Research and Technology Initiatives Plasma-Assisted Reforming and HydroDesulfurization of Diesel Fuels for Fuel Cells K. Becker1, P.J. Ricatto2, J. Hunt3, and H. Ghezel Ayagh3 1 Polytechnic Institute of New York University, Brooklyn, NY 11201 2 Stevens Institute of Technology, Hoboken, NJ 07030, USA 3 FuelCell Energy Inc., Danbury, CT 06813 USA Objectives: • Investigate feasibility of a low-T plasma to produce a feed gas for High-Temperature Fuel Cells that is rich in CH4and H2 from A model synthetic fuel (dodecane, C12H26) Diesel or a Diesel/Steam mixture • Investigate feasibility of a low-T Plasma to convert organic sulfur compounds in Diesel to H2S (which can be scrubbed) Work supported by the US Dept. of Energy and the US Navy and by FCE MOTIVATION: Research and Technology Initiatives The Navy’s Shipboard Fuel Cell Program SLOGAN: Electric Power Sources for the Navy and Marine Corps CHARGE: Develop new safe, efficient, environmentally friendly sources of power and power generation concepts that support portable, long-lived power sources for all future marine-carried equipment and electric power sources required for all-electric ships and other war-fighting platforms BENEFITS: (a) Cost savings – higher efficiency through reduced fuel consumption & lower maintenance through reduced shipboard load (b) Reduced emissions – reduced exhaust emissions & reduced acoustic and IR signature and radar cross section Comparison of Efficiencies Research and Technology Initiatives LHV (lower heating value) is the heat released by combusting a specified quantity of fuel at 25 C and returning the temperature of the products to 150 C. The latent heat of vaporization or water in the fuel and the reaction products is not recovered. Additional Benefits Research and Technology Initiatives • Ship design flexibility • Modular approach that is applicable to all ship power requirements • Applicable to multiple platforms • Facilitates all-electric ship with integrated power system and zonal power distribution system • Permits the use of alternate and synthetic fuels Challenges • Use of logistic fuels (JP-5, JP-7, NATO 76) High sulfur content (up to 10,000 ppm) • Materials & Impurities Catalyst degradation Tolerance to CO (PEM), sulfur, etc. Stack life degradation • Compact, lightweight, rugged – weight is an issue !!! Research and Technology Initiatives FCE is a World Leader in Fuel Cell Systems current product future technology FCE Direct Carbonate FC !!! Research and Technology Initiatives Fuel Cell Chemistry 2m FCE’s 300 kW Carbonate Direct Fuel Cell Research and Technology Initiatives FCE 625 kW Ship Service Molten Carbonate Fuel Cell System Research and Technology Initiatives Process AC Power Two Catalytic Reactors WEIGHT !!! Diesel Sulfur Removal PreReforming steam Power Conditioning Carbonate DFC/SOFC Heat/Water Recovery Exhaust Steam Generation air Low-T Plasma Alternative Diesel Plasma Reactor Vaporization water Diesel CH4,H2, HCs R-S + H2 H2S + R ZnO Cartridge ZnO + H2S ZnS + H2O Clean Fuel Cell Feed Research and Technology Initiatives Why a Low-Temperature Plasma • A Plasma is a collection of neutrals, ions, and electrons + more globally quasi-neutral, i.e. # of electrons = # of ions electromagnetic forces between the charge carriers are dominant The plasma components (electrons, ions, and neutrals) are characterized by energy distribution functions or alternatively by an “average” energy or temperature (Te, Ti, Tn) Low-Temperature Plasma: Te >> Ti, Tn with Ti ≈ Tn high electron temperature (10,000 – 100,000 K) low gas temperatures (300 – 1,500 K) “high-temperature chemistry” at low ambient temperatures (through electron-induced dissociation and ionization & through molecular vibrational non-equilibrium) !!! Plasmas