Hydrolysis of sorghum straw using phosphoric acid: evaluation of furfural production

Sorghum straw is a waste that has been studied scarcely. The main application is its use as raw material for xylose production. Xylose is a hemicellulosic sugar mainly used for its bioconversion toward xylitol. An alternative use could be its conversion toward furfural. The objective of this work was to study the furfural production by hydrolysis of sorghum straw with phosphoric acid at 134 degrees C. Several concentrations of H(3)PO(4) in the range 2-6% and reaction time (range 0-300 min) were evaluated. Kinetic parameters of mathematical models for predicting the concentration of xylose, glucose, arabinose, acetic acid and furfural in the hydrolysates were found. Optimal conditions for furfural production by acid hydrolysis were 6% H(3)PO(4) at 134 degrees C for 300 min, which yielded a solution with 13.7 g furfural/L, 4.0 g xylose/L, 2.9 g glucose/L, 1.1g arabinose/L and 1.2g acetic acid/L. The furfural yield of the process was 0.1336 g furfural/g initial dry matter was obtained. The results confirmed that sorghum straw can be used for furfural production when it is hydrolyzed using phosphoric acid.     

Optimization of furfural production from hemicellulose extracted from delignified palm pressed fiber using a two-stage process

This study aims to optimize the conditions for furfural production from hemicellulose extracted from delignified palm pressed fiber (dPPF) via two-stage process: acid hydrolysis followed by dehydration, using response surface methodology (RSM). The extracted hemicellulose contained 80.8% xylose. In order to convert hemicellulose to xylose in the acid hydrolysis step, there were four important parameters consisting of reaction temperature (100–150 °C), sulfuric acid concentration (1–10% v/v), ratio of sulfuric acid to hemicellulose (L/S ratio) (10, 9, and 8 v/w), and reaction time (30–120 min). The maximum xylose production (12.58 g/L) was achieved at 125 °C, 5.5% sulfuric acid, L/S ratio of 9 mL/g for 30 min with the determination coefficient (R²) value of 0.90. For the dehydration process, two parameters; reaction temperature (120–160 °C) and reaction time (30–150 min), were optimized. The maximum furfural production (8.67 g/L) was achieved at a reaction temperature of 140 °C for 90 min with the determination coefficient (R²) value of 0.93.     

Evaluation of cotton stalk hydrolysate for xylitol production

Cotton stalk is a widely distributed and abundant lignocellulosic waste found in Turkey. Because of its rich xylose content, it can be a promising source for the production of xylitol. Xylitol can be produced by chemical or biotechnological methods. Because the biotechnological method is a simple process with great substrate specificity and low energy requirements, it is more of an economic alternative for the xylitol production. This study aimed to use cotton stalk for the production of xylitol with Candida tropicalis Kuen 1022. For this purpose, the combined effects of different oxygen concentration, inoculum level and substrate concentration were investigated to obtain high xylitol yield and volumetric xylitol production rate. Candida tropicalis Kuen 1022 afforded different concentrations of xylitol depending on xylose concentration, inoculum level, and oxygen concentration. The optimum xylose, yeast concentration, and airflow rate for cotton stalk hydrolysate were found as 10.41 g L^?1, 0.99 g L^?1, and 1.02 vvm, respectively, and under these conditions, xylitol yield and volumetric xylitol production rate were obtained as 36% and 0.06 g L^?1 hr^?1, respectively. The results of this study show that cotton stalk can serve as a potential renewable source for the production of xylitol.     

Yeast strains for ethanol production from lignocellulosic hydrolysates during in situ detoxification

Yeast strains Y1, Y4 and Y7 demonstrated high conversion efficiencies for sugars and high abilities to tolerate or metabolize inhibitors in dilute-acid lignocellulosic hydrolysates. Strains Y1 and Y4 completely consumed the glucose within 24 h in dilute-acid lignocellulosic hydrolysate during in situ detoxification, and the maximum ethanol yields reached 0.49 g and 0.45 g ethanol/g glucose, equivalent to maximum theoretical values of 96% and 88.2%, respectively. Strain Y1 could metabolize xylose to xylitol with a yield of 0.64 g/g xylose, whereas Y4 was unable to utilize xylose as a substrate. Strain Y7 was able to consume sugars (glucose and xylose) within 72 h during hydrolysate in situ detoxification, producing a high ethanol yield (equivalent to 93.6% of the maximum theoretical value). Y1 and Y7 are the most efficient yeast strains yet reported for producing ethanol from non-detoxified dilute-acid lignocellulosic hydrolysates. These findings offer huge potential for improving the economics of bio-ethanol production from lignocellulosic hydrolysates.     

