joint reduction of petroleum consumption and carbon emissions · 2006-09-22 · joint reduction of...
TRANSCRIPT
Joint Reduction of Petroleum Consumption and Carbon Emissions
NETL/ANL Scenario Analysis Results“Peak Oil” and Other Sensitivities
USAEE/IAEE North American ConferenceSeptember 26, 2005
Peter C. Balash1 and Donald A. Hanson2
1Economist, National Energy Technology Laboratory2Economist, Argonne National Laboratory
Disclaimer/acknowledgements
• We would like to thank our co-authors and colleagues:• Dave Schmalzer, ANL Dale Keairns, NETL • John Molburg, ANL Kathy Stirling, NETL, ret.• John Marano, ANL/NETL Ken Kern, NETL• And other colleagues for their helpful comments along
the way• This work is funded by the National Energy Technology Laboratory,
Pittsburgh, PA, Morgantown, WV and Tulsa, OK, and performed using the AMIGA economic model from Argonne National Laboratory, Chicago, IL.
• All views expressed are those of the authors and should not be construed to reflect the policies or views of the United States Department of Energy, the National Energy Technology Laboratory, or Argonne National Laboratory.
Outline
• Scope• Review of Initial Results• Sensitivity Cases• Future Work• Model information
Scope and Accomplishments
• Presidential goals of reduction in petroleum consumption of 11 million barrels/day and 500 million tonnes carbon by year 2040.
• Transform Presidential objectives into alternative scenarios for use in economic model− Interpret Goals as reductions from baseline
• High-level economic analysis of technology and the ‘hydrogen economy”− Integrate rigorous engineering cost estimates with
macroeconomic model
Coal-Fuels Substitution and Efficient Vehicles Meet Presidential Reduction Goals
• Goals met through− Penetration of more efficient vehicle technologies, either
hybrid-electric (HEVs) or fuel cell vehicles (FCVs)− Carbon capture from Integrated Gasification Combined
Cycle and power-fuels coproduction plants− Moderate substitution of coal-Fischer-Tropsch fuels for
petroleum• Sensitivities stress importance of coal in both “peak
oil” and Kyoto-type carbon-reduction cases• Coal consumption rises significantly in all cases
Technical Challenges
• Integration of cost and performance specifications of refinery and coproduction plants with AMIGA economic model.− Important for richer representation of investment
choices• Implementation of DOE’s H2A production cost
estimates −Must assume technological breakthrough in FCV
case• Identification of appropriate performance
characteristics of advanced vehicles
Scenario Structure
• Uses Presidential reduction goals as drivers−Reductions from future, not current, levels−H2-economy based on FCVs a possible means to
achieving quantitative goals, not an end in itself• As distinct from Academy study (2004)
• replacement of petroleum-based light-duty vehicle fleet, or • DOE H2 Posture plan (2005)
• Focus on renewable hydrogen
• Recognition of scientific debate− E.g. Romm (2004), Shinnar (2003), Demirdöven and Deutch
(2004)
Petroleum Target
0
5
10
15
20
25
30
35
2005 2025 2040
AEO2005 AMIGA
21 21
28 27
35
3111mmb/d reduction
from AMIGA ref.
implies future consumption
at today’s levels
Mill
ion
barr
els p
er d
ay
Source: EIA AEO2005 Yearly Table 11; author extrapolation;AMIGA reference run
Carbon Emissions Target
0
500
1000
1500
2000
2500
2005 2025 2040
AEO2005 AMIGA Ref
1171 1169
1645 1562
2151
1761C target
reduction from AMIGA ref. reduces C to level ~7%
above today’s
Mill
ion
Met
ric to
ns C
eq.