are everywhere !!! Research and Technology Initiatives Sun Aurora Borealis (Northern Lights) Fluorescent Lamps Flame Lightning Plasma Display Televisions Dielectric Barrier Discharge Plasmas Research and Technology Initiatives Research and Technology Initiatives Plasma Reactor I SDM P REACTO R 1. Surface DBDs (S-DBDs) using Microrods IN High Voltage (~10-15 KHz) Dielectric Ground Wires P lasm a Copper W ire Plasma Reactor II 2. Parallel-Plate DBD (PP-DBD) Research and Technology Initiatives Top electrode removed Gas in Gas out 10” Results I: Preliminary Results (1) Low & High Sulfur Fuel @ Steam/Fuel = 3 Good Not bad Research and Technology Initiatives Low Sulfur High Sulfur 27 % (v/v) 23 30 5 1/0 14 28 23 29 2 2/0 16 Methane Hydrogen Ethene Acetylene Ethane/Propane Higher Hydrocarbons (2) Effect of Steam/Fuel Ratio for NATO 76 Diesel Good Not bad Methane Hydrogen Ethene Acetylene Ethene/Propane Higher Hydrocarbons LOW (2:1) 25 % (v/v) 21 28 4 2/1 MEDIUM (3:1) 27 23 30 5 1/0 HIGH (8:1) 25 21 33 4 1/0 19 14 16 Preliminary Results Look Promising, BUT: • obtained under very favorable circumstances • ignore other important parameters • not the basis for realistic implementation – but justified more research Research and Technology Initiatives Results II: (1) Effect of Fuel Flow on Dodecane Conversion Fuel Flow, g/m 0.8 0.4 % Conversion 3.4 % 7.0 % Results II: (2) Effect of Plasma Power on Dodecane Conversion Plasma Power, W % Conversion 100 300 3.4 % 4.2 % Concentration, mol % (dry basis) Concentration, mol % (dry basis) H2 17.6 14.2 CH4 1.0 1.2 CO 0.3 0.3 H2 17.6 9.1 CH4 1.0 2.0 CO 0.3 0.2 CO2 0.2 0.1 CO2 0.2 0.1 C2H6 0.7 0.7 C2H6 0.7 0.9 C3H8 1.2 1.6 C3H8 1.2 2.7 C4-C7 1.7 2.1 C4-C7 1.7 2.3 Results II: (3) Effectiveness of Hydrodesulfurization by Plasma Carrier Gas N2 Air Air Gas Flow, cc/m 250 200 200 Plasma Power, W 50 50 10 3.0 % 3.3 % 2.3 % 1.2 36.6 5.7 JP-5 Conversion, % Total S in Gas Stream, ppm O needed ! Research and Technology Initiatives Results II: (4) Plasma Reforming of JP-5 Reactor PP-DBD C-DBD Carrier gas Argon Air Nitrogen Gas flow (slpm) 0.25 0.25 0.25 Fuel Flow, g/m 0.5 0.5 0.8 1.6% 4.9% 3.0% Fuel Conversion, % Concentration, mol % (dry basis) H2 8.4 10.8 3.5 CH4 0.1 2.0 0.7 CO 0.6 4.6 0.1 CO2 0.3 0.7 0.0 C2H6 0.2 0.8 0.4 C3H8 0.3 1.5 1.8 C4-C7 0.8 1.5 1.9 SUMMARY OF FINDINGS Research and Technology Initiatives • Plasma-assisted partial oxidation of hydrocarbons in the presence of steam gives substantially better % conversion compared with straight steam reforming or straight partial oxidation. This suggests that while the primary conversion pathway is via partial oxidation, the steam plays an important role in the conversion. • While the % conversion and electrical efficiency (both <10%) are well below those required for immediate practical application, the composition of the CH4/H2-rich product gas is suitable for the anode feed of a SOFC. • Preliminary results show that the plasma assisted conversion of organic sulfur compounds to hydrogen sulfide is much greater than the hydrocarbon % conversion, suggesting that the plasma selectively enhances sulfur chemistry. May need 2 separate plasma reactors (cf. 2 catalytic reactors) Next Steps Research and Technology Initiatives • Conduct parametric studies to optimize each of the following: Power Deposition into the Plasma Reactor Temperature Fuel/air/steam ratio Fuel flow rate Carrier gas choice and flow rate • Further optimize the reactor design and material selection to maximize % conversion and reactor durability, and minimize thermal problems and carbon deposition. • Incorporate heterogeneous reforming catalysts (hybrid system). • Other types of plasmas (e-beam sustained, gliding arc).
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