Enhanced isopropanol and <Emphasis Type="Italic">n</Emphasis>-butanol production by supplying exogenous acetic acid via co-culturing two clostridium strains from cassava bagasse hydrolysate

The focus of this study was to produce isopropanol and butanol (IB) from dilute sulfuric acid treated cassava bagasse hydrolysate (SACBH), and improve IB production by co-culturing Clostridium beijerinckii (C. beijerinckii) with Clostridium tyrobutyricum (C. tyrobutyricum) in an immobilized-cell fermentation system. Concentrated SACBH could be converted to solvents efficiently by immobilized pure culture of C. beijerinckii. Considerable solvent concentrations of 6.19 g/L isopropanol and 12.32 g/L butanol were obtained from batch fermentation, and the total solvent yield and volumetric productivity were 0.42 g/g and 0.30 g/L/h, respectively. Furthermore, the concentrations of isopropanol and butanol increased to 7.63 and 13.26 g/L, respectively, under the immobilized co-culture conditions when concentrated SACBH was used as the carbon source. The concentrations of isopropanol and butanol from the immobilized co-culture fermentation were, respectively, 42.62 and 25.45 % higher than the production resulting from pure culture fermentation. The total solvent yield and volumetric productivity increased to 0.51 g/g and 0.44 g/L/h when co-culture conditions were utilized. Our results indicated that SACBH could be used as an economically favorable carbon source or substrate for IB production using immobilized fermentation. Additionally, IB production could be significantly improved by co-culture immobilization, which provides extracellular acetic acid to C. beijerinckii from C. tyrobutyricum. This study provided a technically feasible and cost-efficient way for IB production using cassava bagasse, which may be suitable for industrial solvent production.     

Two-step production of gamma-aminobutyric acid from cassava powder using <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> and <Emphasis Type="Italic">Lactobacillus plantarum</Emphasis>

Production of gamma-aminobutyric acid (GABA) from crop biomass such as cassava in high concentration is desirable, but difficult to achieve. A safe biotechnological route was investigated to produce GABA from cassava powder by C. glutamicum G01 and L. plantarum GB01-21. Liquefied cassava powder was first transformed to glutamic acid by simultaneous saccharification and fermentation with C. glutamicum G01, followed by biotransformation of glutamic acid to GABA with resting cells of L. plantarum GB01-21 in the reaction medium. After optimizing the reaction conditions, the maximum concentration of GABA reached 80.5 g/L with a GABA productivity of 2.68 g/L/h. This is the highest yield ever reported of GABA production from cassava-derived glucose. The bioprocess provides the added advantage of employing nonpathogenic microorganisms, C. glutamicum and L. plantarum, in microbial production of GABA from cassava biomass, which can be used in the food and pharmaceutical industries.     

Inactivation of the transcription factor <Emphasis Type="Italic">mig1</Emphasis> (<Emphasis Type="Italic">YGL035C</Emphasis>) in <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> improves tolerance towards monocarboxylic weak acids: acetic,formic and levulinic acid

Toxic concentrations of monocarboxylic weak acids present in lignocellulosic hydrolyzates affect cell integrity and fermentative performance of Saccharomyces cerevisiae. In this work, we report the deletion of the general catabolite repressor Mig1p as a strategy to improve the tolerance of S. cerevisiae towards inhibitory concentrations of acetic, formic or levulinic acid. In contrast with the wt yeast, where the growth and ethanol production were ceased in presence of acetic acid 5 g/L or formic acid 1.75 g/L (initial pH not adjusted), the m9 strain (Δmig1::kan) produced 4.06?±?0.14 and 3.87?±?0.06 g/L of ethanol, respectively. Also, m9 strain tolerated a higher concentration of 12.5 g/L acetic acid (initial pH adjusted to 4.5) without affecting its fermentative performance. Moreover, m9 strain produced 33% less acetic acid and 50–70% less glycerol in presence of weak acids, and consumed acetate and formate as carbon sources under aerobic conditions. Our results show that the deletion of Mig1p provides a single gene deletion target for improving the acid tolerance of yeast strains significantly.     

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.     

