Keywords
Bioethanol, Fermentation, Molasses, Optimization, S. cerevisiae, Stress tolerance
This article is included in the Energy gateway.
Yeast strains that are tolerant to several environmental stresses are extensively employed to produce bioethanol from sugar-rich feedstock.
In our previous research findings, five wild indigenous strains of multi-stress tolerance yeast were isolated from traditional fermented alcoholic beverages (Tella, Tej, and Areke) in Ethiopia to the purpose of evaluate their potential use for bioethanol using sugarcane molasses as a substrate.
The optimal parameters for maximum ethanol production were pH of 4.5, 25°Brix, 30°C, 4.0 g/l ammonium sulfate, supplement with yeast extract, and 72 h of incubation period. Under these optimum conditions, 13.13 ± 0.08% (v/v) ethanol was obtained. The yield of hydrous and anhydrous bioethanol from fermented molasses samples were produced at 94.20–95.60% (v/v) and 99.05–99.56% (v/v), respectively.
According to this finding, Saccharomyces cerevisiae isolate MUT15F, Saccharomyces cerevisiae isolate MUT18F, and Saccharomyces cerevisiae isolate R9MU strains have been good candidates for production of industrial bioethanol.
Bioethanol, Fermentation, Molasses, Optimization, S. cerevisiae, Stress tolerance
Due to depleted resources and environmental pollution caused throughout by fossil fuels, it was necessary to find out other eco-friendly renewable and sustainable sources of energy.1 Liquid biofuels, which account for 40% of all energy sources worldwide, were prioritized among renewable energies.2 The use of liquid biofuels helps in the reduction of greenhouse gas emissions, energy security, creation of job opportunities, regional development, rural development and reduction of poverty.3 Bioethanol is a promising alternative energy sources and a popular biofuel for transportation globally since it is a renewable, nontoxic, biodegradable resource and it is oxygenated.4 Production and use of bioethanol for transport fuel have recently attracted significant attention worldwide.5
Starch, cellulose, and sucrose can all be used for the production of bioethanol, which may be found in molasses, coconut, sugar palm, cassava, banana stems, sweet potatoes, sugarcane bagasse, sunflower, woodchips and most recently microalgae.6,7 Among the different substrates available for production bioethanol sugarcane molasses is a good substrate because of cheap raw materials, readily available and compared to starchy or cellulosic materials for industrial bioethanol fermentation, ready for conversion with limited pretreatments.8 Molasses contain minerals, organic acids and high sugar content, which is 34-54%,9 especially the fructose contained in molasses varies between 5-12%, 25% to 40% sucrose, 12–35% reducing sugar and the level of total reduced sugar reaches 50-65%.10 In recent years, sugarcane molasses’ high prospects for making bioethanol have gained major attention from researchers.6,11
Several factors affect the process of fermentation as well as the bioethanol yield such as the production microorganism strain, temperature, pH, oxygen, media composition, fermentation duration and initial concentration of sugar.12 Therefore, it is important to use optimal values among these parameters, for each selected production microorganism, to be able to produce the highest amounts of the required product.13 The choice and development of the efficient bioethanol production of yeast with a resistance multi-stress tolerance are crucial importance.14 Yeasts strain tolerant to high temperature, low pH, osmotic pressure and ethanol are ideal for industrial bioethanol production.15
Ethiopian Sugar Factories Fincha and Metehara used molasses from sugarcane used as a substrate for the production of ethanol after being diluted to 12–15 °Brix. These factories currently yield bioethanol production of less than 7% (v/v), in contrast to other countries that produce bioethanol with yields of 12–14% (v/v). This proves that the effectiveness of Ethiopian Factories is 50% less than the value of factories in other parts of the world. This study may provide significant information regarding potential tolerant of yeast that can withstand many stresses that could serve as a starter culture and substitute for strains of commercial yeast. Therefore, the research objective to maximize production bioethanol from molasses using stress-tolerant yeast strains from household alcoholic beverage preparations (Tella, Tej, and Areke) under different optimal conditions. Five yeast strains were used in this study, specifically Saccharomyces cerevisiae strains with accession numbers from the National Center for Biotechnology Information, such as strains R9MU (OR143320.1), strain R20MU (OR143322.1), strain MUT15F (OR209276.1), strain MUT18F (OR209286.1), and strain R19MU (OR143321.1). These strains of Saccharomyces cerevisiae were obtained in our stock cultures from the previous study because to their noteworthy tolerance to ethanol, 26% (v/v), glucose, 70% (w/v) and temperature, 45°C.
