Effect of Generating Heat on Ozone Generation in Dielectric Cylinder-Cylinder DBD Ozone Generator ()
1. Introduction
Nowadays, ozone has attracted attention in the environmental improvement technology, when the environmental problem has become a topic on a world scale. Since ozone is one of the strongest oxidants, it is widely used for treatment of wasted water and offensives odors, disinfections and the removal of organic substances [1]. Ozone is widely used in industrial and domestic applications. It is also widely used in food processing, food storage, odor abatement, groundwater remediation and drinking water purification [2-4].
In current industrial ozone generators, the DBD discharge configuration is usually employed. In this arrangement, dried air or oxygen flows through a discharge gap of 1 - 2 mm width. One side of the gap is formed by a metal electrode at ground potential and the other one by a dielectric, normally glass or ceramic, in good contact with a high voltage electrode. An alternating voltage is applied across the two electrodes so that the resulting alternating electric field is high enough to raise electrical breakdown. Since ozone generators operate at pressures of a few bars, the peak voltage of several kilovolts is needed to initiate the discharge [5].
Recently, DBD is the most extensively studied for ozone generation. It is known that DBD generates a nonthermal equilibrium plasma even under atmospheric pressure, which is suitable for ozone production [6-9]. However, some ozone generator configurations generate inhomogeneous heat-up of the dielectric barrier and result in the decrease of ozone production efficiency. Experimental studies concerning ozone generator configuration such as electrode arrangements, gap lengths, dielectric materials, operating gases and electrical discharges have been widely studied to obtain the optimum discharge conditions for high yield ozone production [8-17].
In this work, a cylinder-cylinder DBD ozone generator has been developed. The heat generated in the ozone tube was investigated using a thermal camera and reported as IR images and temperature values. The ozone concentration as a function of operating time of ozone tube was also measured. The relation between the ozone concentration and temperature was reported.
2. Experimental Arrangements
2.1. Experimental Setup
Figure 1 shows the schematic diagram of the experimental setup. A commercial grade oxygen from oxygen tank with a purity of 95% was used for ozone production. It was filtered and controlled by a pressure regulator to release oxygen at a constant pressure of 4.0 atm. Then, it passed through the mass flow controller which controlled
Figure 1. Schematic diagram of the experimental setup for ozone generation.
the oxygen flow rate. The selected pressure and flow rate of oxygen finally passed into the ozone tube. Oxygen in the ozone tube was discharged by a high voltage power supply and ozone was released to the ozone monitor. In this work, the oxygen flow rate and oxygen pressure were kept constant at 12 L/min and 1.02 atm., respectively.
2.2. Ozone Tube
Figure 2 shows the configurations of the ozone tube. It consisted of a stainless steel sheath with an outer diameter of 40 mm and 24 cm long. It was inserted in a glass tube with a tight contact of their surfaces. The glass tube with a thickness of 1.7 mm, 30 cm long and 42 mm outer diameter was used as a dielectric barrier. The grounded cylindrical electrode was a stainless steel tube with an inner diameter of 43 mm and 25 cm long. Therefore, the air gap and active length of the ozone tube to produce ozone were 0.5 mm and 24 cm, respectively.
2.3. High Voltage Power Supply
The high voltage power supply used in this study is of a switching type. Figure 3 shows the schematic diagram of the high voltage switching power supply. A 220 V ac voltage was stepped down by a transformer and rectified by a rectifier into dc voltage of about 72 V. IGBT (Insulated Gate Bipolar Transistor) was used as electronic switch and controlled by an oscillator to generate a high frequency current in the range of 0 - 4 Arms (0 - 24 Ap-p). Low voltage with high frequency current was stepped up by a high voltage step up transformer, and then the voltage of 1 - 10 kV at frequency of 0 - 10 kHz was obtained. In present work, the optimum frequency to discharge oxygen in the ozone tube was 3.7 kHz.
2.4. Electrical Measurements
The voltage and current were measured using a high voltage probe (Fluke 80K-6) and a current probe (Fluke 40i-1105), respectively. Waveforms were recorded using a digital storage oscilloscope (Agilent 54621A).
