作者: Wei Wan , Zhenghua Dai , Chao Li , Guangsuo Yu , Fuchen Wang
DOI: 10.1016/J.IJHYDENE.2014.03.032
关键词: Waste management 、 Process simulation 、 Coal water 、 Coal 、 Process integration 、 Thermodynamics 、 Chemistry 、 Raw material 、 Exergy efficiency 、 Water-gas shift reaction 、 Energy conversion efficiency
摘要: Abstract In order to achieve the energy cascade utilization and improve efficiency of coal–water–slurry (CWS) gasification for hydrogen system, heat integration scheme (HIS) between water gas shift unit is put forward. The effects temperature change CWS oxygen on performance are investigated. Both HIS non-heat (NHIS) analyzed by using performance, conversion exergy efficiency. results show that specific coal consumption decrease 2.7% 6.5%, respectively, as feedstock preheated up 150 °C. NHIS nearly same. (62.66%) better than (62.02%). Therefore, WGS unit.