Acid hydrolysis of fibers from dairy manure

Concentrated acid hydrolysis of lignocellulosic materials is a conventional treatment process for the production of mono-sugars. However, this method has been proved ineffective and undesirable for the treatment of dairy manure due to the high nitrogen content of dairy manure and the environmental issues caused by the use of highly concentrated acid solution. In an effort to overcome these barriers, a modified acid hydrolysis process with short reaction time was introduced that involved a nitrogen-removing pretreatment followed by decrystallization with concentrated acid and then hydrolysis using dilute acid. The effects of nitrogen, acid concentration, reaction time, and temperature were investigated. A pretreated manure with a low nitrogen content of 1.3% was used as the substrate. The results indicated that the optimal conditions for fiber decrystallization were 75% acid concentration, 3:5 sample to acid ratio (weight basis), and 30 min of reaction time; while the optimal conditions for acid hydrolysis were 12.5% acid and 10% dry sample at 135 degrees C for 10 min. These conditions produced 26 g/L glucose at a yield of 84% and 11 g/L hemicellulose-sugars at a yield of 80%.     

Pretreatment of Extruded Corn Stover with Polyethylene Glycol to Enhance Enzymatic Hydrolysis: Optimization, Kinetics, and Mechanism of Action

Due to the high potential of the extrusion technique for pretreatment of lignocellulosic substrates, several attempts have been conducted in previous studies to further increase the subsequent sugar yield from extrusion pretreatment. Examples include application of chemicals along with extrusion, such as alkali-extrusion and ethylene glycol-extrusion, or before extrusion, such as hot water extraction. In this study, a new sequential technique has been developed for pretreatment of corn stover (CS), which utilizes an initial extrusion pretreatment (155?rpm screw speed and temperatures of 90°C, 180°C and 180°C corresponding to feed, barrel and die zones, respectively at a reaction time of 45?C90?s) followed by pretreatment with polyethylene glycol 6,000 (PEG). In order to fully characterize the response for sugar yield over the range of surfactant treatment conditions assessed, response surface methodology was used. Treatment temperature, incubation time and PEG concentration were varied between 45?C55°C, 1?C4?h, 0.15?C0.6?g PEG/g glucan, respectively. Statistical analysis was conducted by fitting the glucose and xylose yields to a quadratic polynomial model. PEG concentration and temperature were found to be the most significant factors in surfactant pretreatment. The optimum condition resulted in 25.4% and 10.3% increase in glucose and xylose yield, respectively. Using the combination of 10.8?FPU/g glucan of Ctec₂ and 0.3?g PEG/g glucan, the glucose yield of extruded CS reached 98%. A yield was 64% resulted from application of similar amounts of Ctec and Htec. Decreased adsorption of enzyme to the lignocellulosic substrate as well as increased enzyme activity and reaction velocity indicated by kinetic parameter evaluation and nitrogen combustion analysis suggested an increased solubilization of cellulase in the presence of PEG. We propose that a non-productive adsorption of enzymes occur during hydrolysis not only due to lignin but also due to crystalline cellulose. Comparison of enzyme adsorptions and increase in sugar yields between Avicel and CS suggests the presence of other potential mechanisms of action for PEG in addition to increase of enzyme solubilization.     

Bioconversion of waste office paper to L(+)-lactic acid by the filamentous fungus Rhizopus oryzae

L(+)-lactic acid production was investigated using an enzymatic hydrolysate of waste office automation (OA) paper in a culture of the filamentous fungus Rhizopus oryzae. In 4 d culture, 82.8 g/l glucose, 7 g/l xylose, and 3.4 g/l cellobiose contained in the hydrolysate were consumed to produce 49.1 g/l of lactic acid. The lactic acid yield and production rate were only 0.59 g/g and 16.3 g/l/d, respectively, only 75% and 61% of the results from the glucose medium. The low production rate from waste OA hydrolysate was elucidated by trials using xylose as the sole carbon source; in those trials, the lactic acid production rate was 7.3 g/l/d, only 28% that of glucose or cellobiose. The low lactic acid yield from waste OA hydrolysate was clarified by trials using artificial hydrolysates comprised of 7:2:1 or 7:1:2 ratios of glucose:cellobiose:xylose. For both, the lactic acid production rate of 17.4 g/l/d matched that of waste OA paper, while the lactic acid yield was similar to that of the glucose medium. This indicates that the production rate may be inhibited by xylose derived from hemicellulose, and the yield may be inhibited by unknown compounds derived from paper pulp.     

