Transcript Document
High Rate - High Efficiency Water Electrolysis using 3D Isotropic nanoCatalysts coatings for clean energy solutions Robert Dopp DoppStein Enterprises / GridShift, Inc. Presentation to: U.S. Department of Energy Washington, DC 20585 October 14, 2010 GS 770 649 1933 [email protected] 1 Outline Introduction – Robert Dopp and Gridshift Introduction – On Demand & Stationary Power supply- Clean & sustainable energy systems. GridShift nanoCatalysts producing up to 80% energy efficient, cost-effective, full demo cells Bipolar electrolysis with nanoCatalyst -coated flat plates for Bipolar Systems - Rate <350 mA/cm2 Monopolar electrolysis using 3D nanoCatalyst electrodes for Monopolar Systems -Rates >=1 Amp/cm2 GridShift Alkaline Fuel Cell Projections GridShift Hydrogen Flow Cell Next Steps GS 770 649 1933 [email protected] 2 Introducing Robert Dopp Robert Dopp is well known in the Zinc Air and battery world with over 30 years experience. “Principle Engineer” at Rayovac Corp. on the Zinc Air project - 18 Years “Director of Research” at Electric Fuel of Biet Shemesh Israel - 6 years CEO DoppStein Enterprises (DSE) - 9 years CEO Gridshift Inc. (GS) - 2 years Proficiency includes Batteries, Fuel Cells and Hydrogen generation from water electrolysis. 39 Issued patents and 16 in the office in energy related fields Consults to Fuel Cell, Battery and Materials companies. Offers a depth of knowledge in battery systems with freedom & flexibility from his independent laboratory. Developed a very high rate and high efficiency electrolyzer. GS Developed the highest rate air cathode in the world. 770 649 1933 [email protected] 3 Introducing Gridshift (GS) Founded in December 2008 Funded by Khosla Ventures Development began in 2007 as an Electrochemical Fluidized Bed Reactor (FBR) for water electrolysis Physical challenges with an FBR, so GS developed a “Solid-State FBR” Project met milestones on time and under budget Vinod on Board of Directors and supportive GS 770 649 1933 [email protected] 4 Why H2 Production Systems? Benefits: (1) Small distributed electrolyzers (On demand, Automotive) (2) Stationary large-scale electrolyzers (3) Potential synergies with renewable energy power generating systems (wind, nuclear) (4) No greenhouse gas emissions (5) GS H2 Production Cost Challenges: (1) Auto - Safety (2) Auto- NOx increase output with increased Temp (3) DOE Cost goal $2.00-$3.00/gge GS 770 649 1933 [email protected] 5 GS NanoCatalysis Coatings Proprietary multiple nanoparticle recipe/method using complex pulse-shaped coating/plating operation designed by GS. Isotropic, distribution of ‘bezel-mounted nanocabochons’ with uniform 2D/3D surface coverage. Excellent electrical contract from the current collector to the nanoCatalyst. GS 770 649 1933 [email protected] 6 GS NanoCatalysis 3D Coating of Foam Electrodes Ni FOAM GS NanoCatalysts –coated FOAM Isotropic, fully functional 3D electrodes Enhanced current conduction for optimized electrolysis GS 770 649 1933 [email protected] 7 Two-Cell Electrolyzer Parts Au GS Isotropically GS nanoCatalyst 770 649 1933 coated electrodes [email protected] 8 Two-Cell Electrolyzer Assembled GS 770 649 1933 [email protected] 99 Half Cell - Voltammogram Voltammogram Curve 4.0 3.5 3.0 SS 316 Smooth Ni Anode or Oxygen Generating Reaction #119 Decacoat, Tri catalyst, Voltage vs. Zinc 2.5 2.0 1.5 Current Density is Proportional to Gas Output 1.0 0.5 0.0 -0.5 -1.0 Tri catalyst, Decacoat #121 Cathode or Hydrogen Generating Reaction -1.5 0.0001 0.001 0.01 0.1 1 10 Current, Amps/cm^2 GS 770 649 1933 [email protected] 10 Flat-Plates Cell Voltage - FULL CELL Full Cell Voltage of Bifunctional Plates 4.0 SS316 3.5 GridShift 3D Electrode 3.0 Cell Voltage GS 3D nanoCatalyst •High-Rate •Low Power •High Efficiency Best Reported at NHA 2.5 •Used for on Demand Electrolysis •Or large stationary Electrolysis 2.0 1.5 1.0 Lower Full-Cell voltage is desired 0.5 0.0 0.0 GS 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1.0 Current Density, A/cm2 770 649 1933 [email protected] 11 Energy Efficiency - Bipolar Electrolysis Energy Efficiency of Bifunctional Flat Plates 120% Higher Energy Efficiency is desired 100% Energy Efficiency 80% 60% 40% GridShift 3D Electrode Best Reported at NHA 20% SS316 0% 0.0 GS 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1.0 Current Density, A/cm2 770 649 1933 [email protected] 12 H2 Output for Flat Plates- GS High-Rate H2 Output Assuming 14 V, 225 cm2 for On 3.00 Gridshift 3D Any electrolyzer can reach high efficiency. The rate at which the number is reach is the key. 2.50 Gridshift produces more hydrogen for any Efficiency 2.75 GE Best SS316 2.00 1.75 1.50 1.25 1.00 2 H Production, Liters/min 2.25 0.75 0.50 0.25 0.00 40% 45% 50% 55% 60% 65% 70% 75% 80% 85% 90% 95% 100% Energy Efficiency GS 770 649 1933 [email protected] 13 H2 Output for Flat Plates- GS High-Rate H2 Output Assuming 14 V, 225 cm2 for On 3.00 2.75 2.50 Any electrolyzer can run at low voltage. The rate at which the number is reached is the key. Gridshift produces more hydrogen at any voltage due to higher current at any voltage. Gridshift 3D GE Best H2 Production, Liters/min 2.25 SS316 2.00 1.75 1.50 1.25 1.00 0.75 0.50 0.25 0.00 1.5 1.7 1.9 2.1 2.3 2.5 2.7 2.9 3.1 3.3 3.5 Cell Voltage GS 770 649 1933 [email protected] 14 Half- Cell 3D Electrode Voltammogram Voltammogram Curve Half-Cell Data 4.0 Smooth Ni SS 316 3.5 Anode Reaction Oxygen Generation 3.0 Gridshift Triple nano Coating Gr aphite Voltage vs. Zinc 2.5 2.0 1.5 1.0 120% EE Ideal Ce ll Voltage gives Energy Efficiency = 1.482/V 85% EE Gridshift 3D Coated Electrode 0.5 0.0 -0.5 -1.0 Cathode Reaction Hydrogen Generation Gr aphite SS 316 Gridshift Triple nano Coating Smooth Ni -1.5 0.0001 0.001 0.01 0.1 1 10 Current, Amps/cm^2 GS 770 649 1933 [email protected] 15 Energy Efficiency vs.. Rate for GS 3D nanoCatalyst coated foams – FULL CELL Energy Efficiency in Full Cell Electrolyzer Energy Efficiency, % 100% Keyed to 1000 mA/cm2 90% GridShift 3D 70C 80% Raney Nickel 70C 70% Ni Foam 70C 60% 50% 40% Raney Nickel 30% 20% Want highest number at highest current density 10% 0% 0 GS 500 1000 1500 2000 2500 3000 3500 4000 Current Density, mA/cm^2 770 649 1933 [email protected] 16 Energy Efficiency vs.. Rate for GS 3D nanoCatalyst coated foams – FULL CELL Cell Voltage in Full Cell Electrolyzers 7 Keyed to 1000 mA/cm2 6 Ni Foam 70C Raney Nickel Raney Nickel 70C Full Cell Voltage 5 GridShift 3D 70C 4 3 2 Want the lowest voltage at the highest current 1 0 0 GS 500 1000 1500 2000 2500 3000 3500 4000 Current Density, mA/cm^2 770 649 1933 [email protected] 17 H2 Output for GS nanoCatalyst-coated 3D Foam Electrodes- FULL CELL H2 Output per kWh 0.7 0.6 0.5 kg H 2 per Hour 3D Foam Ni Blank GridShift nano-Coated 3D Electrodes 100 cm2 240 VAC (170 VDC) 7K 6K 5K 0.4 Rainey Nickel 4K 0.3 3K Liters H2 per Hour Conditions 70 Deg C 0.2 2K 0.1 1K 0.0 0 GS 20 40 60 80 100 120 140 160 180 200 kWh/kg Hydrogen 770 649 1933 [email protected] 18 Mass Balance (All current leading to electrolysis. No ionic shunting) GS 770 649 1933 [email protected] 19 1000 Hour Test Cell Voltages on 500 mA/cm2 at 90 oC 90% 80% Cell Energy Efficiency 70% 60% 50% 40% There is an initial degradation over the first 200 hours Then there is no further degradation and perhaps some recovery No significant sloughing was observed The cobalt solubility color was only observed in initial use of the electrodes, but not in this re-use of the electrodes 30% 20% 10% 0% 0 100 200 300 400 500 600 700 800 900 1000 Time, Hours GS 770 649 1933 [email protected] 20 Applications for Water Electrolyzers Charging stations in homes for hydrogen powers vehicles Hydrogen generators at filling stations for hydrogen vehicles Synfuel Production CO + H2 Hydrolyze light bio-fuels into more useful fuels Methane fuel production May be solar powered Cobalt and Iron catalyzed H2 + Cellulose --> Methane Ammonia via the Haber-Bosch method for fertilizers Iron oxide catalyzed 3H2 + N2 --> 2NH3 Combine with solar, wind or geothermal for many of above. Improved ICE efficiency Improved diffusivity, higher Octane #, can use higher compression, faster flame-front speed, increases lean limit, etc. GS 770 649 1933 [email protected] 21 High Rate Alkaline Fuel Cell- AFC Power of two Fuel Cell systems 800 700 GridShift Increased Power mW/cm2 Power, 600 500 400 Existing AFC Systems 300 PEM Systems 200 100 0 200 300 400 500 600 700 800 900 1000 Current Density, GS mA/cm 2 770 649 1933 [email protected] 22 Hydrogen Flow Cell Using the GS high rate Electrolyzer, H2 and O2 are produced during peak times: When the sun shines When the wind blows When power is cheap Using the new GS AFC, stored gasses produce electricity: When the sun does not shine When the wind is calm When power is expensive GS 770 649 1933 [email protected] 23 CONCLUSIONS Coating the interior surfaces of a complex shaped current collector with GS 3 D nanoCatalysts results in a very high rate - high efficiency electrolysis cell with a very low potential capital Cost. The GridShift 3D nanoCatalyst-coated full cell demonstrated up to 80% efficiency, is cost effective and reliably productive. Efficiency results may be optimized. Mass balance demonstrates data is accurate with no ionic shunting. Alkaline Fuel Cell is logical extension of work Hydrogen flow cell results when Fuel Cell is complete. GS 770 649 1933 [email protected] 24 Contact Information Robert Dopp & Sharon Stein GS Office: 770 649 1933 Bob’s (CEO) Mobile: Sharon’s (CFO) Mobile: 404 626 9008 [email protected] www.grid-shift.com Share folder: www.grid-shift.com/doe 770 649 1933 [email protected] 770 355 2213 25