Sequential supercritical water gasification and partial oxidation of hog manure
Sequential supercritical water gasification and partial oxidation of hog manure
复制标题
DOI:
10.1016/j.ijhydene.2010.08.097
复制
发表时间:
2010-11
期刊:
影响因子:
--
通讯作者:
Emhemmed A. Youssef;E. Elbeshbishy;H. Hafez;G. Nakhla;P. Charpentier
中科院分区:
文献类型:
--
作者:
Emhemmed A. Youssef;E. Elbeshbishy;H. Hafez;G. Nakhla;P. Charpentier
The catalytic hydrogen production from hog manure using supercritical water gasification and partial oxidation was investigated in a batch reactor at a temperature of 500°C, and pressure of 28MPa using several metallic catalysts. Hog manure was characterized by a total and soluble chemical oxygen demand (TCOD, SCOD) of 57,000 and 28,000mg/L, total and volatile suspended solids (TSS, VSS) of 25,000, 19,000, and ammonia of 2400mg/L, respectively. The order of H2production was the following: Pd/AC>Ru/Al2O3>Ru/AC>AC>NaOH, and the order of COD reduction efficiency was as follows: NaOH>Ru/AC>AC>Ru/Al2O3>Pd/AC. The behavior of the volatile fatty acids (VFAs), ethanol, methanol, ammonia, H2S, and sulfate was investigated experimentally and discussed. A 35% reduction in the H2and CH4yields was observed in the sequential gasification partial oxidation (oxidant at an 80% of theoretical requirement) experiments compared to the gasification experiments (catalyst only). Moreover, this reduction in gas yields was coincided with a 45% reduction in the liquid effluent chemical oxygen demand (COD), 60% reduction of the ammonia concentration in the liquid effluent, and 20% reduction in the H2S concentration in the effluent gas.