A comparison of pretreatments on release of sugars from sweet sorghum bagasse for bioethanol production

2014 ◽  
Vol 14 (6) ◽  
pp. 522-527 ◽  
Author(s):  
Aditi Banerji ◽  
V. V. N. Kishore ◽  
Malini Balakrishnan
Author(s):  
A B Arif ◽  
A Budiyanto ◽  
W Diyono ◽  
M Hayuningtyas ◽  
T Marwati ◽  
...  

2011 ◽  
Vol 86 (4) ◽  
pp. 1542-1548 ◽  
Author(s):  
Fei Shen ◽  
Jack N. Saddler ◽  
Ronghou Liu ◽  
Lili Lin ◽  
Shihuai Deng ◽  
...  

2011 ◽  
Vol 34 (1) ◽  
pp. 1219-1225 ◽  
Author(s):  
Amir Goshadrou ◽  
Keikhosro Karimi ◽  
Mohammad J. Taherzadeh

Energies ◽  
2020 ◽  
Vol 13 (4) ◽  
pp. 854 ◽  
Author(s):  
Hongshen Li ◽  
Shizhong Li

To improve the efficiency of bioethanol production, an advanced process was required to extract ethanol from solid-state fermented feedstock. With regard to the characteristics of no fluidity of solid biomass, a continuous solid-state distillation (CSSD) column was designed with a proprietary rotary baffle structure and discharging system. To optimize the operation condition, fermented sweet sorghum bagasse was prepared as feedstock for a batch distillation experiment. The whole distillation time was divided into heating and extracting period which was influenced by loading height and steam flow rate simultaneously. A total of 16 experiments at four loading height and four steam flow rate levels were conducted, respectively. Referring to packing, rectifying column, mass, and heat transfer models of the solid-state distillation heating process were established on the basis of analyzing the size distribution of sweet sorghum bagasse. The specific heat capacity and thermal conductivity value of fermented sweet sorghum bagasse were tested and served to calculate the ethanol yielding point and concentration distribution in the packing. The extracting process is described as the ethanol desorption from porous media absorbent and the pseudo-first-order desorption dynamic model was verified by an experiment. Benefit (profit/time) was applied as objective function and solved by successive quadratic programming. The optimal solution of 398 mm loading height and 8.47 m3/h steam flow rate were obtained to guide a 4 m in diameter column design. One heating and two extracting trays with 400 mm effective height were stacked up in an industrial CSSD column. The steam mass flow rate of 0.5 t/h was determined in each tray and further optimized to half the amount on the third tray based on desorption equation.


Author(s):  
Yanni Sudiyani ◽  
Eka Triwahyuni ◽  
Muryanto Muryanto ◽  
Dian Burhani ◽  
Joko Waluyo ◽  
...  

BioResources ◽  
2021 ◽  
Vol 16 (3) ◽  
pp. 5875-5889
Author(s):  
Nissa Nurfajrin Solihat ◽  
Rika Raniya ◽  
Triyani Fajriutami ◽  
Apri Heri Iswanto ◽  
Widya Fatriasari ◽  
...  

Sweet sorghum bagasse (SSB) is potential feedstock for bioethanol production due to its natural abundance and high cellulose content (> 40%). This work compared the impact of three variables relative to the enzymatic hydrolysis of SSB kraft pulp. The three variables were the biosurfactant from lignin derivative known as amphiphilic lignin derivatives (A-LD), the enzyme loading level, and the hydrolysis time. These variables were optimized by response surface methodology (RSM) with a Box-Behnken design (BBD). The concentration of polyethylene glycol (PEG) 4000 was also optimized to compare it with the A-LD performance in the enzymatic hydrolysis process. After optimization, the A-LD produced a higher reducing sugar yield (RSY) (99.45%) than the PEG 4000. The difference in the predicted versus experimental values of the RSY was less than 4%, which means that the model was highly predictive. The adequacy of the model was confirmed by a regression value close to 1 for the A-LD assisted test. The result implies that the A-LD significantly improved the enzymatic hydrolysis performance to enhance the RSY. Moreover, the BBD is adequate and useful to identify the optimum concentration of surfactant.


Fuel ◽  
2016 ◽  
Vol 175 ◽  
pp. 20-25 ◽  
Author(s):  
Menghui Yu ◽  
Jihong Li ◽  
Sandra Chang ◽  
Lei Zhang ◽  
Yueying Mao ◽  
...  

2014 ◽  
Vol 61 ◽  
pp. 1957-1960
Author(s):  
Zhipei Yan ◽  
Jihong Li ◽  
Shizhong Li ◽  
Ting Cui ◽  
Yan Jiang ◽  
...  

2021 ◽  
Vol 11 (1) ◽  
Author(s):  
Neha Arora ◽  
George P. Philippidis

AbstractSupplementing cultivation media with exogenous carbon sources enhances biomass and lipid production in microalgae. Utilization of renewable organic carbon from agricultural residues can potentially reduce the cost of algae cultivation, while enhancing sustainability. In the present investigation a medium was developed from sweet sorghum bagasse for cultivation of Chlorella under mixotrophic conditions. Using response surface methodology, the optimal values of critical process parameters were determined, namely inoculum cell density (O.D.750) of 0.786, SSB hydrolysate content of the medium 25% v/v, and zero medium salinity, to achieve maximum lipid productivity of 120 mg/L/d. Enhanced biomass (3.44 g/L) and lipid content (40% of dry cell weight) were observed when the alga was cultivated in SSB hydrolysate under mixotrophic conditions compared to heterotrophic and photoautotrophic conditions. A time course investigation revealed distinct physiological responses in terms of cellular growth and biochemical composition of C. vulgaris cultivated in the various trophic modes. The determined carbohydrate and lipid profiles indicate that sugar addition to the cultivation medium boosts neutral lipid synthesis compared to structural lipids, suggesting that carbon flux is channeled towards triacylglycerol synthesis in the cells. Furthermore, the fatty acid profile of lipids extracted from mixotrophically grown cultures contained more saturated and monosaturated fatty acids, which are suitable for biofuel manufacturing. Scale-up studies in a photobioreactor using SSB hydrolysate achieved a biomass concentration of 2.83 g/L consisting of 34% lipids and 26% carbohydrates. These results confirmed that SSB hydrolysate is a promising feedstock for mixotrophic cultivation of Chlorella and synthesis of algal bioproducts and biofuels.


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