An iron titanate catalyst with a crystallite phase, prepared by a co-precipitation method, showed excellent activity, stability, selectivity and SO 2 /H 2 O durability in the selective catalytic reduction of NO with NH 3 in the medium temperature range.Nitrogen oxides (NO x ) have become a major source of air pollution which can result in photochemical smog, acid rain and ozone depletion and have strong respiratory toxicity endangering human health.1 Stringent environmental legislation has been made worldwide to reduce NO x emitted from mobile and stationary resources including vehicles and coal-fired power plants. Selective catalytic reduction of NO with NH 3 (NH 3 -SCR) is an effective and economical method to remove NO and nowadays the most widely used catalyst system is V 2 O 5 -WO 3 /TiO 2 or V 2 O 5 -MoO 3 /TiO 2 with a relatively narrow temperature window of 350-400 1C.2 The problems of this system are as follows: the low N 2 selectivity in the high temperature range because of N 2 O formation and NH 3 overoxidation; the toxicity of vanadium pentoxide to the environment; and high conversion of SO 2 to SO 3 with increasing vanadium amounts, which can result in catalyst deactivation. 13 with excellent SCR activity and H 2 O/SO 2 durability in the medium temperature range. Based on the idea of combining the predominant SCR activity, thermal stability and N 2 selectivity of Fe-based catalysts and the excellent SO 2 durability of TiO 2 , here we present a novel non-toxic catalyst using an iron titanate crystallite as the active component with a broad operation window in the medium temperature range (200-400 1C) under relatively high space velocities. NO conversion at 300 1C remaining at 100% in the presence of 10% H 2 O and (or) 100 ppm SO 2 makes this catalyst a potential candidate for industrial applications.The iron titanate catalysts were prepared by the conventional co-precipitation method using Fe(NO 3 ) 3 Á9H 2 O and Ti(SO 4 ) 2 as precursors (Fe : Ti ¼ 1 : 1 in molar ratio) and 25 wt% NH 3 ÁH 2 O as precipitator with subsequent filtration, washing, and drying at 100 1C overnight and calcination at 400, 500, 600, 700 1C for 6 h, respectively (signified by Fe x TiO y -400, 500, 600, 700 1C). Catalysts sieved with 20-40 mesh were used in the activity test experiments and the reaction conditions were as follows: 0.6 ml sample, 500 ppm NO, 500 ppm NH 3 , 5% O 2 , 100 ppm SO 2 (when used), 10% H 2 O (when used), balance N 2 , 500 ml min À1 total flow rate and gas hourly space velocity (GHSV) ¼ 50 000 h
À1. The water vapor was injected with an accurate syringe pump equipped with an evaporator which was heated to 300 1C. The tubing of the activity test system was heated to 120 1C to avoid deposition of ammonium salts and water droplets. The effluent gas, including NO, NH 3 , N 2 O and NO 2 dried using CaSO 4 was continuously analyzed by an FTIR spectrometer (Thermo Nicolet Corporation Nexus 670, OMNIC Quantpad software) equipped with a heated, low volume multiple-path gas cell (2 m). The spectra were collected...