The study was carried out at Department of Biology, University of Gondar, Northwestern Ethiopia. A sample of 70 liter of molasses was acquired from Ethiopia’s Methara Sugar Factory through September to January 2023. The molasses from sugarcane was collected in a clean, durable plastic container and kept at room temperature to the laboratory of microbiology at the University of Gondar for further use (Figure 1).
The physicochemical parameters of sugarcane molasses, including pH, specific gravity, Brix, moisture content, sucrose, and sulfated ash were estimated according to Refs. 16, 17. The quantity of total sugar in molasses samples was determined through Fehling method.18 The reducing sugar concentration in the molasses was determined by the 3,5-dinitrosalicylic acid (DNS) method.19 The moisture content molasses sample was determined thought oven (MB45, OHAUS, Switzerland) drying method. Sucrose content in the molasses sample was measured by measuring optical rotation in a polarimeter. Brix was measured with the help of a refractometer (Atagodensimeter model 2312; Atago Co. Ltd., Tokyo, Japan). Specific gravity of molasses samples were estimated by using baume universal hydrometer. The pH of the molasses samples were determined in the laboratory using pH meter (PHS-3C Digital) at ambient temperature. The ash content was established by muffle furnace at 650°C for 2 hours until constant weight.
2.3.1 Pretreatment of molasses
Distilled water was used to dilute raw molasses (1:1) w/w and pretreated with 99.8% sulfuric acid (H2SO4) until the pH reach 3.5 for the purpose of removing unwanted particles, dirt, and microbial contaminants.20 The mixture was heated to 90°C in a water bath (Gemmy industrial Corp, Taiwan) with continuous mixing for 30 minutes. Then it was allowed to stay for 24 h to cool and decant. The required Brix was achieved through the dilution of raw molasses with distilled water, and the medium was supplemented with 0.7 g/L ammonium sulfate (101217; MilliporeSigma) and then homogenized with a magnetic stirrer. Finally, the pH was adjusted at 4.5 using 0.5 M NaOH and autoclaved at 121°C for 15 min. The yeast strains were propagated and fermentation using the treated media to produce ethanol.
Five native wild strains of Saccharomyces cerevisiae designated as R9MU (OR143320.1), R20MU (OR143322.1), MUT15F (OR209276.1), MUT18F (OR209286.1), and R19MU (OR143321.1) were selected in our stock cultures from the previous study. The capacity of these strains to ferment molasses was assessed, which were previously isolated from homemade alcoholic beverages (Tella, Tej, and Areke). Moreover, they were also selected for their remarkable tolerance because of their multi-stress tolerance yeast strains. The commercial yeast strain was used as a control for comparison with other strains.
