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Artificial Photosynthesis:
The Future Of Renewable Fuels And Chemicals




 Rich Masel1, Brian Rosen2, Amin Salehi-Khojin1, Wei Zhu2
                   1Dioxide   Materials    2UIUC




                                     This work was supported by Dioxide Materials and the U.S. Department of
                                     Energy under grant DE-SC0004453. Any opinions, findings, and conclusions
                                     or recommendations expressed in this manuscript are those of the authors
                                     and do not necessarily reflect the views of the Department Of Energy.
About Dioxide Materials
• Independent R&D company founded July 2009
• Focus: Nanotechnology to solve big problems
  (e.g. global warming)
• Patents pending – CO2 remediation, energy
  conservation, indoor air quality control
• Presently one Fortune 500 licensee
Today’s Agenda
CO2 Remediation via Artificial Photosynthesis
• Introduction of artificial photosynthesis
   – Why it is the future of renewable fuels and chemicals
• Description of three different processes
       • Photochemical water splitting
       • Hydrogen electrolysis
       • CO2 electrolysis
   – Why CO2 electrolysis is preferred
• Discussion about Dioxide Material’s recent advances in
  CO2 electrolysis
Artificial Photosynthesis: An Alternate
Route to Renewable Fuels and Chemicals
Biofuels Versus Artificial Photosynthesis


Biofuels

• Use photosynthesis to convert
  CO2 plus water and sunlight
  into biomass
• Use chemical or biological
  processes to convert biomass
  into fuels
Biofuels Versus Artificial Photosynthesis


Artificial Photosynthesis

• Converts sunlight and wind
  into electricity
• Uses electricity and chemical
  processes to convert CO2
  and water into fuels
Process Comparison
Biofuels                            Artificial Photosynthesis
•   Technology works today          •   Technology works today
•   Economically feasible           •   No competition with food supply
     – Tax subsidy                  •   Potential for high energy efficiency

               But
                                                      But
•   Competes with food supply
•   Energy inefficient              •   Not economically feasible today
     – Corn only 1% efficient in    •   Energy efficiency unproven
       converting sunlight into
       biomass – 0.04% to kernels
Potential Energy Efficiencies
                                                    Artificial
  Efficiencies             Biofuels
                                                 Photosynthesis
                           0.2-2%                    10-35%
Solar collection
                    (corn 1% to cellulose)         (solar cells)
                    25-75% of energy used           Electricity loses
                     in planting, fertilizing,   5%of energy during
 Transportation
                         harvesting, and         transmission across
                       transporting crops               country

Present process               5%                        <1%
Potential process             36%                       36%
Potential overall          0.3%                         8%
Artificial Photosynthesis is the Future of
       Renewable Fuels and Chemicals

             There is no other choice
• At maximum efficiency (converting cellulose)
  biotechnology would need 3,000,000 km2 of arable land
  to meet U.S. fuels and chemicals needs
   – Not enough unused arable land in U.S. to meet needs
• Solar collectors need 200,000 km2
   – Desert land & offshore wind sufficient
• Technology exists to produce hydrocarbons
There are Three Types of Artificial
   Photosynthesis Processes
Artificial Photosynthesis Processes
• Photochemical water splitting
      3H2O +h →3H2 + 1.5 O2
      3H2 + CO2→ (CH2)x

• Water electrolysis
      3H2O →3H2 + 1.5 O2
      3H2 + CO2→ (CH2)x +2H2O


• CO2 electrolysis
      2CO2→2CO + O2
      2CO + H2O → (CH2)x + CO2
Photochemical Water Splitting
      May Never Be Practical
                    • At 10% energy
2H2O +h →2H2 + O2
                      efficiency, 100,000 bbl/day
                      plant covers 670 km2
                       – About the size of NYC
                    • 3,000 mi of glass pipe
                       – containing a stoichiometric
                         mixture of H2 and O2


                        Explosion Hazard?
Electrolysis is a Better Alternative
   4-6 GW        Electrolyzer
                5-10x chlor-alkalai




95% efficient
                                      100,000 bbl/
                                       day of fuel
Simplest Process:
 Hydrogen Electrolysis + Fischer Tropsch
  Electrolyzer
3H2O → 3H2 + 1.5 O2    Reverse water gas shift:
                        H2 + CO2→ H2O + CO
                           Fischer Tropsch
                      2H2 + CO → H2O + (CH2)X
Hydrogen Electrolysis Process Economics