per
yea
r
Source: EIA AEO2005 Yearly Table 18 (transport petroleum; electric power); author extrapolation; AMIGA reference run
Scale of Challenge
Small Car
Large Car
Conv. SUV
Large SUV
HEVs
Small Car
Large Car
Conv. SUV
Large SUV
HEVs
0
50
100
150
200
250
300
350
2005 2040
Vehicle Stock Increases
63%
Source: AMIGA Reference Run
Mill
ions
of V
ehic
les
How to Achieve CutsReference Case:“Business as usual”
Extended TransitionHybrid-electric vehiclesand Clean Hydrocarbons“HEV case”
Hydrogen AchievementHydrogen Production for Fuel Cell Vehicles“FCV case”
Oil Prices From $37/b in 2010; Gas Prices from $6/mmBtu
Coal Power/Fischer-Tropsch Co-Production Plants
DOE H2 Posture Plan guidelines
“Clear Skies”-Like Emissions Targets
Energy Security Charges on premium fuels from 2010
H2A program (DOE EE)H2 cost data
Gasification, Hydrotreating and Clean fuels Refinery Modeling
Carbon Charges on Electricity generation from 2015
More stringent clean air regulations begin in California
Nuclear Generating Capacity Constant
Four size categories of Hybrids; eventual Plug-Ins
Technological “breakthroughs”assumed
Assumptions are kept from left to right
Externality Charges
$ per metric ton C;$ per barrel oil
More stringent
anti-smog measures
+ higher fuel economyimplies lower
C charge for
FCV case
Source: AMIGA Presidential Goals Scenario Runs
0
10
20
30
40
50
60
70
80
2005 2010 2015 2020 2025 2030 2035 2040
Reference Carb Ch - HEV Carb Ch - FCV ES Prem - HEV ES Prem - FCV
Model optimizes imposition of charges
Effective Oil Prices
0
10
20
30
40
50
60
70
2005 2010 2015 2020 2025 2030 2035 2040
World Oil Price ES charge per bbl Carb Ch per bbl
0
10
20
30
40
50
60
70
2005 2010 2015 2020 2025 2030 2035 2040
World Oil Price ES charge per bbl Carb Ch per bbl
$/bb
l
HEV-only Case HEV+FCV case
Externality charges result in higher effective than nominal oil prices;Slightly higher imputed carbon and energy security charges in HEV-only case
Source: AMIGA Presidential Goals Scenario Runs
Vehicle Stocks
0
50
100
150
200
250
300
2005 2010 2015 2020 2025 2030 2035 2040
ICEs HEVs FCVs
0
50
100
150
200
250
300
2005 2010 2015 2020 2025 2030 2035 2040
ICEs HEVs
Mill
ion
vehi
cles
Extended Transition Hydrogen Achievement
Source: AMIGA Presidential Goals Scenario Runs
Internal Combustion Engines decline but remain;
externality charges drive adoption of alternative vehicles
Reduced Petroleum Consumption
Source: AMIGA Presidential Goals Scenario Runs - HEV case
Mill
ion
barr
els p
er d
ay
0
5
10
15
20
25
30
2005 2010 2015 2020 2025 2030 2035 2040
FT-Fuels Offset Other fuels vehicle fuels
15% of goal met by coal-fuels substitution; 85% through efficiency
Consumption v. Share of HEV Sales
0
2
4
6
8
10
12
14
16
2005 2010 2015 2020 2025 2030 2035 2040
mm
b/d
0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
% n
ew c
ar s
ales
LDV oil con., BAULDV oil cons, HEV casehybrid sales, BAUhybrid sales, HEV case
HEV new car sales must reach ~45% before consumption falls
Source: AMIGA Presidential Goals Run
HEV wedge
0
5.8
3.9
2.3
1.1
0.40.1
8
0
1
2
3
4
5
6
7
8
9
2005 2010 2015 2020 2025 2030 2035 2040
HEV wedge
Fall in consumption due to HEV penetration
mmB/d
Source: AMIGA Presidential Goals Run
Hydrogen Production, FCV case
0
5
10
15
20
25
30
35
2020 2025 2030 2035 2040
CoaltoH2SMR_Distrb
By 2030, distributed Steam Methane Reforming
H2 production Eclipsed by
Coal to H2 plants
Source: AMIGA Presidential Goals Scenario Runs,FCV Case
Bill
ion
Kilo
gram
s H
2
Caveat: Methane Hydrates?
