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Second-generation bioethanol

Scott, R, Conejeros, R., Aroca, G., 2013. Attainable region analysis for continuous production of second generation bioethanol. Biotechnol. Biofuels 6, 171. [Pg.308]

J. Larsen and H. Jorgensen, Methods for reducing enzyme consumption in second generation bioethanol fermentation in the pnescence of lignin, US Patent 7972826, assigned to Inbicon A/S (Fredericia, DK), July 5, 2011. [Pg.318]

Jeon YJ, Xnn Z, Rogers PL. (2010). Comparative evaluations of cellulosic raw materials for second generation bioethanol production. Lett Appl Microbiol, 51, 518-524. [Pg.195]

This technology is based on the chemical reaction and equilibrium between the sour gases, CO2 and H2S, and the ethanol amine. In this example, we are going to determine the number of units of transmission for a column that treats a gas flow of 50,000 kg/h m with a mass composition of 0.045 H2, 0.627 CO, and 0.328 CO2 in order to remove 99.9% of the CO2 present for its use in the production of second-generation bioethanol. The flow of solution is 1000 kmol/h m. The equilibrium data for the CO2 absorption in monoethanol amine (MEA) can be found in Joe et al. [7]. [Pg.419]

Xavier AM, Correia MF, Pereira SR, Evtuguin DV (2010) Second-generation bioethanol fi-om eucalypt sulphite spent liquor. Bioresour Technol 101(8) 2755-2761... [Pg.182]


See other pages where Second-generation bioethanol is mentioned: [Pg.431]    [Pg.458]    [Pg.65]    [Pg.65]    [Pg.535]    [Pg.262]    [Pg.170]    [Pg.170]    [Pg.171]    [Pg.171]    [Pg.171]    [Pg.172]    [Pg.172]    [Pg.176]    [Pg.184]    [Pg.191]    [Pg.192]    [Pg.193]    [Pg.349]    [Pg.349]    [Pg.160]    [Pg.244]    [Pg.55]    [Pg.201]    [Pg.237]    [Pg.244]   
See also in sourсe #XX -- [ Pg.170 , Pg.171 , Pg.184 , Pg.191 , Pg.192 , Pg.208 ]




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