied → tie-back limited to 8 years | 10% | -$220M (accelerate Phase 2) | -$22M | Negotiate 15-year tie-back agreement before FID. Include contractual compensation for early termination. |
Conclusion
The two-rig drilling schedule analysis in this article - $492.9M NPV from production acceleration at a $99M second rig cost, a 5:1 ROI - demonstrates that the well program timing decision is often the highest-return investment in the entire FDP. This result surprises engineers who have spent months optimizing facility costs and negotiating contractor rates, because the acceleration value calculation is rarely performed explicitly in pre-FEED. The instinct to minimize visible cost (rig day rates are a line item on every weekly operations report) without quantifying the invisible cost of deferred production (the value of oil produced in Year 4 versus Year 6) systematically leads to under-drilling during development and leaves hundreds of millions of dollars of NPV on the table in major developments. The second rig does not appear in the Capex budget as a $492.9M value creation opportunity - it appears as a $99M cost. Only the explicit acceleration value calculation reveals the true economics.
The concept selection scoring - Concept C (phased development) scoring 4.60 versus Concept B (tie-back only) at 4.10 and Concept A (standalone FPSO) at 3.30 - demonstrates the value of the real option embedded in the phased approach. Concept C achieves the same first production date as Concept B (3.5 years) and the same ultimate production rate as Concept A (85,000 STB/day), while preserving the option to defer Phase 2 capital commitment until the reservoir has been producing for 5 years and the aquifer strength, permeability distribution, and commodity price environment are better understood. This optionality is worth $230M in NPV terms (Concept C $1,480M vs Concept B $920M in the base case) because it eliminates the downside scenario where $2.2 billion of Phase 2 capital is committed at FID only for the oil price to fall to $45/bbl before the FPSO produces a single barrel.
For engineers and economists looking to build expertise in field development planning and concept selection, the following references provide comprehensive frameworks and case studies: Field Development Planning and Petroleum Project Management covers FDP structure, concept selection methodology, and execution management, while Applied Petroleum Reservoir Engineering and Production Forecasting provides the quantitative reservoir engineering foundation for well count optimization and production profile construction.
Want to access our FDP toolkit with concept scoring matrix, well count calculator, drilling schedule NPV optimizer, production profile builder, and risk register template, or discuss field development concept selection for a specific discovery? Join our Telegram group for field development and petroleum economics discussions, or visit our YouTube channel for step-by-step tutorials on FDP development, concept selection, and well program optimization.
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