Klaus Lackner CEIC Seminar 1-16-08

Managing Emissions from Fossil Resources

A Challenge to Technology and Policy

Klaus S. Lackner

Columbia University

December 2007

IPCC Model Simulations of CO2 Emissions

Growth in Emissions

0

2

4

6

8

10

12

14

16

18

2000 2010 2020 2030 2040 2050 2060 2070 2080 2090 2100

Year

Frac

tiona

l Cha

nge

Constant Growth 1.6% Plus Population Growth to 10 billion Closing the Gap at 2%

Energy intensity drop 1%/yr Energy Intensity drop 1.5%/yr Energy Intensity drop 2% per year

Constant growth

Plus Population Growth

Closing the Gap

1% energy intensity reduction

1.5% energy intensity reduction

2.0% energy intensity reduction

Resource Will Not Run Out

H.H. Rogner, 1997

Carbon as a Low-Cost Source of Energy

H.H. Rogner, 1997

Lifti

ng C

ost

Cumulative Gt of Carbon Consumed

US1990$ per barrel of oil equivalent

Cumulative Carbon Consumption as of1997

Refining

Carbon

Diesel

Coal

Shale

Fossil fuels are fungible

Tar

Oil

NaturalGas

Jet Fuel

Heat

Electricity

Ethanol

Methanol

DMEHydrogen

SynthesisGas

The Challenge:Holding the Stock of CO2 constant

Constant emissions at 2010 rate

33% of 2010 rate

10% of 2010 rate0% of 2010 rate

Extension of Historic Growth

Rates

560 ppm

280 ppm

Pacala and Socolow, Science 305, 968 – 972, (2004)

Orders of Magnitude

A Triad of Large Scale Options

• Solar– Cost reduction and mass-manufacture

• Nuclear– Cost, waste, safety and security

• Fossil Energy– Zero emission, carbon storage and

interconvertibility

Markets will drive efficiency, conservation and alternative energy

Small Energy Resources

• Hydro-electricity– Cheap but limited

• Biomass– Sun and land limited, severe competition with food

• Wind– Stopping the air over Colorado every day?

• Geothermal– Geographically limited

• Tides, Waves & Ocean Currents– Less than human energy generation

CCS is technically feasible

It is affordable

It can start today

It is likely to be a major contributor to CO2 reductions

worldwide

Dividing The Fossil Carbon Pie

900 Gt C

total

550 ppm

Past

10yr

Removing the Carbon Constraint

5000 Gt C

totalPast

Net Zero Carbon EconomyNet Zero Carbon Economy

CO2 from distributed emissions

Permanent & safe

disposal

CO2 from concentrated

sourcesCapture from power

plants, cement, steel, refineries, etc.

Geological Storage Mineral carbonate disposal

Capture from air



Permanent & safe disposal


sources

Capture from power plants, cement, steel,

refineries, etc.


Capture from air

Underground Injection

statoil

Gravitational TrappingSubocean Floor Disposal

Energy States of CarbonCarbon

Carbon Dioxide

Carbonate

400 kJ/mole

60...180 kJ/mole

The ground state of carbon is a mineral

carbonate

Bedrock geology GIS datasets – All U.S. (Surface area)120°W130°W

110°W

110°W

100°W

100°W 90°W

90°W

80°W

80°W

70°W

25°N 25°N

30°N 30°N

35°N 35°N

40°N 40°N

45°N 45°N

$0 1,000,000Meters

Legend

ultramafic rock

67°W

67°W

66°W

66°W

65°W

18°N

18°N19°N

0 140,000Meters

Puerto Rico

8733 km2

920 km2

166 km2Total = 9820 ±100 km2

Mineral Sequestration

Mg3Si2O5(OH)4 + 3CO2(g) → 3MgCO3 + 2SiO2 +2H2O(l)+63kJ/mol CO2

Rockville Quarry

Belvidere Mountain, Vermont

Serpentine Tailings

Oman Peridotite

Photo: Juerg Matter



Permanent & safe

disposal


sourcesCapture from power

plants, cement, steel, refineries, etc.


Capture from air

Many Different Options

• Flue gas scrubbing– MEA, chilled ammonia

• Oxyfuel Combustion– Naturally zero emission

• Integrated Gasification Combined Cycle– Difficult as zero emission

• AZEP Cycles– Mixed Oxide Membranes

• Fuel Cell Cycles– Solid Oxide Membranes

CO2 N2

H2OSOx, NOx and

other Pollutants

Carbon

Air

Zero Emission Principle

Solid Waste

Power Plant

Boudouard Reaction

C + O2 CO2no change in mole volumeentropy stays constantΔG = ΔH

2H2 + O2 2H2Olarge reduction in mole volumeentropy decreases in reactantsmade up by heat transfer to surroundingsΔG < ΔH