Precultivation of <Emphasis Type="Italic">Bacillus coagulans</Emphasis> DSM2314 in the presence of furfural decreases inhibitory effects of lignocellulosic by-products during <Emphasis Type="SmallCaps">l</Emphasis>(+)-lactic acid fermentation

By-products resulting from thermo-chemical pretreatment of lignocellulose can inhibit fermentation of lignocellulosic sugars to lactic acid. Furfural is such a by-product, which is formed during acid pretreatment of lignocellulose. pH-controlled fermentations with 1 L starting volume, containing YP medium and a mixture of lignocellulosic by-products, were inoculated with precultures of Bacillus coagulans DSM2314 to which 1 g/L furfural was added. The addition of furfural to precultures resulted in an increase in l(+)-lactic acid productivity by a factor 2 to 1.39 g/L/h, an increase in lactic acid production from 54 to 71 g and an increase in conversion yields of sugar to lactic acid from 68 to 88 % W/W in subsequent fermentations. The improved performance was not caused by furfural consumption or conversion, indicating that the cells acquired a higher tolerance towards this by-product. The improvement coincided with a significant elongation of B. coagulans cells. Via RNA-Seq analysis, an upregulation of pathways involved in the synthesis of cell wall components such as bacillosamine, peptidoglycan and spermidine was observed in elongated cells. Furthermore, the gene SigB and genes promoted by SigB, such as NhaX and YsnF, were upregulated in the presence of furfural. These genes are involved in stress responses in bacilli.     

Cloning of <Emphasis Type="Italic">phaCAB</Emphasis> genes from thermophilic <Emphasis Type="Italic">Caldimonas manganoxidans</Emphasis> in <Emphasis Type="Italic">Escherichia coli</Emphasis> for poly(3-hydroxybutyrate) (PHB) production

PHB biosynthesis pathway, consisting of three open reading frames (ORFs) that encode for β-ketothiolase (phaA _Cma , 1179 bp), acetoacetyl-CoA reductase (phaB _Cma , 738 bp), and PHA synthase (phaC _Cma , 1694 bp), of Caldimonas manganoxidans was identified. The functions of PhaA, PhaB, and PhaC were demonstrated by successfully reconstructing PHB biosynthesis pathway of C. manganoxidans in Escherichia coli, where PHB production was confirmed by OD₆₀₀, gas chromatography, Nile blue stain, and transmission electron microscope (TEM). The protein sequence alignment of PHB synthases revealed that phaC _Cma shares at least 60% identity with those of class I PHB synthase. The effects of PhaA, PhaB, and PhaC expression levels on PHB production were investigated. While the overexpression of PhaB is found to be important in recombinant E. coli, performances of PHB production can be quantified as follows: PHB concentration of 16.8 ± 0.6 g/L, yield of 0.28 g/g glucose, content of 74%, productivity of 0.28 g/L/h, and Mw of 1.41 MDa.     

Fatty Acid Characterization and Biodiesel Production by the Marine Microalga <Emphasis Type="Italic">Asteromonas gracilis</Emphasis>: Statistical Optimization of Medium for Biomass and Lipid Enhancement

Lipid production is an important indicator for evaluating microalgal species for biodiesel production. In this study, a new green microalga was isolated from a salt lake in Egypt and identified as Asteromonas gracilis. The main parameters such as biomass productivity, lipid content, and lipid productivity were evaluated in A. gracilis, cultivated in nutrient-starved (nitrogen, phosphorous), and salinity stress as a one-factor-at-a-time method. These parameters in general did not vary significantly from the standard nutrient growth media when these factors were utilized separately. Hence, response surface methodology (RSM) was assessed to study the combinatorial effect of different concentrations of the abovementioned factor conditions and to maximize the biomass productivity, lipid content, and lipid productivity of A. gracilis by determining optimal concentrations. RSM optimized media, including 1.36 M NaCl, 1 g/L nitrogen, and 0.0 g/L phosphorus recorded maximum biomass productivity, lipid content, and lipid productivity (40.6 mg/L/day, 39.3%, and 15.9 mg/L/day, respectively) which agreed well with the predicted values (40.1 mg/L/day, 43.6%, and 14.6 mg/L/day, respectively). Fatty acid profile of A. gracilis was composed of C16:0, C16:1, C18:0, C18:3, C18:2, C18:1, and C20:5, and the properties of fuel were also in agreement with international standards. These results suggest that A. gracilis is a promising feedstock for biodiesel production.     

