Bioethanol production from Gracilaria verrucosa using Saccharomyces cerevisiae adapted to NaCl or galactose

This study examined the pretreatment, enzymatic saccharification, and fermentation of the red macroalgae Gracilaria verrucosa using adapted saccharomyces cerevisiae to galactose or NaCl for the increase of bioethanol yield. Pretreatment with thermal acid hydrolysis to obtain galactose was carried out with 11.7% (w/v) seaweed slurry and 373 mM H₂SO₄ at 121 °C for 59 min. Glucose was obtained from enzymatic hydrolysis. Enzymatic saccharification was performed with a mixture of 16 U/mL Celluclast 1.5L and Viscozyme L at 45 °C for 48 h. Ethanol fermentation in 11.7% (w/v) seaweed hydrolysate was carried out using Saccharomyces cerevisiae KCTC 1126 adapted or non-adapted to high concentrations of galactose or NaCl. When non-adapted S. cerevisiae KCTC 1126 was used, the ethanol productivity was 0.09 g/(Lh) with an ethanol yield of 0.25. Ethanol productivity of 0.16 and 0.19 g/(Lh) with ethanol yields of 0.43 and 0.48 was obtained using S. cerevisiae KCTC 1126 adapted to high concentrations of galactose and NaCl, respectively. Adaptation of S. cerevisiae KCTC 1126 to galactose or NaCl increased the ethanol yield via adaptive evolution of the yeast.

     

Optimization of saccharification and ethanol production by simultaneous saccharification and fermentation (SSF) from seaweed, Saccharina japonica

Ethanol was produced using the simultaneous saccharification and fermentation (SSF) method with macroalgae polysaccharide from the seaweed Saccharina japonica (Sea tangle, Dasima) as biomass. The seaweed was dried by hot air, ground with a hammer mill and filtered with a 200-mesh sieve prior to pretreatment. Saccharification was carried out by thermal acid hydrolysis with H(2)SO(4) and the industrial enzyme, Termamyl 120 L. To increase the yield of saccharification, isolated marine bacteria were used; the optimal saccharification conditions were 10% (w/v) seaweed slurry, 40 mM H(2)SO(4) and 1 g dcw/L isolated Bacillus sp. JS-1. Using this saccharification procedure, the reducing sugar concentration and viscosity were 45.6 ± 5.0 g/L and 24.9 cp, respectively, and the total yield of the saccharification with optimal conditions and S. japonica was 69.1%. Simultaneous saccharification and fermentation was carried out for ethanol production. The highest ethanol concentration, 7.7 g/L (9.8 ml/L) with a theoretical yield of 33.3%, was obtained by SSF with 0.39 g dcw/L Bacillus sp. JS-1 and 0.45 g dcw/L of the yeast, Pichia angophorae KCTC 17574.     

Bioethanol production from brown seaweed, Undaria pinnatifida, using NaCl acclimated yeast

Strain improvement of Pichia angophorae KCTC 17574 was successfully carried out for bioethanol fermentation of seaweed slurry with high salt concentration. P. angophorae KCTC 17574 was cultured under increasing salinity from five practical salinity unit (psu, ‰) to as high as 100 psu for 723 h. The seaweed, Undaria pinnatifida (sea mustard, Miyuk), was fermented to produce bioethanol using high-salt acclimated yeast. The pretreatment of U. pinnatifida was optimized using thermal acid hydrolysis to obtain a high monosaccharide yield. Optimal pretreatment conditions of 75 mM H₂SO₄ and 13 % (w/v) slurry at 121 °C for 60 min were determined using response surface methodology. A maximum monosaccharide content of 28.65 g/L and the viscosity of 33.19 cP were obtained. The yeasts cultured under various salinity concentrations were collected and inoculated to the pretreated seaweed slurry after the neutralization using 5 N NaOH. The pretreated slurry was fermented with the inoculation of 0.1 g dcw/L of P. angophorae KCTC 17574 strain obtained at 90 psu. The maximum ethanol concentration of 9.42 g/L with 27 % yield of theoretical case of ethanol production from total carbohydrate of U. pinnatifida was obtained.     