A loop full of 48 h old cultures has been taken on YEPD solid media and inoculated into each flask containing 100 ml of treated and sterilized molasses. The flasks were incubated for 24 h at 30°C temperature. Then, to increase the cell number, propagated yeast cultures were transferred to the second stage of propagation in Erlenmeyer flasks of 500 mL containing 100 mL of 30 °Brix molasses medium supplemented with 0.7 g/L ammonium sulfate (101217; MilliporeSigma) and sterilized at 121°C for 15 min and incubated at 30°C for another 24 h. Then after, optical density of propagated cultures was estimated using a UV-Vis spectrometer at 600 nm (Abron ISO 9001:2008) (Table 1). Finally, 48 h of propagated yeast culture which is ready as inoculum was transferred to 800 mL bottles containing 300 mL of sterilized and diluted molasses for optimization of feed-batch molasses fermentation to produce ethanol.21
The fed-batch fermentation system was used to optimize the process parameters, including molasses concentration (15, 20, 25, 30 and 35 °Brix), temperature (25, 30, 35, and 40°C), pH (3.5, 4.0, 4.5, 5.0, and 5.5), ammonium sulfate (101217; MilliporeSigma) supplement (1, 2, 3, 4 and 5 gL-1), different supplementation such as, yeast extract (VWR; 97063-370), urea (Koch Fertilizer, LLC), and ammonium nitrate (EM1.01187.5000; MilliporeSigma), and incubation periods (24, 48, 72, 96, and 120 h) by applying the one variable at a time method (VAT).22 Eight hundred milliliter bottles containing 300 ml of sterilized, diluted molasses were inoculated with 48 h of propagated yeast cells. The inoculum of each yeast strain was prepared by growing it in 200 ml of molasses medium for 48 h at 30°C. The inoculated bottles were plugged with sterilized cotton and incubated for 72 h in an incubator (J.P. Selecta Incubator, Spain). The anaerobic condition was maintained for 3 days. Samples were withdrawn after 72 h and analyzed for ethanol content. All treatments were studied in triplicate, and the mean and standard error were calculated.
2.6.1 Effect of substrate concentration
The yeast strains were grown at varying molasses medium concentrations (15, 20, 25, 30, and 35 °Brix), which is an optimum operating condition at 30°C to investigate the effects of substrate concentration on ethanol production. The pH was adjusted before inoculation to 4.5 for all strains and incubated for 72 h. The concentration of ethanol (v/v %) was determined at the end of the fermentation period for each set of concentrations. At the end of the fermentation time for varied substrate concentrations, the amount of ethanol (v/v %) was measured.
2.6.2 Effect of temperature
Each yeast strain was grown on a molasses medium that was diluted by 30% and incubated at various temperatures (25, 30, 35, and 40°C). All yeast strains were incubated for 72 h at different temperatures, and the initial pH was adjusted to 4.5. The concentration of ethanol (v/v %) was determined at the end of the fermentation period at various temperatures.
2.6.3 Effect of pH
The effect of different pH (3.5, 4.0, 4.5, 5.0, and 5.5) on ethanol production from diluted molasses (30%) by yeast strains was evaluated at 30°C. The pH was adjusted using 1N HCl or 0.1N NaOH. The fermentation process after incubation for 72 h and the percentage of ethanol were measured.
2.6.4 Effect of ammonium sulfate supplement
The effects of supplement concentrations of ammonium sulfate (101217; MilliporeSigma) (1, 2, 3, 4, and 5 g/l) on ethanol production by each yeast strain were determined. All yeast strains were grown on a 30% molasses dilution with an initial pH of 4.0 for 72 h at 30°C. At the end of the fermentation period, the percentage of ethanol concentration for each supplement concentration was measured.
2.6.5 Effect of different supplements
The effects of different supplements such as, yeast extract (VWR; 97063-370), urea (Koch Fertilizer, LLC), and ammonium nitrate (EM1.01187.5000; MilliporeSigma) on ethanol production by each yeast strain were conducted. All yeast strains were grown on a 30% molasses dilution with an initial pH of 4.5 for 72 h at 30°C. The effect of these supplements on ethanol concentration was evaluated after measuring the ethanol content of the fermented broth.
2.6.6 Effect of fermentation period
The yeast strains were cultured on 30% diluted molasses with distilled water and incubated at 30°C for various fermentation times (24, 48, 72, 96, and 120 h). At the end of the fermentation period, the amount of ethanol in each fermentation period was measured as a percentage.
The Brix of fermented samples was measured using a refractometer (Atagodensimeter model 2312; Atago Co. Ltd., Tokyo, Japan). The optical density of propagated cultures was determined using a UV-Vis spectrometer at 600 nm (Abron ISO 9001:2008). The ethanol level of fermented molasses was determined by measurement of specific gravity using a Baume universal hydrometer.23 The levels of ethanol produced from the distillate were measured using an alcoholmeter. The calculation of ethanol concentration (ABV%) and bioethanol yield were calculated according to the Refs. 23 and 24 equation, respectively.
Where ABV is the alcohol by volume (%), SGin is the liquid’s initial specific gravity before to the addition of yeast, and SG is the liquid’s current specific gravity.