Very high gravity ethanol and fatty acid production of <Emphasis Type="Italic">Zymomonas mobilis</Emphasis> without amino acid and vitamin

Very high gravity (VHG) fermentation is the mainstream technology in ethanol industry, which requires the strains be resistant to multiple stresses such as high glucose concentration, high ethanol concentration, high temperature and harsh acidic conditions. To our knowledge, it was not reported previously that any ethanol-producing microbe showed a high performance in VHG fermentations without amino acid and vitamin. Here we demonstrate the engineering of a xylose utilizing recombinant Zymomonas mobilis for VHG ethanol fermentations. The recombinant strain can produce ethanol up to 136 g/L without amino acid and vitamin with a theoretical yield of 90 %, which is significantly superior to that produced by all the reported ethanol-producing strains. The intracellular fatty acids of the bacterial were about 16 % of the bacterial dry biomass, with the ratio of ethanol:fatty acids was about 273:1 (g/g). The recombinant strain was achieved by a multivariate-modular strategy tackles with the multiple stresses which are closely linked to the ethanol productivity of Z. mobilis. The over-expression of metB/yfdZ operon enabled the growth of the recombinant Z. mobilis in a chemically defined medium without amino acid and vitamin; and the fatty acids overproduction significantly increased ethanol tolerance and ethanol production. The coupled production of ethanol with fatty acids of the Z. mobilis without amino acid and vitamin under VHG fermentation conditions may permit a significant reduction of the production cost of ethanol and microbial fatty acids.     

Accumulation of conjugated linoleic acid in <Emphasis Type="Italic">Lactobacillus plantarum</Emphasis> WU-P19 is enhanced by induction with linoleic acid and chitosan treatment

Production of conjugated linoleic acid (CLA) by the potential probiotic bacterium Lactobacillus plantarum WU-P19 was investigated with the aim of enhancing production. CLA produced using this bacterium may be used to supplement dietary intake. Cultures were fed linoleic acid for conversion to CLA and the CLA produced was measured. In some cases, chitosan was added to cultures to improve cellular uptake of linoleic acid. Under static conditions at 37 °C, the bacterium grew and produced CLA in the pH range of 5.5–6.5. At pH 6.0, a 36-h incubation period maximized the concentration of the dry biomass (0.82 g/L), the CLA content in the biomass (4.1 mg/g), and linoleic acid in the biomass (1.2 mg/g). In comparison with cultures grown without linoleic acid in the medium, supplementing the medium with linoleic acid at 600 μg/mL slowed the production of CLA, but the CLA content in the dry biomass increased to 12–14 mg/g and the linoleic acid content increased to 8–11 mg/g. Supplementing the culture medium with chitosan and linoleic acid enhanced production of CLA in the dry biomass to 21 mg/g within 36 h. Nearly 50% of the CLA was cis-9, trans-11-CLA, and the remainder was trans-10, cis-12-CLA. Linoleic acid content of the dry biomass was increased to 37 mg/g. Accumulation of CLA in the cells was enhanced by feeding linoleic acid. Supplementing the culture with linoleic acid and chitosan further increased accumulation of CLA.     

Enhancement of Pyruvate Productivity in <Emphasis Type="Italic">Candida glabrata</Emphasis> by Deleting the <Emphasis Type="Italic">CgADE13</Emphasis> Gene to Improve Acid Tolerance

Acid tolerance is one of the critical factors to evaluate the quality of the industrial production strains, especially organic acid producing microorganisms. To circumvent this problem, we investigated the physiological function of adenylosuccinate lyase in AMP metabolism from Candida glabrata by deleting the corresponding gene, CgADE13. At pH 4.0, CgADE13 deletion resulted in a 68.3% and 112.0% increase in biomass and cell viability compared to those of wild type strain (wt), respectively. In addition, CgADE13 deletion also protected cell morphology and counteracted ROS production. Further, the intracellular ATP level of strain Cgade13Δ was decreased by 25.0%, and its H+-ATPase activity was increased by 15.0%. Finally, pyruvate production with strain Cgade13Δ in a 30-L batch bioreactor at pH 4.0 reached 53.9 g/L, and pyruvate productivity was increased by 166.7% compared to that of wt. This is the first report regarding tolerance engineering of C. glabrata for enhancing pyruvate productivity, which provides a good starting point for metabolic engineering to achieve the industrial production of other chemicals.     

