tubular flow reactor to investigate the influence of reaction temperature and chlorine content on chlorinated waste combustion and find incineration process optimization methods for pollution control. The reaction temperature varies from 700 o C to 1000 o C and the CCl 4 /CH 4 (or Cl/H) mole ratio of the inlet mixture varies from 0.21 to 0.84. Products profiles are measured with FT-IR. It is shown that at the same initial CCl 4 concentration and reaction temperature adding CH 4 favors CCl 4 destruction and CO 2 formation. But the destruction and removal efficiency (DRE) of CH 4 decreases with lower Cl/H and higher concentrations of toxic products of incomplete combustion such as COCl 2 and CH 3 Cl are formed at the same time. The chlorine in the system favors CH 4 decomposition, but it also inhibits further oxidation of CO. Higher temperature assists in both CCl 4 destruction and CH 4 conversion, and the concentration of toxic combustion intermediates is reduced. Increasing the temperature is the most effective way to enhance CCl 4 oxidation. The CO 2 concentration increases with temperature. A CO concentration peak is observed around 800 o C: with a certain Cl/H, the CO concentration first increases with temperature and then declines. The effect of increasing CH 4 concentration on CCl 4 destruction becomes mild above 900 o C. Rather, it enhances the interaction between chlorine and carbonaceous radicals, which leads to higher concentration of toxic products. hazardous waste, destruction and removal efficiency (DRE) , oxidation, carbon tetrachloride, chlorinated compounds, methane Citation: Wang B, Chi Y, Yan J H, et al. Experimental study on CCl 4 /CH 4 /O 2 /N 2 oxidation.