Bioethanol production was performed by scaling up the process in 3 L fermenter that each containing 2 L of pretreated molasses at a 30% molasses dilution with an initial pH of 4.5 in anaerobic conditions at 30°C for 72 h. After preparing a loop full of 48-hour-old cultures on YEPD solid media, 500 ml of molasses medium was inoculated for 48 hrs at 30°C. Using a fractional distillation apparatus, bioethanol was extracted from 2.5 L of fermented molasses in 3 L Erlenmeyer flasks.
The distillation flask (Pyrex, 500 ml, England) was filled with 400 ml of the fermented sample and placed on the machine’s heating unit with the water flow connected. The temperature was maintained manually at 78°C (the evaporation temperature of ethanol). The vapor was passed over a fractional column and the bulb of the thermometer, at which point the vapor was determined. The vapor was condensed to a liquid in the horizontal condenser, which was cooled with a flow of cold water. The distillate was collected in a receiver. The distillate was measured for volume. Repeated distillations were carried out until 90% of the bioethanol recovered fulfilled American Standard and Testing Material (ASTM) requirements for fuel.25 Furthermore, the resulting bioethanol was analyzed to determine the yield of the bioethanol. The levels of bioethanol produced from the molasses fermentation and distillation processes were measured using an alcoholmeter.
The initial concentrations of the bioethanol used in the first phase were ranged from 38.70 to 44.62% (v/v). Using a distillation column, the first bioethanol-diluted broth was pre-concentrated to a concentration that was nearly 95% (v/v) of the azeotropic point. During experimentation, samples were frequently taken out, and ethanol content was measured with an alcoholmeter. Near the azeotropic point, a distillate composition of 92.75% w/w was set,26 with a 99.5% w/w recovery of the ethanol feed.
The recovered bioethanol from the pre-concentration process, at a concentration close to 95% (v/v), was used in this study. Dehydrating 3A molecular sieve beads were used in this investigation. Molecular sieve beads were acquired from the Methara Sugar Factory in Ethiopia. The molecular sieves were dried in an oven (MB45, OHAUS, Switzerland) at 190–210°C for 24 h. The dried molecular sieves were kept in bottles, which were then stored in a glass chamber. Samples of distillate were dried using 3A molecular sieves overnight to capture water molecules. After being filtered, decanted, and redistilled to remove sieve dust and achieve anhydrous bioethanol with less than 1% water.27
All Data was analyzed using Statistical Package for Social Sciences software, version 23.0 (IBM SPSSInc., Chicago, IL, SPSS (RRID:SCR_002865), https://www.ibm.com/support/pages/downloading-ibm-spss-statistics-23). Analysis of variance (ANOVA) was conducted to compute the means and standard deviations of the triplicates analysis, and Tukey’s multiple range testing was used to assess if there were any significant differences between the means (p < 0. 05). The statistically significant difference was defined as p < 0. 05.
The process parameters such as molasses concentration (15, 20, 25, 30, and 35 °Brix), temperature (25, 30, 35, and 40°C), pH (3.5, 4.0, 4.5, 5.0, and 5.5), ammonium sulfate supplement (1, 2, 3, 4 and 5 g L-1), different supplementation (yeast extract, urea and ammonium nitrate), and period of incubation (24, 48, 72, 96, and 120 h) were all optimized using fed-batch fermentation (Figure 2). In fed-batch fermentation using a 200 ml treated molasses sample as the inoculum, yeast cell propagation was accomplished with a cell count of 1.710 – 1.892 × 108 cells per ml after 48 h (Table 1).
The physicochemical parameters of sugarcane molasses from the Methara Sugar Factory in Ethiopia are presented in Table 2. Molasses was composed of 84.00 ± 1.53° Brix, 50.35 ± 0.12% total reducing sugars, 33.31 ± 1.94% sucrose, 14.32 ± 0.65% reduced sugars, 19.30 ± 0.26% water content, and 17.01 ± 0.69% sulfated ash (w/v). Moreover, the molasses pH was 5.72 ± 0.09.