Ethanol production from seaweed (Undaria pinnatifida) using yeast acclimated to specific sugars

Ethanol production from Undaria pinnatifida (Sea mustard, Miyuk) was performed using yeast acclimated to specific sugars. Pretreatment conditions were optimized by thermal acid hydrolysis and enzyme treatment to increase the monosaccharide yield. Pretreatment by thermal acid hydrolysis was carried out using seaweed powder at 8 ～ 17% (w/v) solid content with a treatment time of 30 ～ 60 min. Enzyme treatment was carried out with 1% (v/v) Viscozyme L (1.2 FGU/mL), 1% (v/v) Celluclast 1.5 L (8.5 EGU/mL), 1% (v/v) AMG 300 L (3.0 AGU/mL), and 1% (v/v) Termamyl 120 L (0.72 KNU/mL). All enzymes except Termamyl 120 L, which was applied during pretreatment, were treated at 45°C for 24 h following pretreatment. Optimal pretreatment and enzyme conditions were determined to be 75 mM H₂SO₄, 13% (w/v) slurry, and 2.88 KNU/mL Termamyl 120 L at 121°C for 60 min. A maximum monosaccharide concentration of 33.1 g/L with 50.1% theoretical yield was obtained. To increase the ethanol yield, Pichia angophorae KCTC 17574 was acclimated to a high concentration (120 g/L) of galactose and mannitol at 30oC for 24 h. Ethanol production of 12.98 g/L with 40.12% theoretical yield was obtained from U. pinnatifida through fermentation with 0.35 g dry cell weight/L P. angophorae KCTC 17574 acclimated to mannitol and galactose.     

Butanol and butyric acid production from Saccharina japonica by Clostridium acetobutylicum and Clostridium tyrobutyricum with adaptive evolution

Optimal conditions of hyper thermal (HT) acid hydrolysis of the Saccharina japonica was determined to a seaweed slurry content of 12% (w/v) and 144 mM H₂SO₄ at 160 °C for 10 min. Enzymatic saccharification was carried out at 50 °C and 150 rpm for 48 h using the three enzymes at concentrations of 16 U/mL. Celluclast 1.5 L showed the lowest half-velocity constant (K_m) of 0.168 g/L, indicating a higher affinity for S. japonica hydrolysate. Pretreatment yielded a maximum monosaccharide concentration of 36.2 g/L and 45.7% conversion from total fermentable monosaccharides of 79.2 g/L with 120 g dry weight/L S. japonica slurry. High cell densities of Clostridium acetobutylicum and Clostridium tyrobutyricum were obtained using the retarding agents KH₂PO₄ (50 mM) and NaHCO₃ (200 mM). Adaptive evolution facilitated the efficient use of mixed monosaccharides. Therefore, adaptive evolution and retarding agents can enhance the overall butanol and butyric acid yields from S. japonica.

     

Effect of dilute acid pretreatment on the saccharification and fermentation of rye straw

This research shows the effect of dilute acid pretreatment with various sulfuric acid concentrations (0.5–2.0% [wt/vol]) on enzymatic saccharification and fermentation yield of rye straw. After pretreatment, solids of rye straw were suspended in Na citrate buffer or post-pretreatment liquids (prehydrolysates) containing sugars liberated after hemicellulose hydrolysis. Saccharification was conducted using enzymes dosage of 15 or 25 FPU/g cellulose. Cellulose saccharification rate after rye straw pretreatment was enhanced by performing enzymatic hydrolysis in sodium citrate buffer in comparison with hemicellulose prehydrolysate. The maximum cellulose saccharification rate (69%) was reached in sodium citrate buffer (biomass pretreated with 2.0% [wt/vol] H₂SO₄). Lignocellulosic complex of rye straw after pretreatment was subjected to separate hydrolysis and fermentation (SHF) or separate hydrolysis and co-fermentation (SHCF). The SHF processes conducted in the sodium citrate buffer using monoculture of Saccharomyces cerevisiae (Ethanol Red) were more efficient compared to hemicellulose prehydrolysate in respect with ethanol yields. Maximum fermentation efficiency of SHF processes obtained after rye straw pretreatment at 1.5% [wt/vol] H₂SO₄ and saccharification using enzymes dosage of 25 FPU/g in sodium citrate buffer, achieving 40.6% of theoretical yield. However, SHCF process using cocultures of pentose-fermenting yeast, after pretreatment of raw material at 1.5% [wt/vol] H₂SO₄ and hydrolysis using enzymes dosage of 25 FPU/g, resulted in the highest ethanol yield among studied methods, achieving 9.4 g/L of ethanol, corresponding to 55% of theoretical yield.     

