2015
DOI: 10.1016/j.cherd.2015.06.022
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Stripping of ethanol with CO2 in bubble columns: Effects of operating conditions and modeling

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Cited by 22 publications
(13 citation statements)
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“…This technique has been mainly studied for bio‐fuels extraction, particularly in the acetone–butanol–ethanol (ABE) extractive fermentation, showing high potential in reducing product inhibition and increasing yields 13,77‐81 . Chen et al .…”
Section: In Situ Product Recoverymentioning
confidence: 99%
See 1 more Smart Citation
“…This technique has been mainly studied for bio‐fuels extraction, particularly in the acetone–butanol–ethanol (ABE) extractive fermentation, showing high potential in reducing product inhibition and increasing yields 13,77‐81 . Chen et al .…”
Section: In Situ Product Recoverymentioning
confidence: 99%
“…For instance, the use of oleyl alcohol (OA) coupled with nitrogen gas was explored as an extractive hybrid technique for butanol trapping during batch fermentation of Clostridium acetobutylicum , obtaining a near‐twofold increase for butanol production and glucose comsuption 84 . Some studies have addressed gas stripping using mathematical modeling, suggesting that this strategy could facilitate process design by more accurate behavior and yield prediction under certain parameters and assumptioms 76,77 This modeling strategy brings new opportunities for further optimization not only for this technique but also for the others previously mentioned here. By selecting critical factors and adequate physicochemical parameters, mathematical modeling and surface response could be useful tools for cutting time and costs in bioprocess design.…”
Section: In Situ Product Recoverymentioning
confidence: 99%
“…99.5%~99.8% N 2 was verified to be the preferable type of gas in gas stripping ethanol fermentation (GSEF) where the ethanol and glycerol productivity increased by about two times than that of the control. Besides the nature of the gas, other operating conditions have been reported to affect gas stripping performance, such as feed temperature, stripping gas temperature, specific stripping gas flow rate, and liquid height-to-column diameter ratio (h/D) [50]. Despite its advantages, gas stripping technology has not received significant interest and has only been reported in a limited number of studies summarized in Table 2.…”
Section: Gas Strippingmentioning
confidence: 99%
“…Accumulated ethanol during yeast fermentation is main toxic compound, slowing down yeast growth and ethanol production, resulting therefore in low final ethanol titers of about 8 to 9% (v/v). Semantic quantity of energy for ethanol recovery and large fermentation tanks are required, while also generating large amounts of vinasse (Silva et al, 2015;Sonego et al, 2016). Industrial fed-batch ethanol fermentation starts with 25-30% inoculum, resulting compared to conventional batch mode in a higher ethanol concentration due to reduction of sugar inhibitory effect on S. cerevisiae growth and ethanol production during first stages of fermentation process (Sonego et al, 2016).…”
Section: St Generation Biofuels (Biodiesel Bioethanol Pure Plantmentioning
confidence: 99%
“…Extractive fedbatch fermentation with 2.5 vvm CO2 stripping at 34.0°C has been reported to overcome inhibitory effect of ethanol, wherein ethanol is removed during the fermentation process, resulting in 33% higher ethanol concentration of 110.3 g/L and 9.2 g/(L*h) productivity from 240 g/L substrate (Sonego et al, 2016). Using a 5 liter bubble column fermenter, temperature and entrainment factor were positively affected by the starting temperature and specific flow rate of carbon dioxide, and negatively by the ratio between the height and the diameter (Silva et al, 2015). Taylor et al (1995) described a continuous fermenter/stripper process with heat recovery as a lower-cost alternative to conventional fermentation and distillation, reducing heating and cooling costs.…”
Section: St Generation Biofuels (Biodiesel Bioethanol Pure Plantmentioning
confidence: 99%