TY - JOUR
T1 - Supercritical water gasification of biomass for H2 production
T2 - Process design
AU - Fiori, Luca
AU - Valbusa, Michele
AU - Castello, Daniele
PY - 2012/10
Y1 - 2012/10
N2 - The supercritical water gasification (SCWG) of biomass for H2 production is analyzed in terms of process development and energetic self-sustainability. The conceptual design of a plant is proposed and the SCWG process involving several substrates (glycerol, microalgae, sewage sludge, grape marc, phenol) is simulated by means of AspenPlus™. The influence of various parameters - biomass concentration and typology, reaction pressure and temperature - is analyzed. The process accounts for the possibility of exploiting the mechanical energy of compressed syngas (later burned to sustain the SCWG reaction) through expansion in turbines, while purified H2 is fed to fuel cells. Results show that the SCWG reaction can be energetically self-sustained if minimum feed biomass concentrations of 15-25% are adopted. Interestingly, the H2 yields are found to be maximal at similar feed concentrations. Finally, an energy balance is performed showing that the whole process could provide a net power of about 150kWe/(1000kgfeed/h).
AB - The supercritical water gasification (SCWG) of biomass for H2 production is analyzed in terms of process development and energetic self-sustainability. The conceptual design of a plant is proposed and the SCWG process involving several substrates (glycerol, microalgae, sewage sludge, grape marc, phenol) is simulated by means of AspenPlus™. The influence of various parameters - biomass concentration and typology, reaction pressure and temperature - is analyzed. The process accounts for the possibility of exploiting the mechanical energy of compressed syngas (later burned to sustain the SCWG reaction) through expansion in turbines, while purified H2 is fed to fuel cells. Results show that the SCWG reaction can be energetically self-sustained if minimum feed biomass concentrations of 15-25% are adopted. Interestingly, the H2 yields are found to be maximal at similar feed concentrations. Finally, an energy balance is performed showing that the whole process could provide a net power of about 150kWe/(1000kgfeed/h).
KW - Energy analysis
KW - Hydrothermal gasification
KW - Process design
KW - Process modeling
KW - Supercritical water gasification
UR - http://www.scopus.com/inward/record.url?scp=84864408092&partnerID=8YFLogxK
U2 - 10.1016/j.biortech.2012.06.116
DO - 10.1016/j.biortech.2012.06.116
M3 - Journal article
C2 - 22858478
AN - SCOPUS:84864408092
SN - 0960-8524
VL - 121
SP - 139
EP - 147
JO - Bioresource Technology
JF - Bioresource Technology
ER -