Production of bio-fuel ethanol from distilled grain waste eluted from Chinese spirit making process

Distilled grain waste eluted from Chinese spirit making is rich in carbohydrates, and could potentially serve as feedstock for the production of bio-fuel ethanol. Our study evaluated two types of saccharification methods that convert distilled grain waste to monosaccharides: enzymatic saccharification and concentrated H₂SO₄ saccharification. Results showed that enzymatic saccharification performed unsatisfactorily because of inefficient removal of lignin during pretreatment. Concentrated H₂SO₄ saccharification led to a total sugar recovery efficiency of 79.0 %, and to considerably higher sugar concentrations than enzymatic saccharification. The process of ethanol production from distilled grain waste based on concentrated H₂SO₄ saccharification was then studied. The process mainly consisted of concentrated H₂SO₄ saccharification, solid–liquid separation, decoloration, sugar–acid separation, oligosaccharide hydrolysis, and continuous ethanol fermentation. An improved simulated moving bed system was employed to separate sugars from acid after concentrated H₂SO₄ saccharification, by which 95.8 % of glucose and 85.8 % of xylose went into the sugar-rich fraction, while 83.3 % of H₂SO₄ went into the acid-rich fraction. A flocculating yeast strain, Saccharomyces cerevisiae KF-7, was used for continuous ethanol fermentation, which produced an ethanol yield of 91.9–98.9 %, based on glucose concentration.     

Optimization of pretreatment and saccharification for the production of bioethanol from water hyacinth by Saccharomyces cerevisiae

Alkaline-oxidative (A/O) pretreatment and enzymatic saccharification were optimized for bioethanol fermentation from water hyacinth by Saccharomyces cerevisiae. Water hyacinth was subjected to A/O pretreatment at various NaOH and H(2)O(2) concentrations and reaction temperatures for the optimization of bioethanol fermentation by S. cerevisiae. The most effective condition for A/O pretreatment was 7% (w/v) NaOH at 100 °C and 2% (w/v) H(2)O(2). The carbohydrate content was analyzed after reaction at various enzyme concentrations and enzyme ratios using Celluclast 1.5 L and Viscozyme L to determine the effective conditions for enzymatic saccharification. After ethanol fermentation using S. cerevisiae KCTC 7928, the concentration of glucose, ethanol and glycerol was analyzed by HPLC using a RI detector. The yield of ethanol in batch fermentation was 0.35 g ethanol/g biomass. Continuous fermentation was carried out at a dilution rate of 0.11 (per h) and the ethanol productivity was 0.77 [g/(l h)].     

Selection and characterization of a newly isolated thermotolerant Pichia kudriavzevii strain for ethanol production at high temperature from cassava starch hydrolysate

Pichia kudriavzevii DMKU 3-ET15 was isolated from traditional fermented pork sausage by an enrichment technique in a yeast extract peptone dextrose (YPD) broth, supplemented with 4 % (v/v) ethanol at 40 °C and selected based on its ethanol fermentation ability at 40 °C in YPD broth composed of 16 % glucose, and in a cassava starch hydrolysate medium composed of cassava starch hydrolysate adjusted to 16 % glucose. The strain produced ethanol from cassava starch hydrolysate at a high temperature up to 45 °C, but the optimal temperature for ethanol production was at 40 °C. Ethanol production by this strain using shaking flask cultivation was the highest in a medium containing cassava starch hydrolysate adjusted to 18 % glucose, 0.05 % (NH₄)₂SO₄, 0.09 % yeast extract, 0.05 % KH₂PO₄, and 0.05 % MgSO₄·7H₂O, with a pH of 5.0 at 40 °C. The highest ethanol concentration reached 7.86 % (w/v) after 24 h, with productivity of 3.28 g/l/h and yield of 85.4 % of the theoretical yield. At 42 °C, ethanol production by this strain became slightly lower, while at 45 °C only 3.82 % (w/v) of ethanol, 1.27 g/l/h productivity and 41.5 % of the theoretical yield were attained. In a study on ethanol production in a 2.5-l jar fermenter with an agitation speed of 300 rpm and an aeration rate of 0.1 vvm throughout the fermentation, P. kudriavzevii DMKU 3-ET15 yielded a final ethanol concentration of 7.35 % (w/v) after 33 h, a productivity of 2.23 g/l/h and a yield of 79.9 % of the theoretical yield.     