Steam pretreatment of H(2)SO(4)-impregnated Salix for the production of bioethanol

In the bioconversion of lignocellulosic materials to ethanol, pretreatment of the material prior to enzymatic hydrolysis is essential to obtain high overall yields of sugar and ethanol. In this study, steam pretreatment of fast-growing Salix impregnated with sulfuric acid has been investigated by varying the temperature (180-210 degrees C), the residence time (4, 8 or 12 min), and the acid concentration (0.25% or 0.5% (w/w) H(2)SO(4)). High sugar recoveries were obtained after pretreatment, and the highest yields of glucose and xylose after the subsequent enzymatic hydrolysis step were 92% and 86% of the theoretical, respectively, based on the glucan and xylan contents of the raw material. The most favorable pretreatment conditions regarding the overall sugar yield were 200 degrees C for either 4 or 8 min using 0.5% sulfuric acid, both resulting in a total of 55.6g glucose and xylose per 100g dry raw material. Simultaneous saccharification and fermentation experiments were performed on the pretreated slurries at an initial water-insoluble content of 5%, using ordinary baker's yeast. An overall theoretical ethanol yield of 79%, based on the glucan and mannan content in the raw material, was obtained.     

High‐yield lipid production from lignocellulosic biomass using engineered xylose‐utilizing Yarrowia lipolytica

Lignocellulosic biomass shows high potential as a renewable feedstock for use in biodiesel production via microbial fermentation. Yarrowia lipolytica, an emerging oleaginous yeast, has been engineered to efficiently convert xylose, the second most abundant sugar in lignocellulosic biomass, into lipids for lignocellulosic biodiesel production. Yet, the lipid yield from xylose or lignocellulosic biomass remains far lower than that from glucose. Here we developed an efficient xylose‐utilizing Y. lipolytica strain, expressing an isomerase‐based pathway, to achieve high‐yield lipid production from lignocellulosic biomass. The newly developed xylose‐utilizing Y. lipolytica, YSXID, produced 12.01 g/L lipids with a maximum yield of 0.16 g/g, the highest ever reported, from lignocellulosic hydrolysates. Consequently, this study shows the potential of isomerase‐based xylose‐utilizing Y. lipolytica for economical and sustainable production of biodiesel and oleochemicals from lignocellulosic biomass.     

Fermentation and recovery of glutamic acid from palm waste hydrolysate by Ion-exchange resin column

Glutamic acid produced from palm waste hydrolysate by fermentation with Brevibacterium lactofermentum ATCC 13869 is produced with a remarkably high yield compared with that produced from pure glucose as a carbon source. The produce yield is 70 g/L with glucose, wherease, when palm waste hydrolysate is the fermentation medium in the same bioreactor under same conditions, it is 88 g/L. The higher yield may be attributed to the fact that this organism has the ability to convert sugars other than only glucose present in the hydrolysate. Bioreactor conditions most conducive for maximum production are pH 7.5, temperature of 30 degrees rmentation period of 48 h, inoculum size 6%, substrate concentration of 10 g per 100 mL, yeast extract 0.5 g per 100 mL as a suitable N source, and biotin at a concentration of 10 pg/L. Palm waste hydrolysate used in this study was prepared by enzymic saccharification of treated palm press fiber under conditions that yielded a maximum of 30 g/L total reducing sugars. Glutamic acid from fermentation broth was recovered by using a chromatographic column (5cm x 60 cm) packed with a strong ion-exchange resin. The filtered broth containing glutamic acid and other inorganic ions was fed to the fully charged column. The broth was continuously recycled at a flow rate of 50 mL/min (retention time of 55 min) until glutamic acid was fully adsorbed on the column leaving other ions in the effluent. Recovery was done by eluting with urea and sodium hydroxide for total displacement of glutamic acid from the resin. The eluent containing 88 g/L of glutamic acid was concentrated by evaporation to obtain solid crystals of the product. (c) 1995 John Wiley & Sons, Inc.     