As shown in Table 3, various molasses percentages (Brix of 15%, 20%, 25%, 30%, and 35%) were utilized in fed batch fermentation to examine the optimization of ethanol concentration at 30°C and a pH of 4.5. Based on the present study, the five yeast strains from molasses with a Brix of 15–35 (oB) were produced ethanol in amounts ranging from 7.80 to 12.47% (v/v) of the concentration of ethanol. The standard industrial yeast strain was used as a control for comparison with other strains. Saccharomyces cerevisiae isolate MUT15F, 12.47 ± 0.07% (v/v) and Saccharomyces cerevisiae isolate R9MU, 11.81 ± 0.16% (v/v) have been shown statistically (p ≤ 0.05) greater ethanol concentrations than the remaining strains. Production of ethanol in all yeast strains was significantly (p ≤ 0.05) reduced in either low concentration (15–20%) or high concentration (30–35%). Higher or lower concentrations of molasses have a significant negative effect on ethanol production. These findings have been shown that the optimal molasses concentration for all yeast strains to produce ethanol was 25% (Table 3).
The effect of temperature at 25, 30, 35, and 40°C in the production process of ethanol was also investigated. The ethanol production maximum was shown in Table 3 to be achieved at a temperature of 30°C, and subsequent increases in temperature reduced the production of ethanol. According to this finding, Saccharomyces cerevisiae isolate MUT15F, 11.94 ± 0.06% (v/v) and Saccharomyces cerevisiae isolate R9MU, 11.15 ± 0.08% (v/v) were statistically (p ≤ 0.05) greater in ethanol concentration than the other strains, which was included strain MT (the commercial strains) at 30°C after 72 h of the fermentation period. Saccharomyces cerevisiae isolate MUT18F has been shown a statistically lower (p ≤ 0.05) amount of ethanol, 9.84 ± 0.16% (v/v) at 30°C than the other yeast strains. There was no statistically significant (p ≥ 0.05) difference between strains of Saccharomyces cerevisiae R19MU, Saccharomyces cerevisiae R20MU, and MT (standard) at 30°C. Below 25°C or above 30°C, the production of ethanol by all yeast strains was significantly (p ≤ 0.05) reduced. According to this finding, the optimum incubation temperature for all yeast strains was 30°C.
The results of different ethanol productions with pH values ranging from 3.5 to 5.5 were shown in Table 3. The ethanol production gradually increases along with the increase in pH and reaches a maximum at a pH 4.5. The production was decreased slightly for pH values higher than 5. The yeast strains have been shown a different pattern of ethanol production of 6.08–11.94% (v/v) from pH 3.5 to pH 5.5. Based on the present study, ethanol produced by yeast strain Saccharomyces cerevisiae isolate MUT15F, 11.94 ± 0.06% (v/v) and Saccharomyces cerevisiae isolate R9MU, 11.15 ± 0.08% (v/v) were shown a statistically significant (p ≤ 0.05) greater concentration than all the remaining strains at pH 4.5. Saccharomyces cerevisiae isolate R20MU has been shown statistically (p ≤ 0.05) lower ethanol concentration than all other strains. There was no statistically significant (p ≥ 0.05) difference between strains Saccharomyces cerevisiae isolate R19MU, Saccharomyces cerevisiae isolate R20MU, and the MT (standard) at pH 4.5. All the strains were more effective to produce high amount of ethanol at pH 4.5 and less ethanol produced at pH 3.5 (Table 3).
In Table 4, the effect of ammonium sulfate as a nitrogen source is shown. Under optimal conditions, 4.0 g/l of ammonium sulfate produced the highest amount of ethanol. As the ammonium sulfate concentration increased from 1.0 to 4.0 g/l, the production ethanol also significantly (p ≤ 0.05) increased and then reduced in amount as concentration of ammonium sulfate increased. In this study, the amount of ethanol production by Saccharomyces cerevisiae isolate MUT15F was increased from 11.95 ± 0.1 to 13.13 ± 0.08% (v/v) between 1.0 and 4.0 g/l ammonium sulfate. According to this finding, Saccharomyces cerevisiae isolate MUT15F (13.13 ± 0.08% (v/v) has been shown statistically (p ≤ 0.05) greater ethanol production than that of the other strains including strain MT (the commercial strains). Saccharomyces cerevisiae isolate MUT18F was shown significantly (p ≥ 0.05) less ethanol concentration, (10.76 ± 0.03% (v/v)) at 4.0 g/l ammonium sulfate than all other strains.
