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The Economic Viability of Carbon Capture and Sequestration
(CCS) Technologies: Value Chain Linkages from Capture to
Enhanced Oil Recovery (EOR) in Trinidad and Tobago
Nicole Crichlow n.crichlow.08@aberdeen.ac.uk +44 7503228058; +868 785-3465 www.abdn.ac.uk
University of Aberdeen, King's College, Aberdeen, AB24 3FX
Relevance of CCS to Trinidad and Tobago
-Trinidad and Tobago is a highly industrialised country due to its
oil and gas resources and its dramatic growth in the
petrochemical and steel industry.
-Alongside its economic growth was a significant increase in CO2
emissions
- T&T is the largest producer of CO2 per capita in the world.
-Clear imbalance in CO2 emission levels with respect to
population size (1.3 million) and gross domestic product (GDP).
-This undermines the sustainability of T&T’s development and
CCS has been a major topic of discussion.
Research Objective
This project:
 examines the economic viability of a proposed CCS plant
within the Point Lisas Industrial Estate in Trinidad and Tobago
and how it can be linked to EOR.
seeks to be a guide to the level of investment and risk involved
at each stage of the value chain.
Location of Point Lisas Industrial Estate relative to other important sites
Trinidad
Methodology
The analysis was broken down into two economic models linked
by the price of the captured CO2.
Framework for Model #1: CCS from the perspective of a potential investor
in the proposed centralised capture plant
Framework for Model #2- Demand for CO2 by EOR operations.
The models are linked with the Carbon capture plant being
treated as a supplier of CO2 to the Oil Company utilizing the CO2
for Enhanced Oil Recovery (EOR).
Model #2 considers the government’s role through legislation to
ensure sufficient demand for the captured CO2 versus the
cheaper natural CO2 as this would reduce incentives to
invest in CO2 capture.
Researcher: Nicole Crichlow
Excess Carbon Dioxide
stored in depleted oil
and gas reservoirs
Carbon Dioxide
Captured and
transported from the
centralized Capture
Plant
Majority CO2. is
supplied to oil
companies for
Enhanced Oil
Recovery
Anthropogenic Carbon
Dioxide sourced from
the Carbon Capture
Plant
Naturally existing Carbon
Dioxide derived in situ from
the reservoir, purified and
then re-injected
Oil Company
investing into
EOR and
therefore
demanding
Carbon Dioxide
Required investments; main risk
factors and their impact upon NPV
Local
adjustments due
to local
circumstances
eg. Very low
electricity price
Technological
plant lifetime,
materials used,
plant capacity
Financial
CAPEX, OPEX,
tax, cost of CO2,
oil price,
abandonment
costs, etc
Results
NPV of -239.165 mil US$ derived
from CAPEX being the main risk
factor.
The long term social cost of
mitigated carbon emissions is
892.5 mil US$
Conclusions
The Capture Plant is not
economically viable despite the
long term social cost benefits.
CAPEX- only variable
manipulated independently can
make the investment viable.
Results
NPV was minimal at 476,206USD.
Oil price- the greatest +ve
contributor to NPV. The amount
of anthropogenic CO2 - the
greatest -ve contributor.
Conclusions
Economically viable but risky as
a slight decrease in oil price
below 75US$ may lead to a
negative NPV
NPV is -ve if more than 50% of
the CO2 required is
anthropogenic.
Inputs/
Assumptions
Outputs
Main results and conclusions - Model #1
Main results and conclusions-Model #2
Economic
Modeling
Excel (model
building, NPV and
sensitivity analysis)
and Oracle Crystal
Ball (Monte Carlo
analysis) software

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Nicole Crichlow - Energy Institute presentation MSc Dissertation poster

  • 1. The Economic Viability of Carbon Capture and Sequestration (CCS) Technologies: Value Chain Linkages from Capture to Enhanced Oil Recovery (EOR) in Trinidad and Tobago Nicole Crichlow n.crichlow.08@aberdeen.ac.uk +44 7503228058; +868 785-3465 www.abdn.ac.uk University of Aberdeen, King's College, Aberdeen, AB24 3FX Relevance of CCS to Trinidad and Tobago -Trinidad and Tobago is a highly industrialised country due to its oil and gas resources and its dramatic growth in the petrochemical and steel industry. -Alongside its economic growth was a significant increase in CO2 emissions - T&T is the largest producer of CO2 per capita in the world. -Clear imbalance in CO2 emission levels with respect to population size (1.3 million) and gross domestic product (GDP). -This undermines the sustainability of T&T’s development and CCS has been a major topic of discussion. Research Objective This project:  examines the economic viability of a proposed CCS plant within the Point Lisas Industrial Estate in Trinidad and Tobago and how it can be linked to EOR. seeks to be a guide to the level of investment and risk involved at each stage of the value chain. Location of Point Lisas Industrial Estate relative to other important sites Trinidad Methodology The analysis was broken down into two economic models linked by the price of the captured CO2. Framework for Model #1: CCS from the perspective of a potential investor in the proposed centralised capture plant Framework for Model #2- Demand for CO2 by EOR operations. The models are linked with the Carbon capture plant being treated as a supplier of CO2 to the Oil Company utilizing the CO2 for Enhanced Oil Recovery (EOR). Model #2 considers the government’s role through legislation to ensure sufficient demand for the captured CO2 versus the cheaper natural CO2 as this would reduce incentives to invest in CO2 capture. Researcher: Nicole Crichlow Excess Carbon Dioxide stored in depleted oil and gas reservoirs Carbon Dioxide Captured and transported from the centralized Capture Plant Majority CO2. is supplied to oil companies for Enhanced Oil Recovery Anthropogenic Carbon Dioxide sourced from the Carbon Capture Plant Naturally existing Carbon Dioxide derived in situ from the reservoir, purified and then re-injected Oil Company investing into EOR and therefore demanding Carbon Dioxide Required investments; main risk factors and their impact upon NPV Local adjustments due to local circumstances eg. Very low electricity price Technological plant lifetime, materials used, plant capacity Financial CAPEX, OPEX, tax, cost of CO2, oil price, abandonment costs, etc Results NPV of -239.165 mil US$ derived from CAPEX being the main risk factor. The long term social cost of mitigated carbon emissions is 892.5 mil US$ Conclusions The Capture Plant is not economically viable despite the long term social cost benefits. CAPEX- only variable manipulated independently can make the investment viable. Results NPV was minimal at 476,206USD. Oil price- the greatest +ve contributor to NPV. The amount of anthropogenic CO2 - the greatest -ve contributor. Conclusions Economically viable but risky as a slight decrease in oil price below 75US$ may lead to a negative NPV NPV is -ve if more than 50% of the CO2 required is anthropogenic. Inputs/ Assumptions Outputs Main results and conclusions - Model #1 Main results and conclusions-Model #2 Economic Modeling Excel (model building, NPV and sensitivity analysis) and Oracle Crystal Ball (Monte Carlo analysis) software