Removal of tars using an external magnetic field assisted-plasma torch K. T. Kim1, D. G. Kim1, M. Hur1, S. A. Roh1, S. I. Keel1, K. Y. Kang1 and M. S. Cha2 1 Environmental and Energy Systems Research Division, Korea Institute of Machinery & Materials 104 Sinseong-Ro, Yuseong-Gu, Daejeon 305-343, Korea 2 Clean Combustion Research, Mechanical Engineering Program, King Abdullah University of Science and Technology, Jeddah, Saudi Arabia Abstract: The influence of external magnetic field on the discharge characteristics is investigated in a plasma torch designed for the removal of tars ejected from a gasification reactor. Toluene (C7H8) is used as a simulation gas for tars, and byproducts produced by passing plasmas are identified and quantified with a Fourier transform infrared (FTIR) spectroscopy. The external magnetic field allows for a more uniform plasma generation in space because of a faster rotation of arc column. As the power applied to the solenoid increases, the arc voltage is more fluctuated with time, and as a result the arc power is greatly raised up without increasing arc current. In addition, both the decomposition rate and energy efficiency for C7H8 are enhanced with the external magnetic field due to an increasing arc power and more uniform plasmas in space. Keywords: removal of tars, energy efficiency, plasma torch, external magnetic field 1. Introduction Syngas production from waste is very attractive in that useless and even hazardous materials are converted into valuable fuels. We have developed a waste gasification system, mainly consisting of an oxy-fuel burner and a plasma torch, which are used as a heat source for waste destruction and a reformer for tar removal, respectively. In gasification by an oxy-fuel burner, tars, caused by the non-uniform temperature distribution in the reactor, are byproducts which should be removed for high-purity syngas production. The tar removal is, however, known to be very difficult because tars produced from gasification process have generally very strong C-H bonds. To destroy tars and thus to produce high-purity syngas from waste, a plasma torch is placed downstream of the gasification reactor. Plasma torches have widely used as a heat or chemical source for melting, reforming and waste treatment because of their high temperatures, high energy densities, and abundant reactive species, which can’t be provided by any other devices. Disadvantage of plasma torches originates from the use of electricity, most expensive form of energy. In our system, an oxy-fuel burner is used as a main heating source, whereas a plasma torch is used as a reformer for tar removal. The combination of an oxy-fuel burner with a plasma torch allows for lessening a burden of operation cost of plasmas, and this method is useful especially in large-scale devices such as gasification process. This work aims to demonstrate the feasibility of a plasma torch for removing tars emitted from a gasification reactor, especially focused on the effects of external magnetic field. 2. Experimental Figure 1 shows a schematic of experimental setup. The plasma torch mainly consists of a conical cathode, cylindrical anode, and a swirl chamber. The cathode has a protruding part for an easier gas breakdown. The smallest gap between the cathode and the anode is 2 mm while the internal diameter of anode is 50 mm. The swirl chamber induces a swirl motion of discharge gas which contributes to the improvement of discharge stability and the reduction of electrode erosion. Table 1. Gas conditions used to simulate the gas compositions ejected from the gasification reactor. 3. Results and discussion Figure 1. A schematic of experimental system. To obtain more uniform plasmas in space and thereby to enhance the decomposition rate of tars, a solenoid is installed on the periphery on the anode. The solenoid (80 mm in length and 100 turns) induces the magnetic field in the axial direction, and then Lorentz force, proportional to the arc current and the magnetic field induced, acts in the azimuthal direction. As a result, the arc column rotates with a very high speed, expecting to improve plasma uniformity especially in the radial direction. Two DC power supplies are used for the plasma torch (10 kV - 1 A) and solenoid (4 V - 60 A). H2, CO, and CO2 are the main gases ejected from the gasification reactor, and small quantity of H2O and tars is mixed with them. By consulting the preliminary experiments, the gas conditions in Table 1 are selected to simulate the gas compositions ejected from the gasification reactor. Toluene (C7H8) is used as a simulation gas for tars, and the Fourier transform infrared (FTIR) spectroscopy is used for the evaluation of decomposition rate along with the identification and quantification of byproducts produced. Figure 2 shows the front discharge images taken by varying the power applied to the solenoid. Without the external magnetic field, plasmas have the region with very weak light intensities at some distance away from the center. The region with weak light intensities is surely to be inefficient to heat the tars. As the power applied to