Ammonium nitrate, urea, and yeast extract are different nitrogen sources and their effects were studied at a concentration of 1 g supplementation per liter, as presented in Table 4. Yeast extract supplement was produced high levels of ethanol when in contrast to other nitrogen sources and the control. Compared to the other supplemented media, an ammonium nitrate-supplemented medium was shown the lowest level of ethanol. Saccharomyces cerevisiae isolate MUT15F (12.24 ± 0.08% (v/v)) and Saccharomyces cerevisiae isolate R9MU (11.60 ± 0.06% (v/v)) were statistically (p ≤ 0.05) greater in ethanol production from yeast extract supplementation than stains MT (the commercial strains) (10.89 ± 0.12% (v/v)) and Saccharomyces cerevisiae isolate R19MU (10.83 ± 0.02% (v)). The lowest ethanol concentration was observed (10.43 ± 0.12% (v/v)) by strains Saccharomyces cerevisiae isolate R20MU and Saccharomyces cerevisiae isolate MUT18F (9.95 ± 0.09% v/v) from supplementation of yeast extract compared to the rest of the yeast strains. The maximum ethanol concentration was observed (11.95 ± 0.1% (v/v)) by Saccharomyces cerevisiae isolate MUT15F and Saccharomyces cerevisiae isolate R9MU (11.17 ± 0.08% (v/v)) from the supplementation of urea than the rest of the yeast strains. All yeast strains grown without nitrogen sources (control) had the lowest ethanol concentration in comparison to other supplemented media in this study.
Incubation periods effect on ethanol production after fermentation processes were carried out for 24, 48, 72, 96, and 120 h is presented in Table 4. Ethanol production was increased during incubation periods up to 72 h and then decreased again to reach the minimum levels at 120 h of incubation. After 72 h of fermentation, the maximum amount of ethanol was produced. Therefore, the optimum period of incubation to produce ethanol was 72 h except for yeast strains Saccharomyces cerevisiae isolate MUT15F (12.02 ± 0.13% (v/v)) and Saccharomyces cerevisiae isolate R19MU (10.77 ± 0.04% (v/v)), which achieved their maximum production after 96 h. Saccharomyces cerevisiae isolate R9MU (11.15 ± 0.08% (v/v)) was shown statistically (P ≤ 0.05) higher ethanol production.
The yield of anhydrous and hydrous bioethanol generated from molasses sample is shown in Table 5. A continuous distillation was utilized to accomplish fractional distillation on each sample of fermented molasses, yielding various distillate quantities and hydrous bioethanol (Figure 3). After pre-concentration, the distillation column concentrates hydrous bioethanol up to a final concentration of 94.20–95.60% (v/v) was determined using an alcoholmeter. The volume of bioethanol produced using different yeast strains in molasses samples varied significantly (p ≤ 0.05). Anhydrous bioethanol of 99.05–99.56% (v/v) was achieved by further distillation employing a 3A molecular sieve bead (Figure 4). Saccharomyces cerevisiae isolate R9MU has been shown the highest anhydrous bioethanol concentration (99.56% (v/v)) after dehydration, while Saccharomyces cerevisiae isolate MUT18F produced the least amount of anhydrous bioethanol (99.05% (v/v)) as shown in Table 5. The maximum yield of bioethanol (8.50% v/v) was produced by S. cerevisiae isolate R9MU. All the bioethanol produced was clear and colorless.
