significant influences on the formation of these radicals [1,2]. Operation conditions, i.e. reaction temperature, gas flow rate, and reactor parameters, are also important factors affecting the non-thermal plasma process [3]. NH 3 injection provides reductive radicals, thus enhances the removal rate of the pollutants [4,5], and neutralizes nitric acids which are produced by the interaction of the radicals with NO.In this study, the influences of gas compositions and reaction conditions, including inlet NO, O 2 , CO 2 , H 2 O, and NH 3 concentrations, temperature, gas flow rate, and reactor parameter, on total NO conversion and NO oxidation to NO 2 were experimentally investigated in a link tooth wheelcylinder discharge reactor by utilizing a positive DC power supply.
Experimental methodsThe schematic diagram of the experimental setup is shown in Fig. 1.The feed gas compositions and gas flow rate were controlled by mass flow controllers. Water was introduced into the system with a temperature controlled bubble tower. A tubular pre-heater was used to heat the feed gas. The feed gas consisted of air, 500 ppm NO, and the reaction temperature and flow rate were 15°C and 5.0 L/min, respectively, except when described especially. The treated gas was either conducted into a chemiluminescent NO-NO x analyzer (Thermo Electron Corp. Model 44) for NO and NO x measurement, or chemically absorbed by solutions for O 3 and NH 3 measurement by an Indigo disulphonate spectrophotometry and soldium salicylate-soldium hypochloritometric method, respectively.A link tooth wheel-cylinder discharge reactor energized by a positive DC power supply, shown in Fig. 2(a), was used in the study. This reactor consisted of a stainless steel wire electrode (3 mm diameter) as an active electrode and a stainless steel cylinder (42 mm inner diameter, 400 mm long) as a Abstract The effects of gas compositions and reaction conditions on NO conversion by positive streamer discharge were experimentally investigated by using a link tooth wheelcylinder reactor. The results showed that NO conversion increased with increasing O 2 concentration and NH 3 concentration, but decreased with increasing inlet NO concentration and gas flow rate. The addition of CO 2 or H 2 O to the feed gas promoted NO conversion by increasing the maximum discharge voltage, and NH 4 NO 3 was formed in the presence of NH 3 . There was a most suitable range interval between discharge tooth wheels if both NO conversion and energy consumption were considered. Increasing applied voltage resulted in the increase in the amount of O 3 generated by streamer discharge.