Simultaneous saccharification and ethanol fermentation of sago starch using immobilized Zymomonas mobilis

Simultaneous saccharification and ethanol fermentation (SSF) of sago starch using amyloglucosidase (AMG) and immobilized Zymomonas mobilis ZM4 on sodium alginate was studied. The immobilized Zymomonas cells were more thermo-stable than free Zymomonas cells in this system. The optimum temperature in the SSF system was 40°C, and 0.5% (v/w) AMG concentration was adopted for the economical operation of the system. The final ethanol concentration obtained was 68.3 g/l and the ethanol yield, Y_p/s, was 0.49 g/g (96% of the theoretical yield). After 6 cycles of reuse at 40°C with 15% sago starch hydrolysate, the immobilized Z. mobilis retained about 50% of its ethanol fermenting ability.     

The effect of biomass moisture content on bioethanol yields from steam pretreated switchgrass and sugarcane bagasse

This study aimed to determine the effect of moisture content of three different feedstocks on overall ethanol yield. Switchgrass and sugarcane bagasse from two sources were either soaked in water (∼80% moisture) or left dry (∼12% moisture), and half each of these were impregnated with 3% w/w SO₂ and all were steam pretreated. The twelve resulting substrates were compared based on overall sugar recovery after pretreatment, cellulose conversion following enzymatic hydrolysis, and ethanol yield following simultaneous saccharification and fermentation. The overall ethanol yield after simultaneous saccharification and fermentation of hexoses was 18-28% higher in samples that were soaked prior to SO₂ addition than in SO₂-catalyzed samples that were not soaked. In samples that were uncatalyzed, soaking made little difference, indicating that the positive effect of increased moisture content may be related to increased permeability of the biomass to SO₂.     

Butyric acid production from brown algae using <Emphasis Type="Italic">Clostridium tyrobutyricum</Emphasis> ATCC 25755

Butyric acid fermentation by Clostridium tyrobutyricum ATCC 25755 using glucose or brown algae as a carbon source was carried out. Initially, different fermentation modes (batch, fed-batch, and semi-continuous) at pH 6 and 37°C were compared using a model medium containing glucose as a carbon source. By feeding the whole medium containing 40 ∼ 50 and 30 g/L of glucose into the fed-batch and semi-continuous fermentations, very similar butyrate yields (0.274 and 0.252 g butyrate/g glucose, respectively) and productivities (0.362 and 0.355 g/L/h, respectively) were achieved. The highest butyrate concentration was about 50 g/L, which was observed in the fed-batch fermentation with whole medium feeding. However, semi-continuous fermentation sustained a longer fermentation cycle than the fed-batch fermentation due to end-product and metabolic waste inhibition. The established conditions were then applied to the fermentation using brown algae, Laminaria japonica and Undaria pinnatifida, as substrates for butyric acid fermentation. To hydrolyze brown algae, 7.5 ∼ 10% (w/v) dried brown algae powder was suspended in 1% (w/v) NaOH or 0.5 ∼ 2.5% (w/v) H₂SO₄ and then autoclaved at 121°C for 30 ∼ 90 min. The resulting butyrate concentration was about 11 g/L, which was produced from 100 g/L of L. japonica autoclaved for 60 min in 1.5% H₂SO₄ acid solution.     

Fermentation of paddy malt mash to ethanol by mixed cultures of Saccharomyces cerevisiae and Zymomonas mobilis ZM4 with penicillin G

Traditional fermentation of paddy malt mash (containing 18.1% w/v dextrose equivalent) to paddy arrack using paddy husk as source of inoculum yielded very low level of ethanol (4.25% v/v). Use of yeast isolates obtained from paddy husk as well as a potent ethanol producer like Zymomonas mobilis ZM4 and their combinations in the fermentation revealed that a combination of an yeast isolate PH 03 (Saccharomyces cerevisiae) and Z. mobilis ZM4 produced synergistically and statistically more ethanol (10.1% v/v) than the individual and other combination of cultures. In this process, addition of penicillin G at a concentration of 20 U/ml rather than heat sterilization, helped retention of the limited amylase activity in the mash for simultaneous saccharification and fermentation over 7 d at 30°C. About 98.5% of the carbohydrate was accountable in the fermentation which yielded 86.7% of the theoretical yield of ethanol, apart from biomass and acids.     