Assumption                                                                  $5.00
  • Wind-generated electricity                                              $4.50




                                                Hydrogen Cost, $/gal fuel
  • Net hydrogen cost of                                                    $4.00
    $4.03/kg today, dropping                                                $3.50
    to $2.33/kg in 2030+                                                    $3.00
                                                                            $2.50
                                                                            $2.00
                                                                                    2010   2020   2030


           +NERL  Report: J. Levene, B. Kroposki, and G. Sverdrup Wind Energy and
        Production of Hydrogen and Electricity — Opportunities for Renewable Hydrogen
CO2 Electrolysis is Potentially
          More Energy Efficient
  Electrolyzer
2CO2→ 2CO + 1.5 O2           Water gas shift:
                       2H2O + 2CO → 2H2 + 2CO2
                             Fischer Tropsch
                        2H2 + CO → H2O + (CH2)X

                          Combined chemistry:
                       H2O + 2CO → (CH2)X + CO2
How CO2 Electrolysis Works

   Acidic conditions               Alkaline conditions

       CO2 + e- → (CO2)-
 (CO2)- + 2H+ + e- → CO + H2O   CO2 + 2e- + H2O → CO + 2 OH-
            cathode                        cathode
           electrolyte                    electrolyte
             anode                          anode

       CO2 + e- → (CO2)-           4 OH- → O2 + H2O + 4e-
(CO2-) + H2O + e- → CO + 2OH-
Ideal Thermodynamic Comparison
                     1000
                                                                        30% electricity
                     800                                                waste
Energy Kj/mole CH2




                     600

                     400
                                Electrolysis      Water gas shift

                     200
                             water electrolysis    CO₂ Combined cycle
                       0
                                    Reaction Progress
(Title TBD by R. Masel)
                     2000
                                                 Water
                                                 gas shift
                     1500
Energy Kj/mole CH2




                                                                   Waste 70% of
                                                                   electricity
                     1000   Electrolysis


                     500

                                    CO₂ Combined cycle
                                     Ideal                   Actual Combined
                                                              Actual
                       0
                                           Reaction Progress
                                           Reaction Progress
CO2 Electrolysis Also Results in Issue
       Cathode Overpotential
                    -1.8
                    -1.6
                    -1.4
                    -1.2       Actual
   Voltage vs SHE




                      -1
                    -0.8                                            Wasted
                    -0.6
                                                                    energy
                    -0.4
                                       Equilibrium
                    -0.2
                       0   Pb Cd Tl Bi In Zn Hg Sn Cu Ag Ga Pd Au
                     0.2
High Energy in (CO2)- Intermediate
 Production Causes Overpotential
                    1.2

                      1
                            (CO2)-
      Free Energy   0.8

                    0.6

                    0.4

                    0.2

                      0

                    -0.2


                           Reaction Progress
Dioxide Material’s Patent Pending
Approach to CO2 Electrolysis Solves
    the Overpotential Problem
Dioxide Material’s Approach
Using two catalysts…       …results in lower
• Ionic liquid or amine    net energy loss.
  to catalyze formation                 1.2

  of (CO2)-                               1    (CO2)-
• Transition metal to




                          Free Energy
                                        0.8

  catalyze the                          0.6

  conversion of (CO2)-                  0.4
  to products
                                        0.2

                                          0         EMIM-(CO2)-
                                        -0.2
                                                 Reaction Progress
SFG To Verify (CO2)- Formation
                                  at Low Overpotentials
                                                           Emim-(CO2)-
                                                 -1.24 V
                                                 vs. SHE

                                                 -1.04
SFG intensity (arb. u.)




                                                               Brian A. Rosen, Amin Salehi-
                                                 -0.84
                                                               Khojin, PrabuddhaMukherjee, BjörnBraunschweig, Joh
                                                 -0.64
                                                               n L. Haan, W. Zhu, Dana D. Dlott, Richard I.
                                                               Masel, science under review
                                                 -0.44


                                                 -0.24         See Paper 295B
                                                 +0.04
                                                               12:55 Room 150F
                                                 +0.24

                          2200 2300 2400 2500
                                            -1
                          wavenumber / cm
CO Formation Also Observed
                             at Very Low Potentials
                                                 -0.55 V
                                                 vs. SHE
SFG intensity (arb. u.)




