| dc.creator |
Kihedu, Joseph H. |
|
| dc.creator |
Yoshiie, Ryo |
|
| dc.creator |
Naruse, Ichiro |
|
| dc.date |
2016-06-17T19:52:52Z |
|
| dc.date |
2016-06-17T19:52:52Z |
|
| dc.date |
2015-08-08 |
|
| dc.date.accessioned |
2018-03-27T08:37:39Z |
|
| dc.date.available |
2018-03-27T08:37:39Z |
|
| dc.identifier |
Kihedu, J., Yoshiie, R., & Naruse, I. (2016). Performance indicators for air and air–steam auto-thermal updraft gasification of biomass in packed bed reactor. Fuel Processing Technology, 141, 93-98. http://dx.doi.org/10.1016/j.fuproc.2015.07.015 |
|
| dc.identifier |
0378-3820 |
|
| dc.identifier |
http://hdl.handle.net/20.500.11810/2539 |
|
| dc.identifier |
doi:10.1016/j.fuproc.2015.07.015 |
|
| dc.identifier.uri |
http://hdl.handle.net/20.500.11810/2539 |
|
| dc.description |
Full text can be accessed at the following link http://www.sciencedirect.com/science/article/pii/S0378382015300928 |
|
| dc.description |
Auto-thermal updraft gasification of biomass pellets in a packed bed reactor was conducted by using air and air–steam mixture. Air–steam gasification produced syngas with slightly improved lower heating value of 4.5 MJ/mN3 in comparison to 4.4 MJ/mN3 produced during air gasification. The corresponding tar generation for air gasification and air–steam gasification was 21.2 g/mN3 and 26.2 g/mN3, respectively. Cold gas efficiency for air gasification and air–steam gasification was realized to be 91% and 91.4%, respectively. Carbon conversion during air–steam gasification reached about 91.5% while carbon conversion during air gasification was limited to 84.3%. |
|
| dc.language |
en |
|
| dc.publisher |
Sciencedirect |
|
| dc.subject |
Biomass gasification |
|
| dc.subject |
Updraft |
|
| dc.subject |
Auto-thermal |
|
| dc.subject |
Packed bed reactor |
|
| dc.title |
Performance indicators for air and air–steam auto-thermal updraft gasification of biomass in packed bed reactor |
|
| dc.type |
Journal Article, Peer Reviewed |
|