Different molasses concentrations were used to determine their effect on the ethanol concentration using the optimized pH of 4.5. The finding indicated that 25 °Brix was the most suitable sugar concentration for isolate of Saccharomyces cerevisiae MUT15F and Saccharomyces cerevisiae R9MU to produce ethanol concentrations of 12.47 ± 0.07% (v/v) and 11.81 ± 0.16% (v/v) at 72 h, respectively. The ethanol concentration in this study was higher than the findings of other authors.28,29 However, Gu et al.30 used yunnan molasses and recorded that the highest production of ethanol was 16% (v/v) by strain 1912 and 13.7% (v/v) by strain 1190 at 30% molasses sugar for 72 h. Muruaga et al.31 also reported that for the A10 strain isolated from molasses at 250 g/L of initial sugar, the highest level of ethanol production was 13.20% (v/v). The production of ethanol by all yeasts significantly decreased at high molasses concentrations (35%). This may be because to the high quantities of substrates being inhibitory to the fermentation process of yeasts due to osmotic stress.
Temperature is the key factor that affects the growth, metabolism, and ethanol production capability of the fermenting organisms. During this investigation, ethanol production by all yeast strains increased with the increase in temperature, reaching its maximum value at 30°C. This finding is in line with the findings of.32,33 Below 25°C or above 30°C, the production of ethanol by all yeast strains was significantly reduced. This might be due to the fact that denaturation happens at high temperatures and reduced enzyme activity at low temperatures.
Optimal pH values are essential for the activity of plasma membrane-based proteins, including enzymes and transport proteins.34 Based on the present finding, the production of ethanol gradually increased along with the increase in pH and reached a maximum production for a pH equal to 4.5, then started to decline. An optimum pH of S. cerevisiae was obtained at pH 4.5. This is line with the report of other investigators.33,35,36 In contrast to this investigation, Ercan et al.37 found that optimum ethanol production using S. cerevisiae was obtained at pH 5.5. The most favorable pH of S. cerevisiae for ethanol production ranges from 4.0 to 5.0.27
Nitrogen limitation has been shown to affect cell growth and biomass formation as well as directly affect the fermentation rate.38 Although most of the nutrients needed for yeast development are present in molasses, sufficient nitrogen is frequently added to promote yeast growth and the production of ethanol.39 Numerous investigations were conducted in previous years to optimize supplies of nitrogen and other supplements.40 The obtained data revealed that the addition of ammonium sulfate to the fermentation medium also increased ethanol production from 1.0 to 4.0 g/l. In the present finding, the amount of ethanol production by Saccharomyces cerevisiae isolate MUT15F increased from 11.95 ± 0.1 to 13.13 ± 0.08% (v/v) between 1.0 and 4.0 g/L ammonium sulfate. Our study agrees with previous studies by Ref. 41 the optimal medium for S. cerevisiae to produce ethanol was 4 g/L of ammonium sulfate with 10% (v/v) ethanol content. Anupama et al.42 was reported that the usage of ammonium sulfate at a concentration of 3 g/l resulted in an optimal 5.6% yield of ethanol.
Nutrients are quite effective in the production of ethanol from sugar cane molasses.22 Different nitrogen sources (yeast extract, urea, and ammonium nitrate) were investigated as possible nitrogen supplements for sugar cane molasses. This study revealed that all nitrogen sources investigated had a positive effect on the production of ethanol. The maximum ethanol production was recoreded as nitrogen source yeast extract from Saccharomyces cerevisiae isolate MUT15F (12.24 ± 0.08% (v/v)) and Saccharomyces cerevisiae isolate R9MU (11.60 ± 0.06% (v/v)). These results were in agreement with Rasmey et al.,35 who found that yeast extract addition significantly improved the ethanol concentration. In this finding, yeast extract provides convenient growth factors for yeast growth and it is in line with Ortiz-Muñiz et al.43 report. On the other hand, it was also detected that ammonium sulfate was a good nitrogen source that stimulated ethanol production from sugar cane molasses. An effective and common source of nitrogen for yeast development is ammonium sulfate; it is cheap and has been chosen for future experiments.39
Controlling a number of variables can result in increased ethanol fermentation activity. Temperature, pH, substrate concentration, and fermentation time also greatly influences ethanol production by yeasts.12,44 According to this finding, ethanol concentration was reaching its maximum amount after 72 h except for Saccharomyces cerevisiae isolate MUT15F (12.02 ± 0.13% (v/v)) and Saccharomyces cerevisiae isolate R19MU (10.77 ± 0.04% (v/v)), which achieved their maximum production after 96 hrs. After three days of growth, it was determined that yeasts produce the highest amounts of ethanol by fermenting sugary substrates with actively growing yeast cells.45 Ethanol production increased gradually, but a slight decrease in ethanol concentration with an increasing incubation period could be due to the loss of yeast cell viability and consumption of it by the yeast cells as time passed.46 The current findings showed that optimization of temperature, pH, incubation duration, and substrate concentration is quite important for the maximization of ethanol production, as previously reported by other studies.47,48
The result of our study indicated that hydrous bioethanol was concentrated in the distillation column to a final concentration of 94.20–95.60% (v/v). Further distillation using a 3A molecular sieve bead resulted in anhydrous bioethanol of about 99.05-99.56% (v/v). The highest anhydrous bioethanol concentration was obtained from Saccharomyces cerevisiae isolate R9MU (99.56% (v/v)) after distillation and dehydration. These results were in agreement with Yang et al.,49 who produced bioethanol in the form of hydrous ethanol (96% v/v).
