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31st International Conference of the System Dynamics Society
Developing a Fair and Robust Energy Policy
Frank Blaskovich
Blaskovich Services, Inc.
31st International Conference of the System Dynamics Society
AGENDA
Slide 2
• Goals & Approach
• Model Design & Features
• Policy Development
• Example
• Summary
31st International Conference of the System Dynamics Society
GOALS & APPROACH
Slide 3
• Fair, robust policy
• Uncertainty difficult to quantify
• Technical and non-technical factors
• Start simple, add complexity
• Process most important
31st International Conference of the System Dynamics Society
MODEL DESIGN & FEATURES
Slide 4
• System Dynamics & Feedback
• Oil Production & Economics
• State & Producer
• Maximize NPV
31st International Conference of the System Dynamics Society
SYSTEM NARRATIVE
StateProducer
Energy Production
Slide 5
31st International Conference of the System Dynamics Society
SYSTEM NARRATIVE
HIGHER Taxes & Royalties => Higher State Revenue =>Higher State NPV
LOWER Taxes & Royalties => Higher Producer Profits =>
Higher Producer NPV
Higher Production => Higher Revenue =>
Higher NPV
Slide 6
31st International Conference of the System Dynamics Society
SYSTEM NARRATIVE
ProducerDevelopment Plan
Wells to drill
Facilities
Field Development(3 yr min)
Economicforecast
Production
Exponential declinebased on oil reserves
Producer Net Revenue(Gross Revenue - State
Royalty)
Producer Cash Flow(Net Revenue - Opex -
State Taxes)
Producer CashFlow Positive?
Yes
NoEnd of Field Life(Abandonment)
Essential Logic of Current Model
Slide 7
31st International Conference of the System Dynamics Society
SYSTEM MODEL
Slide 8
Oil Reserves Cum Oil
ProductionOil Rate
Decline RateInitial Oil Reserves
Max Well Oil Rate
Active WellsOil Price
Gross Oil Revenue
Discount Rate
Decline Point
<Decline Point>
Success Rate
Failure Factor
<INITIAL TIME>
<Time>
Drilling Cost PerWell
OPEX Cost Rate
Producer TotalCosts
Producer Net OilRevenue
State Royalty Rate
State Oil Revenue
Producer NPVState NPV
Time Conv Factor
CAPEX Costs
Facility CostRate
Development Time
<INITIAL TIME>
<Time>
Pipeline Tariff
<Oil Rate>
Pipeline OPEXCosts
State Prod Tax
<Producer TotalCosts>
OPEX Costs
Producer NetIncome Before Tax
State Income Tax
State Income TaxRate
Producer NCFBefore Tax
Producer NCFAfter Tax
<Producer NCFAfter Tax>
<State IncomeTax>
State RoyaltyIncome
<State RoyaltyIncome>
<DevelopmentTime>
Producer NCF AfterTax Last Year
End Of Field LifeEOFL Flag
<EOFL Flag>
Pipeline OPEXCorrelation
State Cum OilRevenue
Producer CumNCF After Tax
Wells DrilledEach Year
Total WellsDrilled
Drilling Rate PerYear
<Total WellsDrilled>
<Wells Required>
<Total WellsDrilled>
<Max Well OilRate>
Max Field OilRate
<Max Field OilRate>
<CAPEXDepreciation>
<UndepreciatedCAPEX Expensed>
<Field AbandonmentCost>
<Active Wells>
<CAPEXExpensed>
<State Prod TaxRate>
Oil Production
State Economics Producer Economics
Field Operations
31st International Conference of the System Dynamics Society
State NPV Producer NPV
SENSITIVITY RESULTS
Slide 9
Levers
Drivers
31st International Conference of the System Dynamics Society
REGRET ANALYSIS
Slide 10
• Uncertainties difficult to define
• Minimize impacts of “worst case” scenarios
• Regret = difference between best and actual outcomes
• Multiple futures, wide probability distributions
31st International Conference of the System Dynamics Society
REGRET DEFINITIONS
Slide 11
• Regret(s,f) = Maximum NPV(f) – NPV(s,f)
• Relative Regret(s,f) = Regret(s,f) / Maximum Regret(f)
• Equivalent Regret(s,f) = |State Relative Regret(s,f) – Producer Relative Regret(s,f)|
s = scenario (lever(s))
f = future (driver(s))
31st International Conference of the System Dynamics Society
REGRET EXAMPLE
Slide 12
Ta
x R
ate
State NPV
Maximum NPV
Failure
Decreasing NPV Increasing Regret
Minimum Regret
Maximum Regret
Future
31st International Conference of the System Dynamics Society
REGRET EXAMPLE
Slide 13
Future Oil Price = $100/stbInitial Oil Reserves = 200 mmstb
0.36
State NPV
3.8
(0.2)
3.1 Regret = 3.8 – 3.1 = 0.7
Regret = 3.8 – 3.8 = 00.72
0.80
Ta
x R
ate
0 Regret = 3.8 – 2.3 = 1.5
State Regret
2.3
31st International Conference of the System Dynamics Society
REGRET EXAMPLE
Slide 14
0.36
State Regret
0
0.7 Relative Regret = 0.7 / 1.5 = 0.4
Relative Regret = 0 / 1.5 = 00.72
0.80
Ta
x R
ate
Relative Regret = 1.5 / 1.5 = 1.00
State Relative Regret
1.5
Future Oil Price = $100/stbInitial Oil Reserves = 200 mmstb
31st International Conference of the System Dynamics Society
REGRET EXAMPLE
Future Oil Price = $100/stbInitial Oil Reserves = 200 mmstb
Possible Solution
0.36
State Rel Regret
0
0.4
0.72
0.80
Ta
x R
ate
0
Prod Rel Regret
0.4
0.8
01.0
0.0
0.8
1.0
Equiv Regret
Slide 15
31st International Conference of the System Dynamics Society
STATE RELATIVE REGRET
Slide 16
Non-optimal solutions
31st International Conference of the System Dynamics Society
PRODUCER RELATIVE REGRET
Slide 17
Non-optimal solutions
31st International Conference of the System Dynamics Society
EQUIVALENT REGRET
Slide 18
Equivalent regret solutions
31st International Conference of the System Dynamics Society
NPV vs PRICE & RESERVES
Slide 19
State NPV Results Producer NPV Results
31st International Conference of the System Dynamics Society
SUMMARY
Slide 20
• Fair & robust policies require compromise and consideration of unexpected events
• System Dynamics & Regret Analysis are useful policy development & analysis tools
• Other factors also need to be considered
31st International Conference of the System Dynamics Society
Slide 21
Questions or Comments?