22nd International Symposium on Plasma Chemistry July 5-10, 2015; Antwerp, Belgium Pulsed corona-induced CO 2 methanation W.F.L.M. Hoeben, E.J.M. van Heesch, F.J.C.M. Beckers, W. Boekhoven and A.J.M. Pemen Department of Electrical Engineering, Electrical Energy Systems group, Eindhoven University of Technology, Den Dolech 2, 5612 AZ Eindhoven, the Netherlands Abstract: CO 2 methanation has been observed by application of pulsed corona discharges in a CO 2 atmosphere over a deionized water film. At 46 kJ/L energy density, approximately 440 ppm CH 4 has been observed at a production efficiency near 398 pmol/J. Nickel-based corona wires seems to strongly promote the plasma-induced CO 2 methanation process. Keywords: CO 2 , methanation, non-thermal plasma, plasma catalysis, DSRD pulse source 1. Introduction Exclusively reserving fossil hydrocarbons for synthesis of life sustaining chemicals (e.g., pharmaceuticals, crop protection and food conservation agents, garments) prevents preliminary depletion of precious organic carbon sources through energy generation. An immense world reserve of inorganic carbon is stored in both the atmosphere as carbon dioxide and in oceans as carbonates. CO 2 back conversion thus is of great interest [1-3] but at the same time attractive only, if the required energy originates from sustainable energy sources. The direct conversion of carbon dioxide to methane has been studied using pulsed corona discharges in a carbon dioxide atmosphere over a deionized water film. CH 4 formation is assumed to proceed via the precursors CO and H 2 , produced from plasma-induced dissociation of CO 2 and H 2 O, respectively. Although experiments have been performed without direct use of catalytic materials, d-metal catalytic activity of the corona wires seems to play an important role in CO 2 methanation. 2. Experiments Under ambient conditions, nanosecond-risetime 65 kV high voltage pulses of 100 ns pulse duration from a driftstep-recovery-diode (DSRD) based pulse source [4] have been applied to a capacitive electrode configuration in a reactor with gas flow recycling, see Fig. 1. Typical voltage & current oscillograms are given in Fig. 2. The gas phase composition has been monitored using a gas chromatograph - flame ionization detector - mass spectrometer (Shimadzu QP2010p GC-FID-MS) and also a gas chromatograph with Thermal Conductivity Detector and MTN-assisted Flame Ionization Detector (Shimadzu GC2010p GC-TCD-MTN-FID). Experiments have been performed using both Nikrothal 80 and stainless corona wires. The GC-FID-MS with dedicated separation column is used to identify gas phase products, especially possibly complex organics. The GC-TCD-MTN-FID instrument focusses on simple permanent gases, with increased sensitivity for CO and CO 2 using the CO x -converting MTN unit in combination with the FID. P-II-8-10 Fig. 1. Pulsed corona reactor with gas infrastructure. Fig. 2. Typical voltage & current oscillograms recorded at energy density 46 kJ/L, with derived pulse energy. 1 3. Results Initial CO 2 methanation experiments have been performed using Nikrothal 80 corona wires. The GCFID-MS chromatograms represented by Fig. 3 indicate the formation of CH 4 as a function of the energy density, adjusted up to 46 kJ/L where about 440 ppm CH 4 has been detected. CH 4 production is confirmed by the mass spectrometer Total Ion Current chromatograms given by Fig. 4. The CH 4 production efficiency is approximately 3.98E-10 mol/J. Fig. 3. Top: GC-Total Ion Current chromatograms with peaks CO ~ 3.4 min, O 2 ~ 3.5 min, CH 4 ~ 3.6 min, CO 2 ~ 4.0 min, H 2 O ~ 12.5 min. Bottom: GC-Flame Ionization Detector chromatograms with CH 4 peak ~ 3.6 