2018
DOI: 10.1016/j.fuel.2018.08.004
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Improving carbon efficiency and profitability of the biomass to liquid process with hydrogen from renewable power

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Cited by 91 publications
(103 citation statements)
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“…With an average insolation of 220 W/m 2 (corresponding to a total incoming solar power of 120 MW) and 20% efficient PV modules, the facility produces an average of 24 MW el of electrical power. A physical model for the chemical processing equipment, analyzed using the Aspen Hysys software (54), is proposed in SI Appendix: An input seawater flow of 6.2 t/h undergoes reverse osmosis desalination and electrolysis, consuming 18 MW el and producing 0.345 t/h H 2 . Some of the produced oxygen is used to combust excess H 2 to provide process heat.…”
Section: Solar Methanol Island Operationmentioning
confidence: 99%
“…With an average insolation of 220 W/m 2 (corresponding to a total incoming solar power of 120 MW) and 20% efficient PV modules, the facility produces an average of 24 MW el of electrical power. A physical model for the chemical processing equipment, analyzed using the Aspen Hysys software (54), is proposed in SI Appendix: An input seawater flow of 6.2 t/h undergoes reverse osmosis desalination and electrolysis, consuming 18 MW el and producing 0.345 t/h H 2 . Some of the produced oxygen is used to combust excess H 2 to provide process heat.…”
Section: Solar Methanol Island Operationmentioning
confidence: 99%
“…In all processes mentioned in Figure 6, except fermentation which does not involve high temperatures, RWGS can be effectively thermally integrated with the remaining process components to lower the external energy requirements. As suggested by Hillestad et al [39], RWGS reactor can be placed within the gasifier or incinerator to increase CO 2 conversion as a result of the increased temperature. High temperature conditions are essential for the reaction kinetics, as it reduces the residence time required to attain equilibrium.…”
Section: Reverse Water Gas Shift (Rwgs)mentioning
confidence: 99%
“…This has implication on the required volume for the RWGS reactor. For instance, the RWGS reactor volume required to reach equilibrium decreases 6-fold by simply increasing the RWGS reactor temperature from 1100 • C to 1200 • C [39]. integrated with the remaining process components to lower the external energy requirements.…”
Section: Reverse Water Gas Shift (Rwgs)mentioning
confidence: 99%
“…The FT method defines the catalytic transform of carbon dioxide and hydrogen gas as a result of the gasification of biomass to a liquid state of hydrocarbon [9]. The nature of hydrocarbon turn to a catalyst and some other factor such as temperature, pressure and other conditions [10].…”
Section: A Thermochemical Technologymentioning
confidence: 99%