Modifying the Libyan fiscal regime to optimise its oil reserves and attract more foreign capital part 2: application to CO2‐EOR project in Libya

AuthorSaad A. Balhasan,Jennifer L. Miskimins,Brian F. Towler
Date01 September 2013
Published date01 September 2013
DOIhttp://doi.org/10.1111/opec.12001
Modifying the Libyan fiscal regime to
optimise its oil reserves and attract more
foreign capital part 2: application to
CO2-EOR project in Libya
Saad A. Balhasan,* Brian F. Towler** and Jennifer L. Miskimins***
*PhD Candidate, Chemical and Petroleum Engineering Department, University of Wyoming, Laramie, WY,
USA. Email: sbalhasa@uwyo.edu; sbalhasan@yahoo.com
**Professor of Chemical and Petroleum Engineering, CES Fellow for Hydrocarbon Energy Research,
University of Wyoming, Laramie, WY, USA
***Associate Professor, Colorado School of Mines, Golden, CO, USA
Abstract
This paper extends the analysis of our proposed modification to the first model of Libyan Explora-
tion and Production Sharing Agreement (LEPSA I) to field applications. Four decision-making
models are coded in a spreadsheet program to estimate profitability indicators for two development
scenarios. These scenarios are primary and secondary recovery methods with water injection and
enhanced oil recovery byinjecting carbon dioxide. The paper concludes that the economic profit for
the foreign investor (second party) under LEPSA I was improved compared with EPSA IV.Also,
Libya increased its oil reserves with a reasonable decrease of its production share. Moreover, the
results showed that the profit indicators under the current production shares (cost recovery) of the
fourth model of Exploration and Production Sharing Agreement (EPSA IV) were not favourable to
the second party. Because of that, the second party would not be motivated to make a decision to
investany money for an oil development projects in Libya. Finally,the paper investigates how EPSA
IV should be redesigned to maximise the Libyan National Oil Corporation (first party) oil reserves
and give more attention to the economic objectivesof the second par ty.
Nomenclature
A The A value at the indicated ratios of the cumulativevalue
of petroleum received by second party overthe cumulative
petroleum operations expenditure by the SP
B The B value at the indicated levels of the average total
daily production of oil and LHP
C Constant of proportionality, %
CAPEX Capital expenditure, US$
CAPEXincremental Incremental capital expenditure, %
270
© 2013 The Authors. OPEC Energy Review © 2013 Organization of the Petroleum Exporting Countries. Published by
John Wiley & Sons Ltd, 9600 Garsington Road, Oxford OX4 2DQ, UK and 350 Main Street, Malden, MA 02148, USA.
CAPEXinitial Initial capital expenditure, US$
CAPEXSR% Capital expenditure of secondary recovery,%
CAPEXTR% Capital expenditure of tertiary recovery, %
$CAPEXinitial Initial capital expenditure, US$
$CAPEXSR Capital expenditure of secondary recovery,US$
$CAPEXTR Capital expenditure of tertiary recovery,US$
CO Cost oil, %
COR Cost oil revenue, US$
DS Development share, %
FP NCF (t) First party net cash flow at yearn, US$
FPS First party share, %
Gp Gas production, MMcf/d
HCPVI Injected hydrocarbon pore volume
LHP Liquid hydrocarbon by product
LHPp Liquid hydrocarbon by product production, stb/d
Np Oil production, stb/d
NpbBonus of oil production, US$
OPEX Operating expenditure, US$
$OPEXSR Operating expenditure of secondary recovery,US$
$OPEXTR Operating expenditure of tertiary recovery,US$
OPEXSR% Operating expenditure of secondary recovery,%
OPEXTR% Operating expenditure of tertiary recovery, %
P Probability, %
Pg Gas price, US$/Mcf
Plhp Liquid hydrocarbon by product price, US$/b
Po Oil price, US$/b
Por Reference oil price, US$
POS Probability of success, %
Pot Oil price at time, US$
rk Capitalcost
R Ratio of the cumulative value of production received by
second party over the cumulative petroleum operation
expenditures incurred by the second party
SiInitial share, %
SP NCF (t) Second party net cash flow at yearn, US$
SPS Second party share, %
pEXS Excess profit, US$
pEXSg, pEXSlhp, pEXSo Excess profit of gas, LHP and oil, US$
CO2-EOR project in Libya 271
OPEC Energy Review September 2013© 2013 The Authors.
OPEC Energy Review © 2013 Organization of the Petroleum Exporting Countries
1. Introduction
The present fiscal regime in Libya is Exploration and Production Sharing Agreement IV
(EPSA IV). The Libyan fiscal regime under EPSA IV is not a favourable model for the
second party (SP), especially for a heavy investmentlike enhanced oil recovery (EOR) and
offshore projects. Therefore, EPSA IV mayhave serious effects on the field development
methods and the volume of recoverable reserve calculations. In part one of this series of
papers, a new model, LibyanExploration and Production Sharing Agreement I (LEPSA I),
was introduced,aiming to maximise the reser ves for the LibyanNational Oil Cor poration
(LNOC), designated the first party (FP), and profit for the foreign investor, designated the
SP.A coded spreadsheet program has been built for the EPSA IV and LEPSA I models for
the two developmentscenarios. The four programmed models are incorporated with deci-
sion variables of oil rate, gas rate, liquid hydrocarbon product (LHP) rate, oil prices, gas
prices, LHP prices, exploration costs, development costs, operation costs, oil production
bonuses, cost recovery, cost of capital, equity split models and profit indicators. The
models were used to evaluate the profitability indicators, net present value (NPV) and
internal rate of return (IRR). Because the FP is focused on the EOR to raise its oil produc-
tion and oil reserves, many of the studies carried out by the FP on many reservoirs deter-
mined the acceptable EOR methods for the FP’s reservoirs’ circumstances. Some basic
assumptions on CO2flooding1provided byOccidental Oil Company (OXY) are utilised in
this study.These r ules were based on experience, applied by OXY in their oil fields.The
hyperbolic decline model is used when the relativepermeability dominated secondar y and
tertiary recovery processes, such as water and EOR, by injecting CO2(Masoner, 1998).
Based on this fact, the hyperbolic decline model has been selected for the field production
profile for forecasting the water and CO2injection scenarios. For the second development
scenario, the two models assumed that the CO2project has been started 12 years after the
beginning of the field production. The project will take 3 yearsto complete the CO2infra-
structure upgrades and 1 year to develop the production mechanism. The oil prices
are assumed to fluctuate between US$ 80 and US$ 90/b, the gas prices are assumed to
fluctuate between US$ 4 and US$ 5/MMBtu and the condensate prices can be assumed to
fluctuate between US$ 80 and US$ 95/b for the agreement life. Moreover, the economic
indicators NPV and IRR were used as tools to determine which model is preferable for the
SP. In spite of all 24 cases in the second scenario plans of the oil recovery having a cash
flow income–investment–income,the dual IRR did not appear in the cash flow of EPSA IV
and LEPSA I models. The feasibility study for the developmentscenarios for the four pro-
grammed models has showed that the LEPSA I model is more attractiveto the SP than the
current model of EPSA IV.The LEPSA I model has shown how the increase in investment
with the step function will increase the SP share of profit and the field recovery factor
(RF) for the FP. In spite of the reinvestment for the CO2injection project, the maximum
Saad A. Balhasan, Brian F. Towler and Jennifer L. Miskimins272
OPEC Energy Review September 2013 © 2013 The Authors.
OPEC Energy Review © 2013 Organization of the Petroleum Exporting Countries

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