Catalytic gasification of a pig compost (PC) was investigated over transition metal catalysts (TMCs, including limonite, CoMo/Al 2 O 3 , Ni/Al 2 O 3 , and nickel loaded on lignite char) and Ca-based catalysts (dolomite and CaO) in a two-stage fixed-bed reactor to understand the effects of catalyst, temperature, and steam on nitrogen distributions. Non-catalytic thermal decomposition (TD) of PC volatiles below 750 o C is not effective for decomposing the entire volatile nitrogen species (VNSs) to N 2. NH 3 was found to be the predominant nitrogenous gas under inert conditions used in this investigation, and its yield increased with raising TD temperature. The N yield in HCN is lower than 5% below 550 o C, and sharply increased to 13.9% at 750 o C due to TD of volatiles. Most of VNSs were converted to N 2 over TMCs, especially over Ni-based ones. The TMCs proved to be quite active not only for tar reduction, but also for VNSs decomposition at 450-650 o C. On the contrary, CaO-based catalysts, especially dolomite, significantly promoted the conversion of VNSs to NH 3. Ni/Al 2 O 3 effectively promoted the conversion of NH 3 and HCN to N 2 at 550 o C. Steam introduced mainly prevented HCN decomposition over dolomite and coke deposition over Ni/Al 2 O 3. This study provides a basic insight into the nitrogen transformations during catalytic gasification of PC, which would benefit the clean utilization of PC as an energy source.