                                                 -0.45 V
                                                           Brian A. Rosen, Amin Salehi-
                                                           Khojin, PrabuddhaMukherjee, BjörnBraunsch
                                                           weig, John L. Haan, W. Zhu, Dana D. Dlott,
                                                 -0.35 V   Richard I. Masel, science under review



                                                 -0.25 V



               1800         2000   2200     2400
                                            -1
                          wavenumber / cm
Steady CO Production Observed at 110 C
                                                  GC Analysis
         PCO₂ = 1 Atm
         CO2 + 2e- + H2O → CO + 2 OH-
                      Pt cathode
           Electrolyte with 100 mMol water
                       Pt anode
            4 OH- → O2 + H2O + 4e-


              Observe CO product with GC
          Turnover rate = xx/sec at 0.6 V (SHE)
          Ran for yy hours with no degradation
Dioxide Material’s Technology
     Suppresses H2 Formation


CO2 + 2H+ + 2e- → CO + H2O
      2H+ + 2e- → H2
         cathode
                             Paper 182E
        electrolyte          Monday, 4pm
          anode              Room 151F
  2H2O → O2 + 4H+ + 4e-
The Future of Dioxide Material’s
            Patent Pending Process
• CO2 electrolysis demonstrated at low overpotential
   – Requires two catalysts
• Lifetime studies needed
• Need cell designs to suppress crossover
   – (CO2)- concentration high – can cross over to anode
Electrolysis Technology
              Development Still Needed
• Better cell design to raise efficiency from 70% to 83%
• Manufacturing expertise to lower capital cost of
  electrolyzer from $740/kW to $300/kW
• Government investment
   – U.S.D.O.E. spends $500m/yr. on biotech, $50m/yr. on solar
     water splitting, but has no specific program for electrolyzers.
     (Dioxide Materials is funded through SBIR.)
Summary
• Artificial photosynthesis is the future of renewable fuels
  and chemicals
   – Only alternative that can produce enough renewable
     hydrocarbons to meet the U.S. needs
• Two routes make sense
   – Hydrogen electrolysis + reverse water-gas shift
   – CO2 electrolysis
• Dioxide Materials has made a breakthrough in CO2
  electrolysis
The People Who Did The Work
                 CO2 Catalysis, Electrochemistry




            Brian Rosen   Amin Salehi-Khojin   Wei Zhu

                             CO2 SFG




John Haan   PrabuddhaMukherjee      BjörnBraunschweig    Prof Dana Dlott
Questions
NYC Sized Solar Collector Is Needed

      Assume 100,000 barrels/day -1% of US demand
        5 kw-hr/m2/day solar flux, 5% efficiency solar to gasoline


  5                9             2
10 bbl 6 10 J                  m day
 day         bbl           (5%)(5kw     hr)
                       2
 kw     hr     km                       2
         6         6       2
                               670 km
3.6    10 J 10 m
                                                   770 km2 of land
Also Need to Examine Selectivity

      CO2 + 2H+ + 2e- → CO + H2O
            2H+ + 2e- → H2
                cathode
               electrolyte
                 anode