Optimization of the pretreatment of rice straw hemicellulosic hydrolyzates for microbial production of xylitol

Hemicellulosic hydrolyzate obtained from rice straw was evaluated to determine if it was a suitable fementation medium for the production of xylitol byCandida mogii ATCC 18364. To obtain xylose selectively from rice straw, it is important to establish rapid hydrolysis conditions that yield xylose-rich substrates. The results of hydrolysis experiments indicated that the optimal reaction conditions for the recovery of xylose from rice straw hemicellulose were obtained using a sulfuric acid concentration of 1.5%, a reaction temperature of 130°C, a reaction time of 20 min and a solid to liquid ratio of 1∶10. Because the fermentation of concentrated acid hydrolyzates can be inhibited by compounds present in the raw material or produced during the hydrolysis process, various methods were tested to determine if they could detoxify the hydrolyzates and thus improve xylitol production. The greatest xylitol yield (0.53 g/g) and volumetric productivity (0.38 g/L·h) were obtained when an overlimed hydrolyzate was treated with activated charcoal.     

Synthesis of polyketides from low cost substrates by the thermotolerant yeast Kluyveromyces marxianus

Kluyveromyces marxianus is a promising nonconventional yeast for biobased chemical production due to its rapid growth rate, high TCA cycle flux, and tolerance to low pH and high temperature. Unlike Saccharomyces cerevisiae, K. marxianus grows on low-cost substrates to cell densities that equal or surpass densities in glucose, which can be beneficial for utilization of lignocellulosic biomass (xylose), biofuel production waste (glycerol), and whey (lactose). We have evaluated K. marxianus for the synthesis of polyketides, using triacetic acid lactone (TAL) as the product. The 2-pyrone synthase (2-PS) was expressed on a CEN/ARS plasmid in three different strains, and the effects of temperature, carbon source, and cultivation strategy on TAL levels were determined. The highest titer was obtained in defined 1% xylose medium at 37°C, with substantial titers at 41 and 43°C. The introduction of a high-stability 2-PS mutant and a promoter substitution increased titer four-fold. 2-PS expression from a multi-copy pKD1-based plasmid improved TAL titers a further five-fold. Combining the best plasmid, promoter, and strain resulted in a TAL titer of 1.24 g/L and a yield of 0.0295 mol TAL/mol carbon for this otherwise unengineered strain in 3 ml tube culture. This is an excellent titer and yield (on xylose) before metabolic engineering or fed-batch culture relative to other hosts (on glucose), and demonstrates the promise of this rapidly growing and thermotolerant yeast species for polyketide production.     

Lactic acid production from sugarcane bagasse hydrolysates by Lactobacillus pentosus: Integrating xylose and glucose fermentation

Lactic acid, traditionally obtained through fermentation process, presents numerous applications in different industrial segments, including production of biodegradable polylactic acid (PLA). Development of low cost substrate fermentations could improve economic viability of lactic acid production, through the use of agricultural residues as lignocellulosic biomass. Studies regarding the use of sugarcane bagasse hydrolysates for lactic acid production by Lactobacillus spp. are reported. First, five strains of Lactobacillus spp. were investigated for one that had the ability to consume xylose efficiently. Subsequently, biomass fractionation was performed by dilute acid and alkaline pretreatments, and the hemicellulose hydrolysate (HH) fermentability by the selected strain was carried out in bioreactor. Maximum lactic acid concentration and productivity achieved in HH batch were 42.5 g/L and 1.02 g/L h, respectively. Hydrolyses of partially delignified cellulignin (PDCL) by two different enzymatic cocktails were compared. Finally, fermentation of HH and PDCL hydrolysate together was carried out in bioreactor in a hybrid process: saccharification and co-fermentation with an initial enzymatic hydrolysis. The high fermentability of these process herein developed was demonstrated by the total consumption of xylose and glucose by Lactobacillus pentosus, reaching at 65.0 g/L of lactic acid, 0.93 g/g of yield, and 1.01 g/L h of productivity. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 35: e2718, 2019     

Fermentation of lignocellulosic sugars to acetic acid by <Emphasis Type="Italic">Moorella thermoacetica</Emphasis>

