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.

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

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

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.

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.

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.