        2H2O → O2 + 4H+ + 4e-

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Diox001 art pho

  • 1. Artificial Photosynthesis: The Future Of Renewable Fuels And Chemicals Rich Masel1, Brian Rosen2, Amin Salehi-Khojin1, Wei Zhu2 1Dioxide Materials 2UIUC This work was supported by Dioxide Materials and the U.S. Department of Energy under grant DE-SC0004453. Any opinions, findings, and conclusions or recommendations expressed in this manuscript are those of the authors and do not necessarily reflect the views of the Department Of Energy.
  • 2. About Dioxide Materials • Independent R&D company founded July 2009 • Focus: Nanotechnology to solve big problems (e.g. global warming) • Patents pending – CO2 remediation, energy conservation, indoor air quality control • Presently one Fortune 500 licensee
  • 3. Today’s Agenda CO2 Remediation via Artificial Photosynthesis • Introduction of artificial photosynthesis – Why it is the future of renewable fuels and chemicals • Description of three different processes • Photochemical water splitting • Hydrogen electrolysis • CO2 electrolysis – Why CO2 electrolysis is preferred • Discussion about Dioxide Material’s recent advances in CO2 electrolysis
  • 4. Artificial Photosynthesis: An Alternate Route to Renewable Fuels and Chemicals
  • 5. Biofuels Versus Artificial Photosynthesis Biofuels • Use photosynthesis to convert CO2 plus water and sunlight into biomass • Use chemical or biological processes to convert biomass into fuels
  • 6. Biofuels Versus Artificial Photosynthesis Artificial Photosynthesis • Converts sunlight and wind into electricity • Uses electricity and chemical processes to convert CO2 and water into fuels
  • 7. Process Comparison Biofuels Artificial Photosynthesis • Technology works today • Technology works today • Economically feasible • No competition with food supply – Tax subsidy • Potential for high energy efficiency But But • Competes with food supply • Energy inefficient • Not economically feasible today – Corn only 1% efficient in • Energy efficiency unproven converting sunlight into biomass – 0.04% to kernels
  • 8. Potential Energy Efficiencies Artificial Efficiencies Biofuels Photosynthesis 0.2-2% 10-35% Solar collection (corn 1% to cellulose) (solar cells) 25-75% of energy used Electricity loses in planting, fertilizing, 5%of energy during Transportation harvesting, and transmission across transporting crops country Present process 5% <1% Potential process 36% 36% Potential overall 0.3% 8%
  • 9. Artificial Photosynthesis is the Future of Renewable Fuels and Chemicals There is no other choice • At maximum efficiency (converting cellulose) biotechnology would need 3,000,000 km2 of arable land to meet U.S. fuels and chemicals needs – Not enough unused arable land in U.S. to meet needs • Solar collectors need 200,000 km2 – Desert land & offshore wind sufficient • Technology exists to produce hydrocarbons
  • 10. There are Three Types of Artificial Photosynthesis Processes
  • 11. Artificial Photosynthesis Processes • Photochemical water splitting 3H2O +h →3H2 + 1.5 O2 3H2 + CO2→ (CH2)x • Water electrolysis 3H2O →3H2 + 1.5 O2 3H2 + CO2→ (CH2)x +2H2O • CO2 electrolysis 2CO2→2CO + O2 2CO + H2O → (CH2)x + CO2
  • 12. Photochemical Water Splitting May Never Be Practical • At 10% energy 2H2O +h →2H2 + O2 efficiency, 100,000 bbl/day plant covers 670 km2 – About the size of NYC • 3,000 mi of glass pipe – containing a stoichiometric mixture of H2 and O2 Explosion Hazard?
  • 13. Electrolysis is a Better Alternative 4-6 GW Electrolyzer 5-10x chlor-alkalai 95% efficient 100,000 bbl/ day of fuel
  • 14. Simplest Process: Hydrogen Electrolysis + Fischer Tropsch Electrolyzer 3H2O → 3H2 + 1.5 O2 Reverse water gas shift: H2 + CO2→ H2O + CO Fischer Tropsch 2H2 + CO → H2O + (CH2)X
  • 15. Hydrogen Electrolysis Process Economics Assumption $5.00 • Wind-generated electricity $4.50 Hydrogen Cost, $/gal fuel • Net hydrogen cost of $4.00 $4.03/kg today, dropping $3.50 to $2.33/kg in 2030+ $3.00 $2.50 $2.00 2010 2020 2030 +NERL Report: J. Levene, B. Kroposki, and G. Sverdrup Wind Energy and Production of Hydrogen and Electricity — Opportunities for Renewable Hydrogen
