요 약V 2 O 5 /TiO 2 계 촉매상에서 NH 3 에 의한 NO x 의 선택적환원은 310의 지구온난화지수를 갖는 N 2 O의 또 다른 인위적인 배출원이 될 수 있는 것으로 보고되고 있으므로, 본 총설은 화석연료를 연소시키는 화력발전소용 상기 촉매상에서 SCR 탈질반응 동안에 N 2 O 생성과 관계되는 주요 변수들의 유의성을 다루고자 한다.Abstract − Selective catalytic reduction of NO x by NH 3 (NH 3 -SCR) over V 2 O 5 /TiO 2 -based catalysts is recently reported to be an anthropogenic emitter of N 2 O that is a global warming gas with a global warming potential of 310. Therefore, this review will get a touch on significance of some parameters regarding N 2 O formation in the deNO x ing reaction for fossil fuels-fired power plants applications. The N 2 O production in NH 3 -SCR reaction with such catalysts occurs via side reactions between NOx and NH 3 in addition to NH 3 oxidation, and the extent of these undesired reactions depends strongly on the loadings of V 2 O 5 as a primary active component and the promoter as a secondary one (WO 3 and MoO 3 ) in the SCR catalysts, the feed and operating variables such as reaction temperature, NO 2 /NO x ratio, oxygen concentration, gas hourly space velocity, water content and thermal excursion, and the physical and chemical histories of the catalysts on site. Although all these parameters are associated with the N 2 O formation in deNO x ing reaction, details of some of them have been discussed and a better way of suppressing the N 2 O production in commercial SCR plants has been proposed.