Author/Authors :
Wang، نويسنده , , Jingbo and Xu، نويسنده , , Shan-Shan Xiao، نويسنده , , Bo and Xu، نويسنده , , Minghou and Yang، نويسنده , , Lin and Liu، نويسنده , , Shiming and Hu، نويسنده , , Zhiquan and Guo، نويسنده , , Dabin and Hu، نويسنده , , Mian and Ma، نويسنده , , Caifeng and Luo، نويسنده , , Siyi، نويسنده ,
Abstract :
The catalytic steam gasification of pig compost (PC) for hydrogen-rich gas production was conducted in a fixed-bed reactor. The influence of the catalyst and reactor temperature on yield and product composition was studied at the temperature range of 700–850 °C, for weight hourly space velocity (WHSV) in the range of 0.30–0.60 h−1. The results indicate that the developed NiO on modified dolomite (NiO/MD) catalyst reveals better catalytic performance on the tar elimination and hydrogen yield than calcined MD or NiO/γ-Al2O3 catalyst. Meanwhile, the lower WHSV and higher reactor temperature can contribute to more hydrogen production and gas yield. Moreover, the char from catalytic steam gasification of PC has a highest ash content of 75.84% at 850 °C. In conclusion, pig compost is a potential candidate for hydrogen gas production through catalytic steam gasification technology.
Keywords :
Hydrogen production , gasification , Catalyst , Pig compost