V2O5/TiO2 catalyst impregnated ceramic candle filters are in principle, capable of performing shallow-bed dust filtration plus a catalytic reaction, promoted by a catalytic deposited in their inner structure. Pilot-scale V2O5/TiO2 catalyst impregnated ceramic candle filters were prepared, characterized and tested for their activity towards the SCR reaction. The effect on NO conversion of operating temperature, gas hourly space velocity, amount of deposited catalyst, pressure drops and long-term experiment (life of catalytic filter) was determined. The following effects of V2O5/TiO2 catalyst impregnated ceramic candle filters in SCR reaction are observed: (1) It increases the activity and widens the temperature window for SCR. (2) When the content of V2O5 catalyst increases further from 3 to 9wt.%, activity of NO increases. (3) NO conversion at first increases with temperature and then decreases at high temperatures (above 400℃ over), possibly due to the occurrence of the ammonia oxidation reaction.

This study was conducted to investigate the removal characteristics of PO4 3- -P contained in livestock wastewater using waste concrete. With small particle size, increased dosage and temperature of water, PO4 3- -P was well removed by waste concrete. PO4 3- -P was removed by adsorption reaction in low pH of the primary phase, but the crystallization reaction predominated for increasing pH with passed time. As a result of adapting the adsorption isotherm equation, PO4 3- -P removal was more affected by the crystallization reaction than the adsorption reaction. In the SEM micrograph, there was no evident change on the waste concrete surface. Particle size was plate-phase before reaction but appeared a dense form to progress in the crystallization reaction after reaction.