Carbon makes a better fuel cell

PCO2CO2 O2-

CO32- CO3

2-CO32- CO3

2-

O2- O2- O2- CO2

Phase I: Solid Oxide

Phase II: Molten Carbonate

Multi-Phase Equilibrium

Proposed Membrane

CO2CO2CO2

CO2

CO2

CO2CO2

CO2

CO2

CO2CO2

CO2

CO2

CO2 + O2- = CO32-

CO2 extraction from air

Permanent & safe

disposal


sources


Air Capture: A Different Paradigm

• Leave existing infrastructure intact

• Retain quality transportation fuels

• Eliminate shipping of CO2

• Open remote sites for CO2 disposal

• Enable fuel recycling with low cost electricity

Separate Sources from Sinks

Relative size of a tank

Electrical, mechanical storage

Batteries etc.

hydrogen

gasoline

Challenge: CO2 in air is dilute

• Energetics limits options– Work done on air must be small

• compared to heat content of carbon• 10,000 J/m3 of air

• No heating, no compression, no cooling• Low velocity 10m/s (60 J/m3)

Solution: Sorbents remove CO2from air flow

CO2

1 m3of Air40 moles of gas, 1.16 kg

wind speed 6 m/s

0.015 moles of CO2

produced by 10,000 J of gasoline

2

20 J2

mv=

Volumes are drawn to scale

CO2 Capture from Air

Air Flow

Ca(OH)2 solution

CO2 diffusion

CO2 mass transfer is limited by diffusion in air boundary layer

Ca(OH)2 as an absorbent

CaCO3 precipitate

Wind area that carries 22 tons of CO2 per year

Wind area that carries 10 kW

0.2 m 2

for CO2 80 m 2

for Wind Energy

How much wind?(6m/sec)

50 cents/ton of CO2 for contacting

A First Attempt

Air contactor:2Na(OH) + CO2 → Na2 CO3

Calciner:CaCO3→CaO+CO2

Ion exchanger:Na2CO3 + Ca(OH)2 →2Na(OH) + CaCO3

ProcessReactions

Capture Device

Trona Process

Limestone Precipitate

Dryer

Fluidized Bed

Hydroxylation Reactor

Membrane Device

(1)

(2)(3)(6)

(5)

(4)

Membrane

(1) 2NaOH + CO2 → Na2CO3 + H2O ΔHo = - 171.8 kJ/mol(2) Na2CO3 + Ca(OH)2 → 2NaOH + CaCO3 ΔHo = 57.1 kJ/mol

(3) CaCO3 → CaO + CO2 Δ Ho = 179.2 kJ/mol

(4) CaO + H2O → Ca(OH)2 Δ Ho = - 64.5 kJ/mol

(6) H2O (l) → H2O (g) Δ Ho = 41. kJ/mol

(5) CH4 + 2O2 → CO2 + 2H2O Δ Ho = -890.5 kJ/mol

Source: Frank Zeman

CO2

AirDepleted

Air

1/ρ

Unit Cost

Cost of Contacting the Air

1/ρ

Unit Cost

Cost of CO2 from Air

Sorbent Choices

-30

-25

-20

-15

-10

-5

0

100 1000 10000 100000

CO2 Partial Pressure (ppm)

Bin

ding

Ene

rgy

(kJ/

mol

e)

350K

300KAir Power plant

Cost of CO2 from Air(rescaled)

1/ρ

Unit Cost

Fixed Cost

60m by 50m

3kg of CO2 per second

90,000 tons per year

4,000 people or

15,000 cars

Would feed EOR for 800 barrels a day.

250,000 units for worldwide CO2 emissions

GRT’s Vision

The first of a kind

EnergySource

EnergyConsumer

H2O H2O

O2

O2

H2

Materially Closed Energy Cycles

EnergySource

EnergyConsumer

H2O H2O

O2

O2

CO2CO2

H2 CH2

Materially Closed Energy Cycles

C H

O

Fuels

Oxidizer

Combustion products

Biomass

CO

Fischer Tropsch Synthesis GasMethanol

EthanolNatural Gas

Town Gas

PetroleumCoal

GasolineBenzeneCarbon Hydrogen

CO2 H2O

Oxygen

Increasing Hydrogen Content

Incr

easi

ng O

xida

tion

Stat

e

Methane

Free

O2

Free

C-

H

Carbon Capture and Storagefor

Carbon Neutral World

• CCS simplifies Carbon Accounting– Ultimate Cap is Zero– Finite amount of carbon left

Private SectorCarbon Extraction

CarbonSequestration

Farming, Manufacturing, Service, etc.

Certified Carbon Accounting

certificates

certification

Public Institutionsand Government

Carbon Board

guidance

Permits & Credits

Klaus Lackner CEIC Seminar 1-16-08

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