1997
DOI: 10.1016/s0360-3199(96)00198-x
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Hynol?An economical process for methanol production from biomass and natural gas with reduced CO2 emission

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Cited by 80 publications
(41 citation statements)
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“…Steam reforming of bio-syngas with an additional natural gas feedstock is also considered as a viable option. [102][103][104][105][106] The Fe/Cu/K catalyst on Al 2 O 3 /SiO 2 support has recently demonstrated high FT activity on bio-syngas. [107] The key challenge of using bio-syngas is the clean-up step to separate tar, and other impurities prior to conversion steps.…”
Section: Synthetic Biofuelsmentioning
confidence: 99%
“…Steam reforming of bio-syngas with an additional natural gas feedstock is also considered as a viable option. [102][103][104][105][106] The Fe/Cu/K catalyst on Al 2 O 3 /SiO 2 support has recently demonstrated high FT activity on bio-syngas. [107] The key challenge of using bio-syngas is the clean-up step to separate tar, and other impurities prior to conversion steps.…”
Section: Synthetic Biofuelsmentioning
confidence: 99%
“…The process is further elaborated, including techoeconomic analysis, but no experimental data, in Borgwardt (1995) (USA), Steinberg and Dong (1996) (USA), Steinberg (1997) (USA), Dong and Steinberg (1997) (USA) Dong and Borgwardt (1998) (USA) and Sethi et al (1999) (USA).…”
Section: Pyrolysis To Hydrogen and Carbon Or Methanolmentioning
confidence: 99%
“…On the other hand, methanol can be produced from widely available agricultural, forest, and municipal waste as a renewable feedstock that can be mixed with lower-cost inputs such as coal and natural gas as fossil feedstocks. 19 If the water-to-methanol molar ratio (w) in the methanol solution is less than unity, one can assume that all of the steam is reduced to hydrogen by methanol according to eq 4. The rest of the methanol not oxidized by steam decomposes to CO and H 2 according to eq 1 if there is enough heat for 100% conversion.…”
Section: Introductionmentioning
confidence: 99%
“…The mixture heat value of a neat fuel (in units of kJ/L) can be determined from the fresh charge's molar density (ρ) after intake valve closure (IVC), the relative air/fuel ratio (λ), the mean lower heating value (LHV), and the stoichiometric oxygen (o st ), as shown in eq 6. 19 These parameters will be defined and determined for any gaseous fuel mixture in the next section.…”
Section: Introductionmentioning
confidence: 99%