Energy Supply to Vehicles, Extended Transition
0
500
1000
1500
2000
2500
3000
3500
4000
4500
5000
2005 2010 2015 2020 2025 2030 2035 2040
Petroleum Grid
Growth in Energy Input to Transport
Sector levels off as more efficient
plug-in HEVs become
prevalent
Source: AMIGA Presidential Goals Scenario Runs - HEV case
Trill
ion
Btu
s
GRID
PETROLEUM
Power Sector Generation by Fuel Type, Year 2040
447
3411
929
780
807
0
155
3288
1018
780
1029
137
26
3333
1073
780
1170
290
0
1000
2000
3000
4000
5000
6000
7000
reference FCV case HEV case
Coal Existing Coal New Gas & Oil Nuclear Renewables Fischer-Tropsch
Trill
ion
Wat
t Hou
rs
Source: AMIGA Presidential Goals Scenario Runs
Renewable Generation Capacity and Growth
0
200
400
600
800
1000
1200
1400
2005 2010 2015 2020 2025 2030 2035 20400%
2%
4%
6%
8%
10%
12%
14%
16%
18%
20%
Ref FCV HEV Refsh FCV share HEV share
Trill
ion
Wat
t Hou
rs
Sha
re o
f Pow
er S
ecto
r Gen
erat
ion
Source: AMIGA Presidential Goals Scenario Runs
All growth is in non-hydro renewables;Renewable share of total generation grows fastest in FCV case;
Absolute renewable capacity greatest in HEV case
Sensitivities
• HEVs are more efficient relative to both conventional Internal Combustion Engines and H2 FCVs than in the National Academy Study
• Higher carbon reduction targets would require more coal plant sequestration
• Sensitivities include − constrained oil supplies (eg “peak” oil from 2015)− less efficient advanced vehicles (consumers prefer
performance, no plug-in HEVs)− higher carbon reduction targets (Back to 1990 levels)− faster development of coal technologies (better FT
technology)
Light-Duty Vehicle Oil Consumption
0
2
4
6
8
10
12
14
16
2005 2010 2015 2020 2025 2030 2035 2040
BAU HEV FCV PEAK CO2 90 FT IMPR PERF
No Discernible difference in
HEV, CO2 1990,
AndFT-TechnologyImprovement
cases
Peak Oil after 2015 quickens pace
Performance over efficiency slows pace
of reductionsMmb/d
Source: AMIGA Presidential Goals Scenario Sensitivity Runs
Consumption can fall in long-term, but 15 years need elapse before more efficient vehicles lead to less consumption
Effective Oil Price Sensitivities, 2040
0
20
40
60
80
100
120
BAU2005
BAU HEV FCV PEAK CO2 FTIMPR
PERF
energy security charge carbon charge per bblworld oil price
Peak Oil removes need for energy
security premium as world oil price rises
Performance over efficiency forces
higher energysecurity premium
If real-time (2006) prices persist,Economics predict change will occur; declining oil supplies hasten technological change
Source: AMIGA Presidential Goals Scenario Sensitivity Runs
$/bbl
scenario
The Rise of Diesel
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
2000 2005 2010 2015 2020 2025 2030 2035 2040 2045
ReferenceHEV CaseFCV Case
Distillate share of premium fuels
Source: AMIGA Presidential Goals Scenario Sensitivity Runs
Refinery Fuel Mix and the Transition to Alternative Vehicles
• Reference Case – Current refinery configuration, optimized for gasoline production using fluid catalytic cracking (FCC)− FCC capacity continues to grow with gasoline demand − FCC produces gasoline by rejecting carbon from heavier fuel oils
• Alternative cases – As crude consumption falls due to declining LDV gasoline demand, demand for diesel fuel remains strong− However FCC is not optimal for producing clean diesel fuel− Refiners have trouble meeting diesel fuel demand and quality as the ratio of
gasoline to diesel produced from a barrel of oil decreases− Refinery hydrocracking capacity increases to provide higher quality diesel− Unlike FCC, hydrocracking adds large amounts of hydrogen to heavier fuel
oils
• In the HEV case, about 55% of current FCC capacity would need to be replaced with new hydrocracking capacity by 2040; additional hydrocracking capacity would also need to be built to meet incremental growth in diesel demand− Conversion of existing FCC-based refineries to hydrocracking refineries is