Enhancement of NAD(H) pool for formation of oxidized biochemicals in <Emphasis Type="Italic">Escherichia coli</Emphasis>

The NAD⁺/NADH ratio and the total NAD(H) play important roles for whole-cell biochemical redox transformations. After the carbon source is exhausted, the degradation of NAD(H) could contribute to a decline in the rate of a desired conversion. In this study, methods to slow the native rate of NAD(H) degradation were examined using whole-cell Escherichia coli with two model oxidative NAD⁺-dependent biotransformations. A high phosphate concentration (50 mM) was observed to slow NAD(H) degradation. We also constructed E. coli strains with deletions in genes coding several enzymes involved in NAD⁺ degradation. In shake-flask experiments, the total NAD(H) concentration positively correlated with conversion of xylitol to l-xylulose by xylitol 4-dehydrogenase, and the greatest conversion (80%) was observed using MG1655 nadR nudC mazG/pZE12-xdh/pCS27-nox. Controlled 1-L batch processes comparing E. coli nadR nudC mazG with a wild-type background strain demonstrated a 30% increase in final l-xylulose concentration (5.6 vs. 7.9 g/L) and a 25% increase in conversion (0.53 vs. 0.66 g/g). MG1655 nadR nudC mazG was also examined for the conversion of galactitol to l-tagatose by galactitol 2-dehydrogenase. A batch process using 15 g/L glycerol and 10 g/L galactitol generated over 9.4 g/L l-tagatose, corresponding to 90% conversion and a yield of 0.95 g l-tagatose/g galactitol consumed. The results demonstrate the value of minimizing NAD(H) degradation as a means to improve NAD⁺-dependent biotransformations.     

Enhanced fed-batch production of pyrroloquinoline quinine in <Emphasis Type="Italic">Methylobacillus</Emphasis> sp. CCTCC M2016079 with a two-stage pH control strategy

The effects of pH control strategy and fermentative operation modes on the biosynthesis of pyrroloquinoline quinine (PQQ) were investigated systematically with Methylobacillus sp. CCTCC M2016079 in the present work. Firstly, the shake-flask cultivations and benchtop fermentations at various pH values ranging from 5.3 to 7.8 were studied. Following a kinetic analysis of specific cell growth rate (μ _x ) and specific PQQ formation rate (μ _p ), the discrepancy in optimal pH values between cell growth and PQQ biosynthesis was observed, which stimulated us to develop a novel two-stage pH control strategy. During this pH-shifted process, the pH in the broth was controlled at 6.8 to promote the cell growth for the first 48 h and then shifted to 5.8 to enhance the PQQ synthesis until the end of fermentation. By applying this pH-shifted control strategy, the maximum PQQ production was improved to 158.61 mg/L in the benchtop fermenter, about 44.9% higher than that under the most suitable constant pH fermentation. Further fed-batch study showed that PQQ production could be improved from 183.38 to 272.21 mg/L by feeding of methanol at the rate of 11.5 mL/h in this two-stage pH process. Meanwhile, the productivity was also increased from 2.02 to 2.84 mg/L/h. In order to support cell growth during the shifted pH stage, the combined feeding of methanol and yeast extract was carried out, which brought about the highest concentration (353.28 mg/L) and productivity (3.27 mg/L/h) of PQQ. This work has revealed the potential of our developed simple and economical strategy for the large-scale production of PQQ.     

Efficient production of α-ketoglutarate in the <Emphasis Type="Italic">gdh</Emphasis> deleted <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> by novel double-phase pH and biotin control strategy

Production of l-glutamate using a biotin-deficient strain of Corynebacterium glutamicum has a long history. The process is achieved by controlling biotin at suboptimal dose in the initial fermentation medium, meanwhile feeding NH₄OH to adjust pH so that α-ketoglutarate (α-KG) can be converted to l-glutamate. In this study, we deleted glutamate dehydrogenase (gdh1 and gdh2) of C. glutamicum GKG-047, an l-glutamate overproducing strain, to produce α-KG that is the direct precursor of l-glutamate. Based on the method of l-glutamate fermentation, we developed a novel double-phase pH and biotin control strategy for α-KG production. Specifically, NH₄OH was added to adjust the pH at the bacterial growth stage and NaOH was used when the cells began to produce acid; besides adding an appropriate amount of biotin in the initial medium, certain amount of additional biotin was supplemented at the middle stage of fermentation to maintain a high cell viability and promote the carbon fixation to the flux of α-KG production. Under this control strategy, 45.6 g/L α-KG accumulated after 30-h fermentation in a 7.5-L fermentor and the productivity and yield achieved were 1.52 g/L/h and 0.42 g/g, respectively.     