Fermentation of Detoxified Acid-Hydrolyzed Pyrolytic Anhydrosugars into Bioethanol with <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> 2.399

Pyrolysate obtained from the pyrolysis of waste cotton is a source of fermentable sugars that could be fermented into bioethanol fuel and other chemicals via microbial fermentation. However, pyrolysate is a complex mixture of fermentable and non-fermentable substrates causing inhibition of the microbial growth. The aim of this study was to detoxify the hydrolysate and then ferment it into bio-ethanol fuel in shake flasks and fermenter applying yeast strain Saccharomyces cerevisiae 2.399. Pyrolysate was hydrolyzed to glucose with 0.2 M sulfuric acid, neutralized with Ba(OH)₂ followed by treatment with ethyl acetate and activated carbon to remove fermentation inhibitors. The effect of various fermentation parameters such as inoculum concentration, pH and hydrolysate glucose was evaluated in shake flasks for optimum ethanol fermentation. With respect to inoculum concentration, 20% v/v inoculum i.e. 8.0 × 10⁸–1.2 × 10⁹ cells/mL was the optimum level for producing 8.62 ± 0.33 g/L ethanol at 9 h of fermentation with a maximum yield of 0.46 g ethanol/g glucose. The optimum pH for hydrolysate glucose fermentation was found to be 6.0 that produced 8.57 ± 0.66 g/L ethanol. Maximum ethanol concentration, 14.78 g/L was obtained for 4% hydrolysate glucose concentration after 16 h of fermentation. Scale-up studies in stirred fermenter produced much higher productivity (1.32 g/L/h^–1) compared to shake flask fermentation (0.92 g/L/h^–1). The yield of ethanol reached a maximum of 91% and 89% of the theoretical yield of ethanol in shake flasks and fermenter, respectively. The complex of integrated models of development was applied, that has been successfully tested previously for the mathematical analysis of the fermentation processes.     

Ethanol production from sunflower meal biomass by simultaneous saccharification and fermentation (SSF) with Kluyveromyces marxianus ATCC 36907

The lignocellulosic materials are considered promising renewable resources for ethanol production, but improvements in the processes should be studied to reduce operating costs. Thus, the appropriate enzyme loading for cellulose saccharification is critical for process economics. This study aimed at evaluating the concentration of cellulase and β-glucosidase in the production of bioethanol by simultaneous saccharification and fermentation (SSF) of sunflower meal biomass. The sunflower biomass was pretreated with 6 % H₂SO₄ (w/v), at 121 °C, for 20 min, for hemicellulose removal and delignificated with 1 % NaOH. SSF was performed with Kluyveromyces marxianus ATCC 36907, at 38 °C, 150 rpm, for 72 h, with different enzyme concentrations (Cellulase Complex NS22086-10, 15 and 20 FPU/g_substrate and β-Glucosidase NS22118, with a cellulase to β-glucosidase ratio of 1.5:1; 2:1 and 3:1). The best condition for ethanol production was cellulase 20 FPU/g_substrate and β-glucosidase 13.3 CBU/g_substrate, resulting in 27.88 g/L ethanol, yield of 0.47 g/g and productivity of 0.38 g/L h. Under this condition the highest enzymatic conversion of cellulose to glucose was attained (87.06 %).     

Whole slurry fermentation of maleic acid-pretreated oil palm empty fruit bunches for ethanol production not necessitating a detoxification process

The yield of ethanol from oil palm empty fruit bunches (EFB) was increased on exploiting maleic acid pretreatment combined with fermentation of the pretreated whole slurry. The optimized conditions for pretreatment were to expose EFB to a high temperature (190 °C) with 1 % (w/v) maleic acid for a short time duration (3 min ramping to the set temperature with no holding) in a microwave digester. An enzymatic digestibility of 60.9 % (based on theoretical glucose yield) was exhibited using pretreated and washed EFB after 48 h of hydrolysis. Simultaneous saccharification and fermentation (SSF) of the whole slurry of pretreated EFB for 48 h resulted in 61.3 % theoretical yield of ethanol based on the initial amount of glucan in untreated EFB. These results indicate that maleic acid is a suitable catalyst not requiring detoxification steps for whole slurry fermentation of EFB for ethanol production, thus improving the process economics. Also, the whole slurry fermentation can significantly increase the biomass utilization by converting sugar from both solid and liquid phases of the pretreated slurry.     

