TY - JOUR
T1 - Effects of blend ratio between high density polyethylene and biomass on co-gasification behavior in a two-stage gasification system
AU - Park, Jae Hyun
AU - Park, Hyun-Woo
AU - Choi, Sooseok
AU - Park, Dong-Wha
N1 - KAUST Repository Item: Exported on 2020-10-01
Acknowledgements: This research was supported by Basic Science Research Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Education (NRF-2013R1A1A2012989) and Regional Innovation Center for Environmental Technology of Thermal Plasma (ETTP) at Inha University designated by the Ministry of Trade, Industry and Energy (2016).
PY - 2016/8/12
Y1 - 2016/8/12
N2 - The co-gasification of a high density polyethylene (HDPE) blended with a biomass has been carried out in a two-stage gasification system which comprises an oxidative pyrolysis reactor and a thermal plasma reactor. The equivalence ratio was changed from 0.38 to 0.85 according to the variation of blend ratio between HDPE and biomass. The highest production yield was achieved to be 71.4 mol/h, when the equivalence ratio was 0.47. A large amount of hydrocarbons was produced from the oxidative pyrolysis reactor as decreasing equivalence ratio below 0.41, while the CO2 concentration significantly increased with a high equivalence ratio over 0.65. The production yield was improved by the thermal plasma reactor due to the conversion of hydrocarbons into syngas in a high temperature region of thermal plasma. At the equivalence ratio of 0.47, conversion selectivities of CO and H2 from hydrocarbons were calculated to be 74% and 44%, respectively. © 2016 Hydrogen Energy Publications LLC.
AB - The co-gasification of a high density polyethylene (HDPE) blended with a biomass has been carried out in a two-stage gasification system which comprises an oxidative pyrolysis reactor and a thermal plasma reactor. The equivalence ratio was changed from 0.38 to 0.85 according to the variation of blend ratio between HDPE and biomass. The highest production yield was achieved to be 71.4 mol/h, when the equivalence ratio was 0.47. A large amount of hydrocarbons was produced from the oxidative pyrolysis reactor as decreasing equivalence ratio below 0.41, while the CO2 concentration significantly increased with a high equivalence ratio over 0.65. The production yield was improved by the thermal plasma reactor due to the conversion of hydrocarbons into syngas in a high temperature region of thermal plasma. At the equivalence ratio of 0.47, conversion selectivities of CO and H2 from hydrocarbons were calculated to be 74% and 44%, respectively. © 2016 Hydrogen Energy Publications LLC.
UR - http://hdl.handle.net/10754/621738
UR - https://linkinghub.elsevier.com/retrieve/pii/S036031991531911X
UR - http://www.scopus.com/inward/record.url?scp=84995931638&partnerID=8YFLogxK
U2 - 10.1016/j.ijhydene.2016.07.199
DO - 10.1016/j.ijhydene.2016.07.199
M3 - Article
SN - 0360-3199
VL - 41
SP - 16813
EP - 16822
JO - International Journal of Hydrogen Energy
JF - International Journal of Hydrogen Energy
IS - 38
ER -