Proper ultrasound treatment increases ethanol production from simultaneous saccharification and fermentation of sugarcane bagasse

RSC Advances ◽  
2016 ◽  
Vol 6 (94) ◽  
pp. 91409-91419 ◽  
Author(s):  
Rajendran Velmurugan ◽  
Aran Incharoensakdi
Keyword(s):  
Ethanol Production ◽  
Sugarcane Bagasse ◽  
Simultaneous Saccharification And Fermentation ◽  
Ethanol Yield ◽  
Ultrasound Treatment ◽  
Fermentation Processes ◽  
Cellulase Complex ◽  
Simultaneous Saccharification

To improve the saccharification and fermentation processes, proper ultrasound was applied which resulted in the presence of cellulase complex with improved β-glucosidase ratio leading to enhanced overall ethanol yield.

Fuel Ethanol Production from Wet Oxidised Corn Stover by S. Cerevisiae

2011 ◽  
Vol 343-344 ◽  
pp. 963-967 ◽  
Author(s):  
Zhang Qiang ◽  
Anne Belinda Thomsen
Keyword(s):  
Ethanol Production ◽  
Corn Stover ◽  
Simultaneous Saccharification And Fermentation ◽  
Ethanol Concentration ◽  
Ethanol Yield ◽  
Liquid Fraction ◽  
Raw Material ◽  
Wet Oxidation ◽  
Inhibition Effect ◽  
Simultaneous Saccharification

In order to find out appropriate process for ethanol production from corn stover, wet oxidation（195°C，15 minutes）and simultaneous saccharification and fermentation (SSF) was carried out to produce ethanol. The results showed that the cellulose recovery of 92.9% and the hemicellulose recovery of 74.6% were obtained after pretreatment. 86.5% of cellulose was remained in the solid cake . After 24h hydrolysis at 50°C using cellulase（Cellubrix L）,the achieved conversion of cellulose to glucose was 64.8%. Ethanol production was evaluated from dried solid cake and the hydrolysate was employed as liquid fraction . After 142 h of SSF with substrate concentration of 8% (W/V), ethanol yield of 73.1 % of the theoretical based on glucose in the raw material was obtained by S. cerevisiae(ordinary baker’ yeast) . The corresponding ethanol concentration and volumetric productivity were 17.2g/L and 0.121g/L.h respectively. The estimated total ethanol production was 257.7 kg/ton raw material by assuming consumption of both C-6 and C-5. No obvious inhibition effect occurred during SSF. These instructions give you the basic guidelines for preparing papers for WCICA/IEEE conference proceedings.

Ethanol Production from Sugarcane Bagasse by Zymomonas mobilis Using Simultaneous Saccharification and Fermentation (SSF) Process

2009 ◽  
Vol 161 (1-8) ◽  
pp. 93-105 ◽  
Author(s):  
Danielle da Silveira dos Santos ◽  
Anna Carolina Camelo ◽  
Kelly Cristina Pedro Rodrigues ◽  
Luís Cláudio Carlos ◽  
Nei Pereira
Keyword(s):  
Ethanol Production ◽  
Sugarcane Bagasse ◽  
Zymomonas Mobilis ◽  
Simultaneous Saccharification And Fermentation ◽  
Ssf Process ◽  
Simultaneous Saccharification

scholarly journals Kinetic modeling of simultaneous saccharification and fermentation of corn starch for ethanol production.

2014 ◽  
Vol 61 (1) ◽  
Author(s):  
Wojciech Białas ◽  
Adrian Czerniak ◽  
Daria Szymanowska-Powałowska
Keyword(s):  
Central Composite Design ◽  
Ethanol Production ◽  
Corn Starch ◽  
Simultaneous Saccharification And Fermentation ◽  
Ethanol Yield ◽  
Kinetics Model ◽  
Ssf Process ◽  
Central Composite ◽  
Simultaneous Saccharification ◽  
Granular Starch

Fuel ethanol production, using a simultaneous saccharification and fermentation process (SSF) of native starch from corn flour, has been performed using Saccharomyces cerevisiae and a granular starch hydrolyzing enzyme. The quantitative effects of mash concentration, enzyme dose and pH were investigated with the use of a Box-Wilson central composite design protocol. Proceeding from results obtained in optimal fermentation conditions, a kinetics model relating the utilization rates of starch and glucose as well as the production rates of ethanol and biomass was tested. Moreover, scanning electron microscopy (SEM) was applied to investigate corn starch granule surface after the SFF process. A maximum ethanol concentration of 110.36 g/l was obtained for native corn starch using a mash concentration of 25%, which resulted in ethanol yield of 85.71%. The optimal conditions for the above yield were found with an enzyme dose of 2.05 ml/kg and pH of 5.0. These results indicate that by using a central composite design, it is possible to determine optimal values of the fermentation parameters for maximum ethanol production. The investigated kinetics model can be used to describe SSF process conducted with granular starch hydrolyzing enzymes. The SEM micrographs reveal randomly distributed holes on the surface of granules.

scholarly journals Simultaneous saccharification and co-fermentation with a thermotolerant Saccharomyces cerevisiae to produce ethanol from sugarcane bagasse under high temperature conditions

BioResources ◽  
2021 ◽  
Vol 16 (1) ◽  
pp. 1358-1372
Author(s):  
Wei-Lin Tu ◽  
Tien-Yang Ma ◽  
Chung-Mao Ou ◽  
Gia-Luen Guo ◽  
Yu Chao
Keyword(s):  
Saccharomyces Cerevisiae ◽  
High Temperature ◽  
Ethanol Production ◽  
Sugarcane Bagasse ◽  
Ethanol Yield ◽  
Xylose Utilization ◽  
Inhibitor Tolerance ◽  
Temperature Conditions ◽  
Xylose Uptake ◽  
Simultaneous Saccharification

Lignocellulosic ethanol production at high temperature offers advantages such as the decrease of contamination risk and cooling cost. Recombinant xylose-fermenting Saccharomyces cerevisiae has been considered a promising strain for ethanol production from lignocellulose for its high inhibitor tolerance and superior capability to ferment glucose and xylose into ethanol. To improve the ethanolic fermentation by xylose at high temperature, the strain YY5A was subjected to the ethyl methanesulfonate (EMS) mutagenesis. A mutant strain T5 was selected from the EMS-treated cultures to produce ethanol. However, the xylose uptake by T5 was severely inhibited by the high ethanol concentration during the co-fermentation in defined YPDX medium at 40 °C. In this study, the simultaneous saccharification and co-fermentation (SSCF) and the separate hydrolysis and co-fermentation (SHCF) processes of sugarcane bagasse were assessed to solve this problem. The xylose utilization by T5 was remarkably improved using the SSCF process compared to the SHCF process. For the SHCF and SSCF processes, 48% and 99% of the xylose in the hydrolysate was consumed at 40 °C, respectively. The ethanol yield was enhanced by the SSCF process. The ethanol production can reach to 36.0 g/L using this process under high-temperature conditions.

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