High-level recombinant production of squalene using selected <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> strains

For recombinant production of squalene, which is a triterpenoid compound with increasing industrial applications, in microorganisms generally recognized as safe, we screened Saccharomyces cerevisiae strains to determine their suitability. A strong strain dependence was observed in squalene productivity among Saccharomyces cerevisiae strains upon overexpression of genes important for isoprenoid biosynthesis. In particular, a high level of squalene production (400 ± 45 mg/L) was obtained in shake flasks with the Y2805 strain overexpressing genes encoding a bacterial farnesyl diphosphate synthase (ispA) and a truncated form of hydroxyl-3-methylglutaryl-CoA reductase (tHMG1). Partial inhibition of squalene epoxidase by terbinafine further increased squalene production by up to 1.9-fold (756 ± 36 mg/L). Furthermore, squalene production of 2011 ± 75 or 1026 ± 37 mg/L was obtained from 5-L fed-batch fermentations in the presence or absence of terbinafine supplementation, respectively. These results suggest that the Y2805 strain has potential as a new alternative source of squalene production.     

High yield production of four-carbon dicarboxylic acids by metabolically engineered <Emphasis Type="Italic">Escherichia coli</Emphasis>

Several metabolic engineered Escherichia coli strains were constructed and evaluated for four-carbon dicarboxylic acid production. Fumarase A, fumarase B and fumarase C single, double and triple mutants were constructed in a ldhA adhE mutant background overexpressing the pyruvate carboxylase from Lactococcus lactis. All the mutants produced succinate as the main four-carbon (C4) dicarboxylic acid product when glucose was used as carbon source with the exception of the fumAC and the triple fumB fumAC deletion strains, where malate was the main C4-product with a yield of 0.61–0.67 mol (mole glucose)^?1. Additionally, a mdh mutant strain and a previously engineered high-succinate-producing strain (SBS550MG-Cms pHL413-Km) were investigated for aerobic malate production from succinate. These strains produced 40.38 mM (5.41 g/L) and 50.34 mM (6.75 g/L) malate with a molar yield of 0.53 and 0.55 mol (mole succinate)^?1, respectively. Finally, by exploiting the high-succinate production capability, the strain SBS550MG-Cms243 pHL413-Km showed significant malate production in a two-stage process from glucose. This strain produced 133 mM (17.83 g/L) malate in 47 h, with a high yield of 1.3 mol (mole glucose)^?1 and productivity of 0.38 g L^?1 h^?1.     

<Emphasis Type="SmallCaps">l</Emphasis>-Serine overproduction with minimization of by-product synthesis by engineered <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

The direct fermentative production of l-serine by Corynebacterium glutamicum from sugars is attractive. However, superfluous by-product accumulation and low l-serine productivity limit its industrial production on large scale. This study aimed to investigate metabolic and bioprocess engineering strategies towards eliminating by-products as well as increasing l-serine productivity. Deletion of alaT and avtA encoding the transaminases and introduction of an attenuated mutant of acetohydroxyacid synthase (AHAS) increased both l-serine production level (26.23 g/L) and its productivity (0.27 g/L/h). Compared to the parent strain, the by-products l-alanine and l-valine accumulation in the resulting strain were reduced by 87 % (from 9.80 to 1.23 g/L) and 60 % (from 6.54 to 2.63 g/L), respectively. The modification decreased the metabolic flow towards the branched-chain amino acids (BCAAs) and induced to shift it towards l-serine production. Meanwhile, it was found that corn steep liquor (CSL) could stimulate cell growth and increase sucrose consumption rate as well as l-serine productivity. With addition of 2 g/L CSL, the resulting strain showed a significant improvement in the sucrose consumption rate (72 %) and the l-serine productivity (67 %). In fed-batch fermentation, 42.62 g/L of l-serine accumulation was achieved with a productivity of 0.44 g/L/h and yield of 0.21 g/g sucrose, which was the highest production of l-serine from sugars to date. The results demonstrated that combined metabolic and bioprocess engineering strategies could minimize by-product accumulation and improve l-serine productivity.     