A systematic study of bioconversion of lignocellulosic sugars to acetic acid by Moorella thermoacetica (strain ATCC 39073) was conducted. Four different water-soluble fractions (hydrolysates) obtained after steam pretreatment of lignocellulosic biomass were selected and fermented to acetic acid in batch fermentations. M. thermoacetica can effectively ferment xylose and glucose in hydrolysates from wheat straw, forest residues, switchgrass, and sugarcane straw to acetic acid. Xylose and glucose were completely utilized, with xylose being consumed first. M. thermoacetica consumed up to 62 % of arabinose, 49 % galactose and 66 % of mannose within 72 h of fermentation in the mixture of lignocellulosic sugars. The highest acetic acid yield was obtained from sugarcane straw hydrolysate, with 71 % of theoretical yield based on total sugars (17 g/L acetic acid from 24 g/L total sugars). The lowest acetic acid yield was observed in forest residues hydrolysate, with 39 % of theoretical yield based on total sugars (18 g/L acetic acid from 49 g/L total sugars). Process derived compounds from steam explosion pretreatment, including 5-hydroxymethylfurfural (0.4 g/L), furfural (0.1 g/L) and total phenolics (3 g/L), did not inhibit microbial growth and acetic acid production yield. This research identified two major factors that adversely affected acetic acid yield in all hydrolysates, especially in forest residues: (i) glucose to xylose ratio and (ii) incomplete consumption of arabinose, galactose and mannose. For efficient bioconversion of lignocellulosic sugars to acetic acid, it is imperative to have an appropriate balance of sugars in a hydrolysate. Hence, the choice of lignocellulosic biomass and steam pretreatment design are fundamental steps for the industrial application of this process.     

Improved bioconversion of lignocellulosic biomass by Saccharomyces cerevisiae engineered for tolerance to acetic acid

Lignocellulosic biomass has considerable potential for the production of fuels and chemicals as a promising alternative to conventional fossil fuels. However, the bioconversion of lignocellulosic biomass to desired products must be improved to reach economic viability. One of the main technical hurdles is the presence of inhibitors in biomass hydrolysates, which hampers the bioconversion efficiency by biorefinery microbial platforms such as Saccharomyces cerevisiae in terms of both production yields and rates. In particular, acetic acid, a major inhibitor derived from lignocellulosic biomass, severely restrains the performance of engineered xylose‐utilizing S. cerevisiae strains, resulting in decreased cell growth, xylose utilization rate, and product yield. In this study, the robustness of XUSE, one of the best xylose‐utilizing strains, was improved for the efficient conversion of lignocellulosic biomass into bioethanol under the inhibitory condition of acetic acid stress. Through adaptive laboratory evolution, we successfully developed the evolved strain XUSAE57, which efficiently converted xylose to ethanol with high yields of 0.43–0.50 g ethanol/g xylose even under 2–5 g/L of acetic stress. XUSAE57 not only achieved twofold higher ethanol yields but also improved the xylose utilization rate by more than twofold compared to those of XUSE in the presence of 4 g/L of acetic acid. During fermentation of lignocellulosic hydrolysate, XUSAE57 simultaneously converted glucose and xylose with the highest ethanol yield reported to date (0.49 g ethanol/g sugars). This study demonstrates that the bioconversion of lignocellulosic biomass by an engineered strain could be significantly improved through adaptive laboratory evolution for acetate tolerance, which could help realize the development of an economically feasible lignocellulosic biorefinery to produce fuels and chemicals.     

A novel isolate of <Emphasis Type="Italic">Clostridium butyricum</Emphasis> for efficient butyric acid production by xylose fermentation

Bacterial fermentation of lignocellulose has been regarded as a sustainable approach to butyric acid production. However, the yield of butyric acid is hindered by the conversion efficiency of hydrolysate xylose. A mesophilic alkaline-tolerant strain designated as Clostridium butyricum B10 was isolated by xylose fermentation with acetic and butyric acids as the principal liquid products. To enhance butyric acid production, performance of the strain in batch fermentation was evaluated with various temperatures (20–47 °C), initial pH (5.0–10.0), and xylose concentration (6–20 g/L). The results showed that the optimal temperature, initial pH, and xylose concentration for butyric acid production were 37 °C, 9.0, and 8.00 g/L, respectively. Under the optimal condition, the yield and specific yield of butyric acid reached about 2.58 g/L and 0.36 g/g xylose, respectively, with 75.00% butyric acid in the total volatile fatty acids. As renewable energy, hydrogen was also collected from the xylose fermentation with a yield of about 73.86 mmol/L. The kinetics of growth and product formation indicated that the maximal cell growth rate (μ _m ) and the specific butyric acid yield were 0.1466 h^?1 and 3.6274 g/g cell (dry weight), respectively. The better performance in xylose fermentation showed C. butyricum B10 a potential application in efficient butyric acid production from lignocellulose.     

