The characteristics of pollutant emission for non-premixed flames with LCG 8000 and LCG 6000 represented as low calorific gases were investigated by numerical simulation. Commercial software (ANSYS 16.2 - FLUENT) is used to predict 2-D pollutant emission with GRI 3.0 detailed reaction mechanism. In addition, the addition of hydrogen to LCG 6000 was also considered. As result, the flame length and temperature of LHVGs were decreased with decreasing calorific value at the same condition. In addition, NO concentration was decreased as temperature decreased. However, CO concentration for LCG 8000 predicted to be slightly higher than that for methane due to the high propane concentration. In the case of LCG 6000 with added hydrogen, the flame length was the shortest and NO concentration was the highest due to the highest flame temperature, but CO concentration decreased rapidly due to the addition of the carbon-free fuel.

Domestic industrial waste small-scale industrial incinerators produce less than 200 kg/hr; this study chose 13 of the 249 potential facilities. The target average emissions for air pollutants resulting from the facilities were SOx 13.56 ppm, NOx 82.74 ppm, NH3 19.95 ppm, HCl 54.33 ppm, HF 0.84 ppm, Hg N.D, As 0.1 ppm, H2S N.D. Dust and heavy metal analysis results for the facilities revealed Dust 32.51 mg/Sm3, Cd 0.04 mg/Sm3, Pb 0.20 mg/Sm3, Cr 0.08 mg/Sm3, and Cu 0.03 mg/Sm3. Combustion indicators were O2 11.58% and CO 271.20 ppm. Average PCDDs/DFs were 17.87 ng ITEQ/ ton. The target facilities were equipped with anti-pollution facilities. However, some items were found to exceed the emission standards. These results are even equipped with control facilities due to manual limitation actions of the management personnel. Therefore, it is determined that the emission control of contaminants is difficult.

Waste electrical and electronic equipment (WEEE) has been received much attention recently due to rapid changes in materials and shorter replacement of consumer products. Most of WEEEs are collected and recycled at the designated recycling centers in Korea, and final residues after recycling, sorting and shredding them to separate valuable and recyclable parts in series are left as forms of shredded plastic mixtures, which would be a problem to be resolved. By further plastics separation the polyurethane foams are mostly remained and becomes waste to be treated by appropriate methods. Gasification to produce syngas and incineration to recover energy for such polyurethane foam waste could be utilized instead landfill presently treated. In this study the experiment was conducted to evaluate such performance characteristics of thermal processes. Pelletized solid refuse fuel (SRF) was fabricated to feed into the test furnace even though it was light with low density. Thermogravimetric analysis, proximate analysis and higher heating value were made. During gasification and incineration, gas composition with gaseous pollutants were measured. Due to nitrogen content in polyurethane, nitrogen containing gaseous substances such as NH3 and HCN were observed with varying equivalent air ratios (ERs). The assessment of polyurethane waste foam to energy using incineration and gasification was made with finding out the optimal condition of air injection to emit less pollutants in both operations. Produced syngas could be utilized as energy fuels by lowering pollutants emission.