  • 16. CO2 Electrolysis is Potentially More Energy Efficient Electrolyzer 2CO2→ 2CO + 1.5 O2 Water gas shift: 2H2O + 2CO → 2H2 + 2CO2 Fischer Tropsch 2H2 + CO → H2O + (CH2)X Combined chemistry: H2O + 2CO → (CH2)X + CO2
  • 17. How CO2 Electrolysis Works Acidic conditions Alkaline conditions CO2 + e- → (CO2)- (CO2)- + 2H+ + e- → CO + H2O CO2 + 2e- + H2O → CO + 2 OH- cathode cathode electrolyte electrolyte anode anode CO2 + e- → (CO2)- 4 OH- → O2 + H2O + 4e- (CO2-) + H2O + e- → CO + 2OH-
  • 18. Ideal Thermodynamic Comparison 1000 30% electricity 800 waste Energy Kj/mole CH2 600 400 Electrolysis Water gas shift 200 water electrolysis CO₂ Combined cycle 0 Reaction Progress
  • 19. (Title TBD by R. Masel) 2000 Water gas shift 1500 Energy Kj/mole CH2 Waste 70% of electricity 1000 Electrolysis 500 CO₂ Combined cycle Ideal Actual Combined Actual 0 Reaction Progress Reaction Progress
  • 20. CO2 Electrolysis Also Results in Issue Cathode Overpotential -1.8 -1.6 -1.4 -1.2 Actual Voltage vs SHE -1 -0.8 Wasted -0.6 energy -0.4 Equilibrium -0.2 0 Pb Cd Tl Bi In Zn Hg Sn Cu Ag Ga Pd Au 0.2
  • 21. High Energy in (CO2)- Intermediate Production Causes Overpotential 1.2 1 (CO2)- Free Energy 0.8 0.6 0.4 0.2 0 -0.2 Reaction Progress
  • 22. Dioxide Material’s Patent Pending Approach to CO2 Electrolysis Solves the Overpotential Problem
  • 23. Dioxide Material’s Approach Using two catalysts… …results in lower • Ionic liquid or amine net energy loss. to catalyze formation 1.2 of (CO2)- 1 (CO2)- • Transition metal to Free Energy 0.8 catalyze the 0.6 conversion of (CO2)- 0.4 to products 0.2 0 EMIM-(CO2)- -0.2 Reaction Progress
  • 24. SFG To Verify (CO2)- Formation at Low Overpotentials Emim-(CO2)- -1.24 V vs. SHE -1.04 SFG intensity (arb. u.) Brian A. Rosen, Amin Salehi- -0.84 Khojin, PrabuddhaMukherjee, BjörnBraunschweig, Joh -0.64 n L. Haan, W. Zhu, Dana D. Dlott, Richard I. Masel, science under review -0.44 -0.24 See Paper 295B +0.04 12:55 Room 150F +0.24 2200 2300 2400 2500 -1 wavenumber / cm
  • 25. CO Formation Also Observed at Very Low Potentials -0.55 V vs. SHE SFG intensity (arb. u.) -0.45 V Brian A. Rosen, Amin Salehi- Khojin, PrabuddhaMukherjee, BjörnBraunsch weig, John L. Haan, W. Zhu, Dana D. Dlott, -0.35 V Richard I. Masel, science under review -0.25 V 1800 2000 2200 2400 -1 wavenumber / cm
  • 26. Steady CO Production Observed at 110 C GC Analysis PCO₂ = 1 Atm CO2 + 2e- + H2O → CO + 2 OH- Pt cathode Electrolyte with 100 mMol water Pt anode 4 OH- → O2 + H2O + 4e- Observe CO product with GC Turnover rate = xx/sec at 0.6 V (SHE) Ran for yy hours with no degradation
  • 27. Dioxide Material’s Technology Suppresses H2 Formation CO2 + 2H+ + 2e- → CO + H2O 2H+ + 2e- → H2 cathode Paper 182E electrolyte Monday, 4pm anode Room 151F 2H2O → O2 + 4H+ + 4e-
  • 28. The Future of Dioxide Material’s Patent Pending Process • CO2 electrolysis demonstrated at low overpotential – Requires two catalysts • Lifetime studies needed • Need cell designs to suppress crossover – (CO2)- concentration high – can cross over to anode
  • 29. Electrolysis Technology Development Still Needed • Better cell design to raise efficiency from 70% to 83% • Manufacturing expertise to lower capital cost of electrolyzer from $740/kW to $300/kW • Government investment – U.S.D.O.E. spends $500m/yr. on biotech, $50m/yr. on solar water splitting, but has no specific program for electrolyzers. (Dioxide Materials is funded through SBIR.)
  • 30. Summary • Artificial photosynthesis is the future of renewable fuels and chemicals – Only alternative that can produce enough renewable hydrocarbons to meet the U.S. needs • Two routes make sense – Hydrogen electrolysis + reverse water-gas shift – CO2 electrolysis • Dioxide Materials has made a breakthrough in CO2 electrolysis
  • 31. The People Who Did The Work CO2 Catalysis, Electrochemistry Brian Rosen Amin Salehi-Khojin Wei Zhu CO2 SFG John Haan PrabuddhaMukherjee BjörnBraunschweig Prof Dana Dlott
  • 33. NYC Sized Solar Collector Is Needed Assume 100,000 barrels/day -1% of US demand 5 kw-hr/m2/day solar flux, 5% efficiency solar to gasoline 5 9 2 10 bbl 6 10 J m day day bbl (5%)(5kw hr) 2 kw hr km 2 6 6 2 670 km 3.6 10 J 10 m 770 km2 of land
  • 34. Also Need to Examine Selectivity CO2 + 2H+ + 2e- → CO + H2O 2H+ + 2e- → H2 cathode electrolyte anode 2H2O → O2 + 4H+ + 4e-