Effects of sulfuric acid loading and residence time on the composition of sugarcane bagasse hydrolysate and its use as a source of xylose for xylitol bioproduction

A 2(2) full factorial design was employed to evaluate the effects of sulfuric acid loading and residence time on the composition of sugarcane bagasse hydrolysate obtained in a 250-L reactor. The acid loading and the residence time were varied from 70 to 130 mg acid per gram of dry bagasse and from 10 to 30 min, respectively, while the temperature (121 degrees C) and the bagasse loading (10%) were kept constant. Both the sulfuric acid loading and the residence time influenced the concentrations of xylose and inhibitors in the hydrolysate. The highest xylose concentration (22.71 g/L) was achieved when using an acid loading of 130 mg/g and a residence time of 30 min. These conditions also led to increased concentrations of inhibiting byproducts in the hydrolysate. All of the hydrolysates were vacuum-concentrated to increase the xylose concentration, detoxified by pH alteration and adsorption into activated charcoal, and used for xylitol bioproduction in a stirred tank reactor. Neither the least (70 mg/g, 10 min) nor the most severe (130 mg/g, 30 min) hydrolysis conditions led to the best xylitol production (37.5 g/L), productivity (0.85 g/L h), and yield (0.78 g/g).     

Production of lactic acid from hemicellulose extracts by <Emphasis Type="Italic">Bacillus coagulans</Emphasis> MXL-9

Bacillus coagulans MXL-9 was found capable of growing on pre-pulping hemicellulose extracts, utilizing all of the principle monosugars found in woody biomass. This organism is a moderate thermophile isolated from compost for its pentose-utilizing capabilities. It was found to have high tolerance for inhibitors such as acetic acid and sodium, which are present in pre-pulping hemicellulose extracts. Fermentation of 20 g/l xylose in the presence of 30 g/l acetic acid required a longer lag phase but overall lactic acid yield was not diminished. Similarly, fermentation of xylose in the presence of 20 g/l sodium increased the lag time but did not affect overall product yield, though 30 g/l sodium proved completely inhibitory. Fermentation of hot water-extracted Siberian larch containing 45 g/l total monosaccharides, mainly galactose and arabinose, produced 33 g/l lactic acid in 60 h and completely consumed all sugars. Small amounts of co-products were formed, including acetic acid, formic acid, and ethanol. Hemicellulose extract formed during autohydrolysis of mixed hardwoods contained mainly xylose and was converted into lactic acid with a 94% yield. Green liquor-extracted hardwood hemicellulose containing 10 g/l acetic acid and 6 g/l sodium was also completely converted into lactic acid at a 72% yield. The Bacillus coagulans MXL-9 strain was found to be well suited to production of lactic acid from lignocellulosic biomass due to its compatibility with conditions favorable to industrial enzymes and its ability to withstand inhibitors while rapidly consuming all pentose and hexose sugars of interest at high product yields.     

Optimization of fermentable sugar production from rape straw through hydrothermal acid pretreatment

Operational conditions for the hydrolysis of rape straw were optimized using the combined severity index (CS), which combines the effects of time, temperature, and acid concentration into a single parameter. The sugar recovery yield was 77.8% of the theoretical yield at a value of CS=1.3. A maximum concentration of xylose of 7.22 g/L was obtained when the straw was treated for 10 min at a low reaction temperature (150 °C) and high acid concentration (pH 1.17). The pentose-rich hydrolyzate exhibited a low concentration of fermentation-inhibiting compounds. The concept of CS can be conveniently and effectively applied for optimization of pretreatments.     

Optimization of dilute sulfuric acid pretreatment of corn stover for enhanced xylose recovery and xylitol production

Pretreatment steps are necessary for the bioconversion of corn stover (CS) to xylitol. In order to optimize the pretreatment parameters, the sulfuric acid concentration, sulfuric acid residence time, and solid slurry concentration were evaluated, based on the glucose and xylose recovered from CS at the relatively low temperature of 120°C. The optimum conditions were found to be pretreatment with 2.5% (w/v) sulfuric acid for 1.5 h, with a solid slurry concentration of 90 g/L. Under these conditions, the hydrolysis rates of glucan and xylan were approximately 26.0 and 82.8%, respectively. High xylitol production (10.9 g/L) and conversion yield (0.97 g/g) were attained from corn stover hydrolysate (CSH) without detoxification and any nutrient addition. Our results were similar for xylitol production in synthetic medium under the same conditions. The non-necessity of both the hydrolysate detoxification step and nutrient addition to the CSH is undoubtedly promising for scale-up application on an industrial scale, because this medium-based manufacturing process is expected to reduce the production cost of xylitol. The present study demonstrates that value-added xylitol could be effectively produced from CS under optimized pretreatment conditions, especially with CSH as the substrate material.