feasible but expensive, and would require a huge amount of additional refinery hydrogen production, resulting in increased diesel fuel prices
Carbon Emission Sensitivities
0
500
1000
1500
2000
2500
2005 2010 2015 2020 2025 2030 2035 2040
BAU HEV FCV PEAK CO2 90 FT IMPR PERF
MM metric tons C
year
Small DifferencesBetween FCV, HEV,FT-improvement, and Performance cases
Kyoto-like targets reduce carbon levels through…
Source: AMIGA Presidential Goals Scenario Sensitivity Runs
Carbon Capture, 2040
0
100
200
300
400
500
600
700
BAU HEV FCV PEAK CO2 90 FT IMPR PERF
IGCC CarbCapture FT CarbCapture Seq from H2A plants
MM metric tons C
More widespread capture employed
to reach stricter C targets
Capture @ H2 producing plants
Source: AMIGA Presidential Goals Scenario Sensitivity Runs
Sectoral C emissions, 2040
0
200
400
600
800
1000
1200
1400
1600
1800
base FCV HEV FT PERF CO2 1990 PEAK
Power TransportH2 plants
mm
Mt C
For deepest cuts Power sector most economic
Source: AMIGA Presidential Goals Scenario Sensitivity Runs
Coal Use by plant type, 2040
Source: AMIGA Presidential Goals Scenario Sensitivity Runs
0
5
10
15
20
25
30
35
40
45
base 2005 BAU HEV FCV PEAK FT PERF CO2 90
Adv coal pwrOld coal pwrOther Coal FT Coal Feed
Wide variation in plant type: Peak Oil and Performance Vehicle
scenarios call forth substantially more FT
Quads
Rising Coal Use
BAU
HEV
FCV PERF
CO2 1990
Peak oil
0
500
1000
1500
2000
2500
2005 2030 2031 2032 2033 2034 2035 2036 2037 2038 2039 2040
BAU HEV FCV PERF CO2 1990 Peak oil
Source: AMIGA Presidential Goals Scenario Sensitivity Runs
Substantial increase in coal utilization in all scenarios
Mill
ion
sho
rt to
ns
CTL Plant Additions
Source: AMIGA Presidential Goals Scenario Sensitivity Runs
-
10
20
30
40
50
60
70
80
90
2010 -2015 2 015 -2020 2 020 -2025 20 25 -2 030 203 0 -20 35 2035 -204 0
F C VH E VP E A KP E R F
Vertical scale dependent on plant size,but relative increments invariant
Number of Plants @9,266 tonsper day coal feed
Coal Use and Reserves
Source: AMIGA Presidential Goals Scenario Sensitivity Runs
129123
115
116113
111
-
50
100
150
200
250
300
2005reserves
2040reserves
2005 R/P 2040 R/P
PERFFCV
HEVPeak oil
CO2 1990BAU
Billi
on s
hort
tons
; Yea
rs L
eft
267 billion tons of reserves in 2004
245 years of production
left in 2004
No reserve growthassumed. Increase in
coal use for power,CTL and/or H2
reduces R/P ratio by ~ half, in 35 years
Future Work/Possible Extensions
• Implementation of alternate coal-synfuel pathways
• Construction of ethanol and biomass co-firing modules
• Incorporate recent H2A delivery cost estimates
• Continual upgrading of existing modules
Appendix
• Model information
The AMIGA Model
• AMIGA is a Computable General Equilibrium (CGE) Model of the US economy with considerable sector detail
• It features characterizations of major end-use electricity- and gas- using technologies, and consumer choice behavioral representations
• AMIGA includes reduced form representations of electricity generation and petroleum refining as they are embedded into the structure of the US economy
• AMIGA can be used to examine structural change in the economy arising from alternative future scenarios, including impacts from climate-related and/or energy-related policies.
The AMIGA Model
Bureau of Economic Analysis sectors of the economyGeneral model of production costs and pricesSpecific energy conversion technologies and capacities
Electric power generationHydrogen productionFuels refining
Market shares: Where are the margins?(often not a question of which is cheaper but at what market shares do marginal costs equate; there may be some role/niche for many energy technologies).