Saccharomyces cerevisiae isolate MUT15F yielded a maximum ethanol production of 13.13 ± 0.08% (v/v) at 30 °Brix of molasses, 30°C, 4g NH4SO4, 4.5 pH, and 72 h fermentation. In contrast to unoptimized conditions, the concentration of ethanol increased approximately by 77.4% after optimization. The candidate yeast strains designated as Saccharomyces cerevisiae isolate MUT15F, Saccharomyces cerevisiae isolate R9MU, and Saccharomyces cerevisiae isolate MUT18F were producing maximum alcohol under the optimized fermentation conditions and have the potential to be used for industrial bioethanol production. Saccharomyces cerevisiae isolate R9MU produced the highest bioethanol yield (8.50% v/v). Traditional alcoholic beverages such as Tella, Tej, and Areke can serves as a potential yeast source that able to produce high concentration of bioethanol.
Conceptualization, M.F. and B.A.; Methodology, M.F.; Data analysis, M.F.; Investigation, M.F.; Resources, M.F.; Writing – original draft, M.F.; Writing – review & editing, M.F. and B.A.; Visualization, M.F.; Supervision, B.A.; Funding acquisition, M.F. All authors have read and agreed to the published version of the manuscript.
Figshare: Molasses concentration (15, 20, 25, 30 and 35 °Brix), and pH (3.5, 4.0, 4.5, 5.0, and 5.5) of data analysis. https://doi.org/10.6084/m9.figshare.24941358. 50
This project contains the following underlying data:
- Molasses concentration (15, 20, 25, 30 and 35 °Brix), and pH (3.5, 4.0, 4.5, 5.0, and 5.5) of data analysis.
- SPSS data analysis of supplements, and period of incubation (24, 48, 72, 96, and 120 h).
Data are available under the terms of the Creative Commons Attribution 4.0 International license (CC-BY 4.0).
We want to express our gratitude to Methara Sugar Factory for support molecular sieves and molasses.
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Partly
Are sufficient details of methods and analysis provided to allow replication by others?
Yes
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Competing Interests: No competing interests were disclosed.
Reviewer Expertise: biotechnology, plant biotechnology
Is the work clearly and accurately presented and does it cite the current literature?
No
Is the study design appropriate and is the work technically sound?
No
Are sufficient details of methods and analysis provided to allow replication by others?
No
If applicable, is the statistical analysis and its interpretation appropriate?
Yes
Are all the source data underlying the results available to ensure full reproducibility?
No source data required
Are the conclusions drawn adequately supported by the results?
No
Competing Interests: No competing interests were disclosed.
Reviewer Expertise: Fuel ethanol production
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You registered with F1000 via Google, so we cannot reset your password.
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If you still need help with your Google account password, please click here.
You registered with F1000 via Facebook, so we cannot reset your password.
To sign in, please click here.
If you still need help with your Facebook account password, please click here.
If your email address is registered with us, we will email you instructions to reset your password.
If you think you should have received this email but it has not arrived, please check your spam filters and/or contact for further assistance.
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