公开(公告)号：US09663733B2

公开(公告)日：2017-05-30

申请号：US14339111

申请日：2014-07-23

申请人： ASTON UNIVERSITY

发明人： Andreas Hornung ,  Andreas Apfelbacher

IPC分类号： C07C7/00 ,  C10J3/00 ,  C10B7/10 ,  C10B49/16 ,  C10B51/00 ,  C10B53/02 ,  C10J3/20 ,  C10J3/26 ,  C10J3/66

CPC分类号： C10J3/007 ,  C10B7/10 ,  C10B49/16 ,  C10B51/00 ,  C10B53/02 ,  C10J3/20 ,  C10J3/26 ,  C10J3/66 ,  C10J2200/09 ,  C10J2300/0916 ,  C10J2300/094 ,  C10J2300/0956 ,  Y02E50/14 ,  Y02P20/145

摘要： A biomass pyrolysis process is provided in which biomass feedstock is mixed with a heat carrier. The heat carrier at least partly comprises char. The ratio by weight of biomass to char is in the range 1:1 to 1:20. The process may be carried out by in a screw/auger pyrolysis reactor in which the solid feedstock components are conveyed along the reactor by a first screw. A second screw conveys at least a portion of the solid products of the biomass pyrolysis back to a heat transfer medium input port. Thus, the heat transfer medium includes char from the biomass pyrolysis.

公开(公告)号：US20140331556A1

公开(公告)日：2014-11-13

申请号：US14339111

申请日：2014-07-23

申请人： ASTON UNIVERSITY

发明人： Andreas Hornung ,  Andreas Apfelbacher

IPC分类号： C10J3/00

CPC分类号： C10J3/007 ,  C10B7/10 ,  C10B49/16 ,  C10B51/00 ,  C10B53/02 ,  C10J3/20 ,  C10J3/26 ,  C10J3/66 ,  C10J2200/09 ,  C10J2300/0916 ,  C10J2300/094 ,  C10J2300/0956 ,  Y02E50/14 ,  Y02P20/145

摘要： A biomass pyrolysis process is provided in which biomass feedstock is mixed with a heat carrier. The heat carrier at least partly comprises char. The ratio by weight of biomass to char is in the range 1:1 to 1:20. The process may be carried out by in a screw/auger pyrolysis reactor in which the solid feedstock components are conveyed along the reactor by a first screw. A second screw conveys at least a portion of the solid products of the biomass pyrolysis back to a heat transfer medium input port. Thus, the heat transfer medium includes char from the biomass pyrolysis.

摘要翻译： 提供生物质热解方法，其中生物质原料与热载体混合。 热载体至少部分地包括炭。 生物质与焦炭的重量比在1:1至1:20的范围内。 该方法可以在螺旋/螺旋式热解反应器中进行，其中固体原料组分通过第一螺杆沿反应器输送。 第二螺杆将至少一部分生物质热解的固体产物输送回传热介质输入口。 因此，传热介质包括来自生物质热解的炭。