Supply and Demand equal in all marketsIncome and price effects, e.g., income effects of reducing oil imports
Flows Within the AMIGA Energy-Economic Model
Coal Power/FT Fuels
• Plant Products− 1.63 bpd of F-T liquid fuel precursors/ton per day of dry
coal feed− 33 kWe/ton per day of dry coal feed
• Capital Cost: $135,000 per ton per day of dry coal including carbon capture w/o sequestration (2003 $)
• Carbon for sequestration: 53% of carbon in coal feed− Lower cost than capture from a power only plant
Source: Dale Keairns and Richard Newby, 2005, “Fuels and Electric Co-Production Plant Cost and Performance Projections,”NETL working paper
Future F-T Liquid Cost Forecast
• Projection for cost of F-T liquid production represented by increase in performance for the reference case investment
• Assume consistent with advanced coal plant performance used in NETL benefit studies
• Project ~20% increase in capacity during 2030-2040 time frame.
Source: Dale Keairns and Richard Newby, 2005, “Fuels and Electric Co-Production Plant Cost and Performance Projections,”NETL working paper
Plant Design Basis Choices
• Plant capacity and availability• Fuel and plant location• Product distribution (fuel, power)• Technology selection (state-of-art,
advanced)• Design choices (e.g. spare gasifiers)• Emissions control• Degree of CO2 capture• Degree of F-T upgrading
Source: Dale Keairns and Richard Newby, 2005, “Fuels and Electric Co-Production Plant Cost and Performance Projections,”NETL working paper
High F-T Liquid Plant With Carbon CaptureCase 3
AGR MDEA & AC Sulfur
Polishing
Coal Gasifier E-Gas & Heat
Recovery
Low-Temperature Gas Cleaning
F-TSynthesis
Liquid FuelPrecursors
Coal
ASUAir
Oxidant
WGS System &CO2 AbsorberReheat Compress
Off-gas
Steam
CO2 toSequester
Sulfur
HalidesAmmoniaMercury Steam
GasTurbine
HRSG &Steam Cycle
AirSteam
Power StackGas
Power
Steam
Source: Dale Keairns and Richard Newby, 2005, “Fuels and Electric Co-Production Plant Cost and Performance Projections,”NETL working paper
Plant Performance ResultsCarbon capture significantly reduces net plant power
Base Plant Case 2 Plant Case 3 Plant
Coal feed rate (TPD)
9,266 9,266 9,266
Liquid fuel precursors (BPD)
12,377 15,063 15,063
Net Plant Power (MW)
675.9 543.8 307.8
Liquid fuel-to-Power (BPD/MW)
13.7 27.7 48.9
Thermal Efficiency (HH%)
52.8 54.4 46.2
Source: Dale Keairns and Richard Newby, 2005, “Fuels and Electric Co-Production Plant Cost and Performance Projections,”NETL working paper
Plant Carbon BalanceBase Plant Case 2 Plant Case 3 Plant
Coal carbon input (TPD) 6,488 6,488 6,488
Carbon in slag (TPD) 308 308 308
Carbon in stack gas (TPD) 4,952 4,626 1,202
Carbon in liquid fuel (TPD) 1,477 1,797 1,826
Carbon in CO2 sequester stream (TPD)
0 0 3,430 (53% of coal C)
Total carbon not emitted to stack (% of coal C)
23.7 28.7 81.5
CO2 reduction from Base Case (%)
--- 6.6 75.8
Source: Dale Keairns and Richard Newby, 2005, “Fuels and Electric Co-Production Plant Cost and Performance Projections,”NETL working paper
Plant Cost Estimates
Base Plant Case 2 Plant Case 3 PlantSolids Handling Area 28,317 28,317 28,317Air Separation Unit 149,791 149,791 149,791Coal Gasification Area 434,094 434,094 434,094F-T Liquids Area 94,283 108,180 108,180Water-Gas Shift Area 0 0 8,630CO2 Removal Area 0 0 44,467CO2 Compression Area 0 0 48,200Power Block 348,788 308,220 246,764BOP 103,785 103,785 103,785Total (mid-2000$) 1,159,058 1,132,386 1,172,228Total (esc. Mid-2003$) 1,239,033 1,210,521 1,253,112