min. GC-FID-MS data as a function of the energy density. Fig. 4. GC-Total Ion Current chromatograms with m/z values recorded at 46 kJ/L. Arrows indicate CH 4 . Further evidence has been obtained with experiments using the same pulse source and reactor, the latter now equipped with stainless steel corona wires. Gas phase analysis has been performed using both diagnostic tools. Applied energy densities have been 90-359 kJ/L. The formation of O 2 , CO and H 2 is illustrated by the GC-TCD-MTN-FID chromatograms in Fig. 5. Again CH 4 has been detected, but levels have appeared to be sub-ppm now, while the applied energy density has been much higher than before. Observed CO 2 conversion levels are high i.e. up to 64%. CO 2 conversion efficiency values are approximately 90 - 143 eV/molecule. Fig. 5. Top: GC-Flame Ionization Detector chromatograms indicating the formation of CO ~ 4.8 min and CH 4 ~ 7.5 min and conversion of CO 2 ~ 9.6 min. Bottom: GC-Thermal Conductivity Detector chromatograms primarily indicating the formation of H 2 ~ 2.8 min, O 2 ~ 4.0 min, CO ~ 4.7 min and the conversion of CO 2 ~ 9.5 min. 4. Discussion It is remarkable that the plasma-induced CO 2 methanation using Nikrothal corona wires is much more effective than that achieved with stainless steel based wires. Nikrothal appears to be an austenitic nickelchromium alloy (19 - 21% Ni), where nickel as d-metal catalytic material exhibits specific methane yielding CO hydrogenation potential [5]. 2 P-II-8-10 Although proof of principle has been provided for plasma-driven CO 2 methanation, the observed energy efficiency of approximately 398 pmol/J is still poor. However, improvement seems feasible by application of a dedicated nickel-based catalyst, sub-nanosecond rise time pulsed corona discharges [6] and tuning of the plasma spatial & energy distribution [7]. Concluding, a topic of special interest is the release of CO 2 from its major source seawater [8]. Preliminary experiments prove the plasma-induced desorption of CO 2 from 200 g seawater (origin: North Sea). Fig. 6 shows GC-TCD-MTN-FID chromatograms of the gas phase after 0, 30 and 60 min of pulsed corona operation using the same settings as before. Prior to the tests, the reactor has been thoroughly flushed with synthetic air 4.8, being CO 2 free. Observed CO 2 quantities are about 529 ppm at maximum. In addition to CO 2 desorption, the formation of some CO has been observed due to plasma-induced dissociation of CO 2 . [3] [4] [5] [6] [7] [8] S. Mahammadunnisaa, E. Reddya, D. Raya, C. Subrahmanyama and J. Whitehead. Int. J. Greenh. Gas Con., 16, 361 (2013) A. Pemen, I. Grekhov, E. van Heesch, K. Yan, S. Nair and S. Korotkov. Rev. Sci. Instr., 74, 4361 (2003) I. Chorkendorff and J.W. Niemantsverdriet. Concepts of Modern Catalysis and Kinetics. (Weinheim: Wiley-VCH Verlag) ISBN 3-52730574-2 (2003) T. Huiskamp, E.J.M. Van Heesch and A. Pemen. IEEE Trans. Plasma Sci., 43, 1 (2015) E. Heesch, K. Yan, A. Pemen, G. Winands, F. Beckers and W. Hoeben. Int. J. Plasma Environ. Sci. Technol., 6, 87 (2012) H.D. Willauer, F. DiMascio, D.R Hardy and F.W. Williams. Ind. Eng. Chem. Res., 53, 12192 (2014) Fig. 6. GC chromatograms of the gas phase over plasma exposed seawater, as a function of the exposure time. Top: GC-Flame Ionization Detector chromatograms indicating CO ~ 4.9 min and CO 2 ~ 10.2 min. Bottom: GC-Thermal Conductivity chromatograms indicating O 2 ~ 3.7 min, N 2 ~ 3.8 min, CO 2 ~ 10.1 min. 5. References [1] W. Wang, S. Wang, X. Ma and J. Gong. Chem. Soc. Rev., 40, 3703-3727 (2011) [2] E. Jwa, H. Lee, S.B. Lee, M.Y.S. Fuel Proc. Technol., 108, 8993 (2013) P-II-8-10 3
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