Abstract:This critical review focuses on potential routes for the multi-production of chemicals and fuels in the framework of thermochemical biorefineries. The up-to-date research and development in this field has been limited to BTL/G (biomass-to-liquids/gases) studies, where biomass-derived synthesis gas (syngas) is converted into a single product with/without the co-production of electricity and heat. Simultaneously, the interest on biorefineries is growing but mostly refers to the biochemical processing of biomass.… Show more
“…A water/steam electrolysis plant is such a consumer [7]. The hydrogen generated by the electrolyser could be converted back to electricity when the demand for electricity is high, but it could be more economically attractive as well as more environmentally attractive to have the opportunity to use the hydrogen for fuel production 2 . If the hydrogen is used for fuel production, a link has been created between the power grid and the transportation sector.…”
Section: H2o + Co ↔ H2 + Co2mentioning
confidence: 99%
“…The conventional way of doing this adjustment is by changing the H 2/CO-ratio in the syngas by using the water gas shift (WGS) reaction (eq. 1) followed by removal of the produced CO2 [2]. This CO2 will typically be vented to the atmosphere, but if it was compressed and stored underground (CCS), the complete biorefinery would have the effect of reducing the CO2 content in the atmosphere and would thereby be a climate-mitigating technology.…”
Document Version Peer reviewed version Link back to DTU Orbit
Citation (APA):Clausen, L. R. (2015). Maximizing biofuel production in a thermochemical biorefinery by adding electrolytic hydrogen and by integrating torrefaction with entrained flow gasification. Energy, 85, 94-101. DOI: 10.1016/j.energy.2015 Maximizing biofuel production in a thermochemical biorefinery by adding electrolytic hydrogen and by integrating torrefaction with entrained flow gasification
AbstractIn a "conventional" thermochemical biorefinery, carbon is emitted from the plant in the form of CO2 to make the synthesis gas from the gasifier suitable for fuel production. The alternative to this carbon removal is to add hydrogen to the plant. By adding hydrogen, it is possible to more than double the biofuel production per biomass input by converting almost all of the carbon in the biomass feed to carbon stored in the biofuel product. Water or steam electrolysis can supply the hydrogen to the biorefinery and also the oxygen for the gasifier. This paper presents the design and thermodynamic analysis of two biorefineries integrating water electrolysis for the production of methanol. In both plants, torrefied woody biomass is supplied to an entrained flow gasifier, but in one of the plants, the torrefaction process occurs on-site, as it is integrated with the entrained flow gasification process. The analysis shows that the biorefinery with integrated torrefaction has a higher biomass to methanol energy ratio (136% vs. 101%) as well as higher total energy efficiency (62% vs. 56%). By comparing with two identical biorefineries without electrolysis, it is concluded that the biorefinery with integrated torrefaction benefits most from the integration of electrolysis.
“…A water/steam electrolysis plant is such a consumer [7]. The hydrogen generated by the electrolyser could be converted back to electricity when the demand for electricity is high, but it could be more economically attractive as well as more environmentally attractive to have the opportunity to use the hydrogen for fuel production 2 . If the hydrogen is used for fuel production, a link has been created between the power grid and the transportation sector.…”
Section: H2o + Co ↔ H2 + Co2mentioning
confidence: 99%
“…The conventional way of doing this adjustment is by changing the H 2/CO-ratio in the syngas by using the water gas shift (WGS) reaction (eq. 1) followed by removal of the produced CO2 [2]. This CO2 will typically be vented to the atmosphere, but if it was compressed and stored underground (CCS), the complete biorefinery would have the effect of reducing the CO2 content in the atmosphere and would thereby be a climate-mitigating technology.…”
Document Version Peer reviewed version Link back to DTU Orbit
Citation (APA):Clausen, L. R. (2015). Maximizing biofuel production in a thermochemical biorefinery by adding electrolytic hydrogen and by integrating torrefaction with entrained flow gasification. Energy, 85, 94-101. DOI: 10.1016/j.energy.2015 Maximizing biofuel production in a thermochemical biorefinery by adding electrolytic hydrogen and by integrating torrefaction with entrained flow gasification
AbstractIn a "conventional" thermochemical biorefinery, carbon is emitted from the plant in the form of CO2 to make the synthesis gas from the gasifier suitable for fuel production. The alternative to this carbon removal is to add hydrogen to the plant. By adding hydrogen, it is possible to more than double the biofuel production per biomass input by converting almost all of the carbon in the biomass feed to carbon stored in the biofuel product. Water or steam electrolysis can supply the hydrogen to the biorefinery and also the oxygen for the gasifier. This paper presents the design and thermodynamic analysis of two biorefineries integrating water electrolysis for the production of methanol. In both plants, torrefied woody biomass is supplied to an entrained flow gasifier, but in one of the plants, the torrefaction process occurs on-site, as it is integrated with the entrained flow gasification process. The analysis shows that the biorefinery with integrated torrefaction has a higher biomass to methanol energy ratio (136% vs. 101%) as well as higher total energy efficiency (62% vs. 56%). By comparing with two identical biorefineries without electrolysis, it is concluded that the biorefinery with integrated torrefaction benefits most from the integration of electrolysis.
“…The production of DME (that e.g., could be produced via methanol dehydration) has also been studied for the aforementioned applications. The objectives of the studies include benchmarking technologies (Ciferno and Marano, 2002); reviewing potential routes (Haro et al, 2013a); conducting techno-economic assessments (Hamelinck and Faaij, 2002;Hannula and Arpiainen, 2014;Haro et al, 2013b); or combining techno-economic and carbon accounting assessments (Gilbert et al, 2014).…”
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