Hydrogen sulfide (H 2 S) removal and catalytic ammonia (NH 3 ) decomposition performance of limonite in the presence of coke oven gas (COG) components has been studied in a cylindrical quartz reactor at 300-850°C under a high space velocity of 51 000 h − 1 to develop a novel hot gas cleanup method. The H 2 S removal behavior in 50% H 2 /He depends on the temperature, with high performance observed at lower temperature. An investigation of the removal behavior of H 2 S in the presence of COG components (CH 4 , CO, CO 2 and H 2 O) at 400°C reveals that CH 4 does not affect the removal performance. On the other hand, the coexistence of CO drastically decreases the H 2 S removal performance. However, the addition of 5% H 2 O to 50% H 2 /30% CH 4 /5% CO/He dramatically improves the H 2 S removal performance, whereas the performance is low at 5% CO 2 with 50% H 2 /30% CH 4 /5% CO/He. In addition, the H 2 S breakthrough curve strongly depends on the space velocity.The limonite catalyst achieves almost complete decomposition of NH 3 in He at 850°C until 240 min. When the decomposition run is performed in the presence of COG components, the coexistence of 30% CH 4 deactivates limonite with significant formation of deposited carbon. On the other hand, the addition of 5% CO 2 , 5% H 2 O or 5% CO 2 /5% H 2 O to 50% H 2 /30% CH 4 /5% CO improves the catalytic activity without carbon deposition, and > 99% conversion of NH 3 to N 2 is maintained until 240 min.