DiSC (direct saccharification of culms) process for bioethanol production from rice straw

A simple process (the direct-saccharification-of-culms (DiSC) process) to produce ethanol from rice straw culms, accumulating significant amounts of soft carbohydrates (SCs: glucose, fructose, sucrose, starch and β-1,3-1,4-glucan) was developed. This study focused on fully mature culms of cv. Leafstar, containing 69.2% (w/w of dried culms) hexoses from SCs and cellulose. Commercially-available wind-separation equipment successfully prepared a culm-rich fraction with a SC recovery of 83.1% (w/w) from rice straw flakes (54.1% of total weight of rice straw). The fraction was suspended in water (20%, w/w) for starch liquefaction, and the suspension was subjected to a simultaneous saccharification and fermentation with yeast, yielding 5.6% (w/v) ethanol (86% of the theoretical yield from whole hexoses in the fraction) after 24 h fermentation. Thus, the DiSC process produced highly-concentrated ethanol from rice straw in a one vat process without any harsh thermo-chemical pretreatments.     

Acetic acid-catalyzed hydrothermal pretreatment of corn stover for the production of bioethanol at high-solids content

Corn stover (CS) was hydrothermally pretreated using CH₃COOH (0.3 %, v/v), and subsequently its ability to be utilized for conversion to ethanol at high-solids content was investigated. Pretreatment conditions were optimized employing a response surface methodology (RSM) with temperature and duration as independent variables. Pretreated CS underwent a liquefaction/saccharification step at a custom designed free-fall mixer at 50 °C for either 12 or 24 h using an enzyme loading of 9 mg/g dry matter (DM) at 24 % (w/w) DM. Simultaneous enzymatic saccharification and fermentation (SSF) of liquefacted corn stover resulted in high ethanol concentration (up to 36.8 g/L), with liquefaction duration having a negligible effect. The threshold of ethanol concentration of 4 % (w/w), which is required to reduce the cost of ethanol distillation, was surpassed by the addition of extra enzymes at the start up of SSF achieving this way ethanol titer of 41.5 g/L.     

The isolation and characterization of simultaneous saccharification and fermentation microorganisms for Laminaria japonica utilization

Brown seaweed contains various carbohydrates, such as alginate, laminaran, and mannitol, therefore ethanol fermentation was attempted with Nuruk and a mixed culture that included Laminaria japonica. Nuruk is used to make Korean traditional alcohol. In the research, four microorganisms that produced ethanol and had the ability to achieve alginate degradation were obtained on the L. japonica medium. Nuruk 4 was found to produce a better result than the other tested microorganisms, and the optimal substrate for ethanol production was found to be mannitol (2.59 g/L at 96 h). Nuruk 4 was more than three times better compared with Candida tropicalis in regards to ethanol production. When alginate lyase activity occurred, it appeared as a clear zone around Nuruk 3. The maximal ethanol production yield conditions were comprised of Nuruk 3 and 4 on the anaerobic culture. In this case, 2.0 g/L of ethanol were efficiently produced under the same conditions.     

Simultaneous saccharification and fermentation of enzyme pretreated Lantana camara using S. cerevisiae

Lantana camara, an abundantly available non-edible lignocellulosic biomass has been found to be a potential feedstock for ethanol production. The substrate was first pretreated with laccase followed by simultaneous saccharification and fermentation using cellulase and Saccharomyces cerevisiae, respectively. Laccase was produced from Pleurotus sp. and carbohydratases (cellulase and xylanase) were produced from Trichoderma reesei Rut C30. Using pretreated substrate simultaneous saccharification and fermentation was optimized through central composite design-based response surface methodology. Maximum bioethanol concentration of 5.14 % (v/v) was obtained at optimum process conditions of substrate concentration 17 % (w/v), inoculum volume 9 % (v/v), inoculum age 60 and 144 h of incubation time. To enhance ethanol yield, S. cerevisiae was treated with ethyl methane sulfonate, a chemical mutagenic agent which induced mutagenesis. A maximum bioethanol concentration of 6.01 % (v/v) was obtained using the mutated strain of S. cerevisiae (CM5).