solenoid increases, the faster rotation of arc column is achieved in the radial direction. As a result, the weak intensity zone gradually disappears with the increase in power applied to the solenoid. Figure 2. Influence of external magnetic field on the discharge images. The power applied to the solenoid is varied from 0 to 95 W. The magnetic field induced by the solenoid greatly influences the waveform of arc voltage as plotted in Figure 3. The external magnetic field enables the arc voltage to fluctuate with time, which leads to the reduction of the period of low voltages. This results in the increase in the arc power under the same arc current. For example, when 60 W is applied to the solenoid, the arc power of 0.7 kW without the external magnetic field is increased by 100 % to 1.4 kW. This tendency would be advantageous to the plasma torch, because the electrode erosion is proportional to the arc current. Tars are changed into the liquid state at low temperatures and then hold together, and finally form sludge. This sludge is very harmful to the aftertreatment system. respectively, plotted as a function of specific energy density (SED) with and without the power applied to the solenoid. The influence of external magnetic field on the energy efficiency seems to be quite small. However, the decomposition rate for C7H8 is greatly enhanced with the use of external magnetic field. The external magnetic field allows for an increase in power and an improvement in plasma uniformity, which enable more destructions of C7H8 without increasing the current. 6000 Voltage [V] 4000 Gas flowrate: 90 L/min Discharge power: -Arc only: 0.7 kW -Magnetic: 1.4 kW Magnetic 2000 0 Arc only -2000 -30 -20 -10 0 10 20 30 Time [msec] Figure 3. Influence of external magnetic field on the arc voltage. The power applied to the solenoid is fixed at 60 W. Figure 4. FRIR spectra measured as a function of total gas flow rate at a fixed input power of 1.4 kW and solenoid power of 60 W. Figure 4 shows the typical spectra indicating the decomposition of Toluene (C7H8) which is used as a simulation gas for tars. It is seen that C7H8 is decomposed into lower hydrocarbons such as CH4 and C2H2, which remain the gaseous state even at low temperatures. As the total gas flow rate increases, the decomposition rate for C7H8 decreases. This means that a higher arc power is required to destruct an increasing quantity of C7H8, and this tendency is well consistent with the previous results done in similar conditions. The influences of external magnetic field on the decomposition of C7H8 are investigated based on the spectra measured with the FTIR spectroscopy. Figures 5 and 6 show the decomposition rate and decomposition energy efficiency for C7H8, C7H8 decomposition rate [%] 80 Arc only Magnetic 60 40 Gas flowrate: 70~110 L/min Discharge power: -Arc only: 0.7 kW -Magnetic: 1.4 kW 70(L/min) 90 110 20 90 0 0.2 0.4 70 0.6 0.8 1.0 1.2 1.4 SED [kJ/L] Figure 5. Influence of external magnetic field on the decomposition rate for C7H8. C7H8 decomposition energy efficiency [g/kWh] waste treatment”, Plasma Sci. Techonol. 9 709 (2007). 10 Arc only Magnetic [3] J. F. Brilhac, B. Pateyron, G. Delluc, J. F. Coudert, and P. Fauchais, “Study of the dynamic and static behavior of dc vortex plasma torches: part I: button type cathode”, Plasma Chem. Plasma Process., 15 231 (1995) 8 110 6 90 90 70(L/min) 70 4 Gas flowrate: 70~110 L/min Discharge power: -Arc only: 0.7 kW -Magnetic: 1.4 kW 2 0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 SED [kJ/L] Figure 6. Influence of external magnetic field on the energy efficiency for C7H8 decomposition. 4. Conclusions We demonstrate the feasibility of a plasma torch assisted by the external magnetic field for the removal of tars ejected from a gasification reactor. An increase in the power applied to the solenoid allows for a more uniform plasma generation in space, and leads to the growth in arc power without increasing arc current. The increase in arc power and plasma uniformity, realized by the external magnetic field, is beneficial to the destruction of C7H8, used as a simulation gas for tars. The decomposition rate for C7H8 is enhanced with the use of external magnetic field. Acknowledgement This work was supported by Basic Research Program (SC0810 and NK163B) of the Korea Institute of Machinery & Materials. References [1] R. Benocci, G. Bonizzoni, and E. Sindoni, Thermal plasmas for hazardous waste treatment, World Scientific, London (1995). [2] L. Bin, M. Kikuchi, L. Heping, T. Iwao, and T. Inaba, “Dual torch plasma arc furnace for medical [4] J. F. Brilhac, B. Pateyron, J. F. Coudert, P. Fauchais, and A. Bouvier, “Study of the dynamic and static behavior of dc vortex plasma torches: part II: well type cathode”, Plasma Chem. Plasma Process., 15 257 (1995). [5] S. W. Chau, K. L. Hsu, D. L. Lin, and C. C. Tzeng, “Experimental study on copper cathode erosion rate and rotational velocity of magnetically driven arc in a well-type cathode non-transferred plasma torch operating in air”, J. Phys. D: Appl. Phys., 40 1944 (2007).
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