Title: CO2 Capture Challenges and Opportunities
1CO2 Capture Challenges and Opportunities
Department of Chemical and Biomolecular
Engineering University of Notre Dame Notre Dame,
IN 46556
2U. S. Energy Consumption - 2003
Source EIA Renewable Energy Trends with
Preliminary Data for 2003, Figure 1, The Role of
Renewable Energy Consumption in the Nation's
Energy Supply, 2003.
3Role of Fossil Fuels
- Fossil fuels gt 85 of primary energy consumption
- Coal gt 50 of electricity
- Vigorous growth in renewables (wind, solar,
cellulosic biomass) will require many decades
before making significant contribution top
primary needs - U.S. (and Indiana 57 billion tons) have
abundant reserves of coal - Will continue to use fossil fuels
- Need to use them responsibly (SO2, NOx,
particulate, and CO2)
Indiana Geological Survey
4Post-Combustion CaptureConventional PC Power
Plant
Atmospheric pressure 12 CO2
http//www.bellona.org/factsheets/1191913555.13
5Pre-Combustion CaptureIGCC
gt20 atmospheres gt30 CO2
http//www.bellona.org/factsheets/1191913555.13
6US Dept. of Energy CCS Targets
- Separation and Capture
- Sequestration/Storage
- Monitoring, Mitigation and Verification
Sean Plasynski NETL, 6/5/07
7US Dept. of Energy CCS Program
Sean Plasynski NETL, 6/5/07
8Adequate CO2 Storage Capacity
6 GT/yr total US emissions
Sean Plasynski NETL, 6/5/07
9Motivation
- Designing Ionic Liquids for specific and
selective gas separations particularly CO2
capture - ILs as absorbent for separation of flue gas
- CO2, N2, O2, H2O, NOx, SOx, etc.
- Replace volatile and/or corrosive solvents
currently used for acid gas capture - Better understand the structure relationships for
gas solubility in ILs
Brennecke and Maginn, US Patent 6579343, 2003
10Typical Ionic Liquids
X Cl NO3 CH3CO2 CF3CO2 BF4 CF3SO3 PF6
(CF3SO2)2N
1-n-butyl-3-methylimidazolium tetrafluoroborate
bmimBF4 Not all ILs created equal
(viscosity, Tm, toxicity, PF6 and BF4 anion
degradation)
11Ionic Liquids and GHG Management
- Exploit unique properties of ILs
- Very low volatility
- High thermal stability
- Properties can be varied by choice of anion,
cation and substituents - Application areas
- Post-combustion CO2 capture
- Pre-combustion CO2 capture
- Other (e.g., air separation for IGCC and oxyfuel)
- Other possible separations
12Typical Post-Combustion Absorption System
13.8 MPa (2000 psia)
Conventional Absorber/Stripper
Trimeric
13Key Properties for CO2 Capture
- High CO2 solubility
- High CO2 selectivity
- Ease of regeneration
- Low enthalpy of solution
- Low solubility with water
- Low heat capacity
- Stability
- Thermal
- Other gases (e.g., SO2)
- Low viscosity
- Inexpensive
14Research Equipment
- Vapor-Liquid Equilibrium
- IGA
- Low pressure (0-20 bar)
- Small sample (75 mg)
- Rubotherm
- High pressure/high temperature
- Larger sample (1.5 g)
Intelligent Gravimetric Analyzer (IGA) -Hiden
Analytical, Inc.
Rubotherm
15Pure Gas Solubility - CO2
- Gas solubility
- Important for reusability of ILs
- Absorb at low T
- Remove at high T
- Trend seen for CO2 solubility in all ILs measured
Muldoon, et al., JPC B, 2007, 111, 9001-9009
16Pure Gas Solubility Other gases
- Gas solubility measured in hmpyTf2N
- Similar trends are seen with other ILs
- CO2 has the highest solubility of the gases
measured - Good selectivity!
Anderson, et al., ACR, 2007, 40, 1208-1216
17Comparison to Other Physical Solvents
Anderson, et al., ACR, 2007, 40, 1208-1216
18Pure Gas Solubility CO2
Muldoon, et al., JPC B, 2007, 111, 9001-9009
19Pure Gas Solubility CO2
Muldoon, et al., JPC B, 2007, 111, 9001-9009
20Pure Gas Solubility CO2
- Increasing fluorination increases CO2 solubility
- Anion effect greater than cation effect
Muldoon, et al., JPC B, 2007, 111, 9001-9009
21Pure Gas Solubility SO2
- SO2 solubility in hmimTf2N
- Same as for CO2
Anderson, et al., J Phys Chem B, 110 (31) 2006
22SO2 Pure Gas Solubility
- SO2 has highest solubility in ILs measured
- Possibility of simultaneous removal of both SO2
and CO2
Anderson, et al., J Phys Chem B, 110 (31) 2006
23Increasing CO2 Solubility
- Preliminary systems analysis indicated needed at
least 10x higher CO2 solubility - Best physical absorbent is p5mimbFAP with
H20 bar at 25 ºC - Chemical complexation
- Strong enough to increase capacity
- Weak enough to keep regeneration costs low
24Chemical Complexation - Literature
- Chemical capture of CO2 by free amine
- Stoichiometric capture of CO2
- 13C NMR evidence of carbamate formation
- Reversible under vacuum with heating
Bates, E. D. Mayton, R. D. Ntai, I. Davis, J.
H., J. Am. Chem., 2002, 124, 926.
25Chemically Complexing ILs
- Chemical complexation
- High CO2 solubility
26Tuning Complexation Strength
Ionic Liquid Pressure Capacity (bar) (mol
CO2/mol IL) NDIL0017 1.6 0.19 EMD0004 0.5
0.70 NDIL0039 1.6 0.06
Room temperature
27Summary
- ILs are excellent media for performing gas
separations (low volatility, tunable selectivity) - Capacity of physical solvents too low for
post-combustion capture but can enhance capacity
by chemical complexation with attractive heats - Important issues
- Reaction rates
- Viscosity changes
- Water content
- Process configuration and operation
28Project Team
- Notre Dame
- Prof. Ed Maginn
- Prof. Bill Schneider
- Prof. Juan de la Fuenta
- Dr. JaNeille Dixon
- Dr. Erica Price
- Dr. Zulema Lopez-Castillo
- Dr. Wei Shi
- Dr. Keith Gutowski
- Dr. Jindal Shah
- Jes Anderson
- Elaine Mindrup
- Burcu Gurkan
- Devan Kestal
- Industrial Partners
- DTE Energy
- Babcock and Wilcox
- EMD Chemicals/Merck KAaG
- Trimeric
- Air Products
29Acknowledgements
- U.S. Department of Energy, National Energy
Technology Laboratory, Award Nos.
DE-FC26-04NT42122 and DE-FC26-07NT43091 - State of Indiana 21st Century Fund