Figure 2. Configurations of the ozone tube.
2.5. Ozone Concentration Measurements
The ozone released from the ozone tube as shown in the experimental setup (Figure 1) was measured using an ozone monitor (Quant Ozone “2”). The measurements were carried out at an oxygen pressure of 1.02 atm and an oxygen flow rate of 12 L/min.
2.6. Temperature Measurements
The heat generated in the ozone tube was investigated using a thermal camera (Infra Tech, model Image IR 3300U). The IR images corresponding to the generated heat were obtained. In addition, the temperature of the ozone tube surface at different areas was also obtained from IR camera. The IR images of the ozone tube at 5 positions as shown in Figure 4 were recorded simultaneously, and then the corresponding surface temperatures were displayed. The operating time of the ozone tube for IR imaging was 10 min.
3. Results and Discussion
The typical waveforms of the discharge voltage, current and power at an oxygen pressure of 1.02 atm and an oxygen flow rate of 12 L/min are shown in Figures 5 (a)-(c), respectively.
The variations of the ozone concentration, voltage and current as a function of the operating time of the ozone tube are shown in Figures 6(a)-(c), respectively.
As seen in Figure 6(a), it is clearly observed that the ozone concentration decreases rapidly with increasing operating time of the ozone tube. The ozone concentration decreased from about 14 g/h at the beginning to 3 g/h after the ozone generator operates for 10 min. How
Figure 4. Schematic diagram for IR imaging.
Figure 5. Waveforms of: (a) discharge voltage, (b) current and (c) power.
ever, the voltage and current are considerably constant through the whole range of operating time.
Figure 7 shows the IR images of the ozone tube surface from the beginning to the 10th min. The temperatures at the positions 1, 2, 3, 4 and 5 on the ozone tube surface were recorded simultaneously. The surface temperatures of the positions 1, 2, 3, 4 and 5 as a function of the operating time are shown in Figure 8.
It is seen that the temperature at all positions on the ozone tube surface increases with the increase of operating time. Furthermore, the temperatures at different positions are significantly different. At the position close to the oxygen inlet such as position 1, the temperature is much lower than that of the one that far from the oxygen inlet such as position 5. The maximum temperature change with operating time is observed at the position 5. The temperature is found to increase from room temperature (26.0˚C) to 97.0˚C after operating of the ozone tube for 10 min. The increase of the temperature of the ozone tube results in the decrease of the ozone concentration as confirmed by Figure 6(a).
The present work has shown that the heat is generated rapidly in the ozone tube. In addition, the heat generated at different positions along the ozone tube is much dif ferent. The generating of the inhomogeneous heat-up
Figure 6. Variations of: (a) ozone concentration, (b) rms voltage and (c) rms current as a function of the operating time.
Figure 7. IR images of the ozone tube surface at different operating times.
Figure 8. Variations of the surface temperature at different positions on the ozone tube as a function of the operating time.
results in the decrease of ozone production efficiency. Therefore, the heat generated in the ozone tube has much effect on the production of ozone in the ozone generator. We can improve the efficiency of the ozone production system by reducing the heat from the ozone tube surface. One method can be made by covering the grounded cylindrical electrode (outer stainless steel tube) with a heat dissipator. For example, two half-cylindrical aluminum tubes with longitudinal fins can be used to cover the grounded stainless electrode, which behave as a heat dissipater. This work will be left for further development.
4. Conclusion
In this work, a cylinder-cylinder DBD ozone generator has been developed. The ozone concentration measurements and the investigation of heat generated on the ozone tube surface were carried out at an oxygen pressure of 1.02 atm and an oxygen flow rate of 12 L/min. It was found that the heat generated in the ozone tube during the operation of the ozone generator significantly reduced the ozone production efficiency.
5. Acknowledgements
This work had partially been supported by Thailand Center of Excellence in Physics (ThEP) and King Mongkut’s University of Technology Thonburi under The National Research University Project.
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