Source: Dale Keairns and Richard Newby, 2005, “Fuels and Electric Co-Production Plant Cost and Performance Projections,”NETL working paper
Macro Analysis of Petroleum Refining SystemsOverview
• MARS is a working prototype refinery forecasting model− Represents 26 primary & secondary refinery processes− Also includes representation of CTL co-production plant
feeding eastern or western coal− Includes 8 major refinery products including gasoline, diesel &
jet fuel− Includes existing regional capacities with provision to expand
existing process capacities during forecast period − Assays for six crude types represented: Low-Sulfur Light, MS
Heavy, HS Light, HS Heavy, HS Very-Heavy, Syncrude
SMR
MARS U.S. Refinery Configuration
Crude Oil
DLC
Prm Gasoline
Reg Gasoline
Field Butanes
Natural
Gasoline
Purchased
EthanolI4O
GSF
LPG
Kerosene(Jet Fuel)
DFO
Petcoke
RFO
Asphalt
Diesel
SRU
PFS
Sulfur
SGPUGP
SFA
Dist
Pool
ISO
NHTDHX
KHTACU
VCU
LPR
DHT
GHT
HCK
CCU
ARD
GDS
HSR
LSR
SRK
SRD
AGO
VGO
VRC
n-Butane
LSR/DHO/HCL
RFT
ISO
ALK
CCLN/CCHN
CSO
HTCN
HTK
SRD
HTD
HCK
HCD
H2
H2
H2
NGS,RGS
H2S
NGS,RGS
ARC
Gaso
Pool
MARS Coal-To-Liquids Submodels
• Coal-To-Liquids (CTL)− Yields for Eastern & Western Coal with and without
CO2 capture & sequestration− Yield of FT Liquids & Power fixed− Sulfur yield by S balance− FT raw product distribution & properties fixed− Utilities consumption fixed
• FT Liquid Hydroisomerization (FHI)− Upgrading assumed to occur at refinery via
hydrotreating, hydrocracking & isomerization− Products: FT Light & Heavy Naphthas, FT Kerosene
& FT Diesel− Hydrogen consumption & product yields fixed− Utilities consumption fixed
FT Liquids Upgrading
lgt Naph
Syncrude C5+
700+ Recycle
Purge
H2 Rec
Purge
H2 Rec
FT Dist C5+
FT Reactor Wax
HDT HIS
H2 Makeup H2 Makeup
• Other product slates are possible besides all light products− Degree of FT wax cracking can be controlled by adjusting
reactor severity & recycle to produce FT Gas Oil− Allows greater flexibility in producing desired ratio of
gasoline to diesel from the refinery
FT Liquids Upgrading OptionsHIS Minimum Conversion
10%26%
25%11%
28%
Naphtha
KeroseneDistillate
Gas Oil
LPG
Max.Gaso.= LPG+.8 Naph.+.75 G.O.= 52%
HIS Maximum O/T Conversion
26%
32%15%
17%
10% Naphtha
Kerosene
Distillate
Gas Oil
LPG
HIS 100% Conversion
34%
36%
19%
11%Naphtha
Kerosene
Distillate
LPG
Max.Dsl.= Dst.+Kero.= 55%Max.Jet.= Kero.+.25 Naph.= 45%
This is representation currently in MARS…but is least likely to be pursued
for “remotely” located GTL/CTL plants
MARS Economic Model
Corporation
E&CContractor
Lenders
Investors
Federal & StateGovernments
Consumers
EmployeesVendorsSuppliers
EmployeesVendorsSuppliers
OSBLoperations
ISBLoperation
CorporateFunds
Refinery
Gross Revenues
Depreciation Charge for Books
Taxable Income
Income Taxes
Repayment& Interest
Dividends
Debt
Equity
GeneralExpenses
Net Income
CashFlow
Project InvestmentsContractor’s Costs
OperatingIncome
OperatingCosts
Internal Revenue& Expense Flows
Macro Analysis of Petroleum Refining SystemsAccomplishments
• MARS model has been used by ANL/NETL to evaluate alternate pathways to reduced petroleum consumption and greenhouse gas emissions
• MARS can be executed as part of AMIGA−Could also be executed as stand-alone program, or −Excel submodels can be used individually or linked
together• Further upgrades to MARS are necessary to
perform wider range of analyses −Problems with near to mid term horizons−Regional issues and product transfers−Seasonality