High-level productivity of <Emphasis Type="Italic">α,ω</Emphasis>-dodecanedioic acid with a newly isolated <Emphasis Type="Italic">Candida viswanathii</Emphasis> strain

α,ω-Dicarboxylic acids (DC) are versatile chemical intermediates with different chain lengths, which are well-known as polymer building block. In this work, a new strain with high productivity of DC was isolated from oil-contaminated soil. Based on the morphology and phylogenetic analyses of the internal transcribed spacer sequences, it was characterized as Candida viswanathii. It was found that the contribution of carbon flux to the cell growth and DC production from n-dodecane could be regulated by the sucrose and yeast extract concentrations in the medium, and besides the broth pH, a suitable proportioning of sucrose and yeast extract was the key to achieve the optimal transition from cell growth phase to DC production phase. By optimizing culture conditions in a 7.5-L bioreactor, a higher DC productivity of 1.59 g·L^?1 h^?1 with a corresponding concentration of 181.6 g/L was obtained. After the purification of DC from the culture, the results from gas chromatography–mass spectrometry, infrared spectroscopy and ¹H-NMR showed that α,ω-dodecanedioic acid (DC₁₂) was the major product of C. viswanathii ipe-1 using pure n-dodecane as substrate. For the first time, we reported that a high productivity of DC₁₂ could be produced by C. viswanathii.     

Whole-cell Immobilization of Engineered <Emphasis Type="Italic">Escherichia coli</Emphasis> JY001 with Barium-alginate for Itaconic Acid Production

Itaconic acid is an important organic acid and a major component of various polymers. It is used in resins, superabsorbent polymers, and substitutes for petrochemicalbased monomers such as acrylic and methacrylic acids. Itaconic acid is primarily produced by the fungus Aspergillus terreus, which yields a high titer with albeit long fermentation period and by-products. In our previous study, Escherichia coli JY001 was reported to produce itaconic acid using citric acid in whole-cell reaction resulting in higher itaconic acid productivity with less by-products formation. The present study aimed to increase whole-cell enzyme stability and reusability, via immobilization of E. coli JY001 using barium-alginate beads. We optimized the cations, temperature, pH, alginate, BaCl₂ concentration, cell density per bead, and CTAB content to improve transfer rate of substrates and products. Under the optimized conditions, immobilized whole cells were stable for four repeated cycles of itaconic acid production. The present results would strengthen the basis for a continuous itaconic acid production.     

Bio-Based Succinate Production from <Emphasis Type="Italic">Arundo donax</Emphasis> Hydrolysate with the New Natural Succinic Acid-Producing Strain <Emphasis Type="Italic">Basfia succiniciproducens</Emphasis> BPP7

Bio-based succinic acid production from lignocellulosic biomass is one of the attractive and prominent alternative technologies to overcome issues associated with the utilization of fossil sources. In this context, it is necessary to find new microorganisms that are able to efficiently ferment this recalcitrant feedstock. The ecological approach developed in this study enabled the isolation of Basfia succiniciproducens BPP7 from a complex rumen ecosystem. This new wild-type strain was able to synthesize up to 6.06 ± 0.05 g/L of succinate (corresponding to 0.84 ± 0.017 g of succinate per gram of consumed glucose + xylose and to 0.14 ± 0.001 g of succinate per gram of glucans + xylans present in the biomass before hydrolysis) from Arundo donax hydrolysate in separate hydrolysis and fermentation (SHF) experiments. Higher titers of succinic acid were obtained through the optimization of growth conditions. The optimal medium composition identified on the smaller scale was then used for 2.5-L batch experiments, which used A. donax hydrolysate and yeast extract as the main C and N sources, respectively. A maximal titer of 9.4 ± 0.4 g/L of succinic acid was obtained after 24 h. The overall results clearly demonstrate the potential of B. succiniciproducens BPP7 for succinate production.