Continuous 2-keto-gluconic acid (2KGA) production from corn starch hydrolysate by Pseudomonas fluorescens AR4

A continuous fermentation process for 2-keto-gluconic acid (2KGA) production from cheap raw material corn starch hydrolysate was developed using the strain Pseudomonas fluorescens AR4. The dilution rate and feeding glucose concentration had a significant effect on the cell concentrations, glucose utilization and 2KGA production performance. The optimal operating factors were obtained as: 0.065 h⁻¹ of dilution rate, 180 g/L of feeding glucose concentration, and 16 h of batch fermentation time as the starting point. Under these conditions, the steady state had the 135.92 g/L of produced 2KGA concentration, 8.83 g/L.h of average volumetric productivity, and 0.9510 g/g of yield. In conclusion, the proposed efficient and stable continuous fermentation process for 2KGA production by the strain P. fluorescens AR4 is potentially competitive for industrial production from corn starch hydrolysate in terms of 2KGA productivity and yield.     

Xylose-based hydrolysate from eucalyptus extract as feedstock for poly(lactate-co-3-hydroxybutyrate) production in engineered Escherichia coli

Woody extract-derived hemicellulosic hydrolysate, which was obtained from dissolving pulp manufacturing, was utilized as feedstock for the production of poly(lactate-co-3-hydroxybutyrate) [P(LA-co-3HB)] in engineered Escherichia coli. The hydrolysate was composed of mainly xylose and galactose, and contained impurities mainly acetate, which was found to inhibit the polymer synthesis rather than the cell growth. Thus, acetate and other impurities were removed through active charcoal and ion-exchange columns. Using the purified hydrolysate, P(LA-co-3HB) was successfully produced (cell dry weight 8.6 g/L, polymer concentration 5.4 g/L, LA fraction 5.5 mol%, polymer content 62.4%), the amount of which was comparable to that obtained using reagent grade xylose and galactose. Therefore, the hydrolysate from woody extract is considered as an abundant, inexpensive and efficient feedstock applicable to consolidated process for P(LA-co-3HB) production, when the removal of acetic acid was satisfactorily accomplished.     

Decanter cake waste as a renewable substrate for biobutanol production by Clostridium beijerinckii

The aim of this study was to determine if decanter cake waste from a palm oil mill could be used as a renewable substrate for biobutanol production. Decanter cake waste was first hydrolyzed to fermentable sugars by nitric acid and detoxified by activated-charcoal. The detoxified hydrolysate supplemented with whey protein and ammonium sulfate as cheap nitrogen sources, was used for butanol production by growing cells of Clostridium beijerinckii. The detoxified hydrolysate was also used as a co-substrate for direct conversion of butyric acid to butanol in a nitrogen-free medium. By these two steps, C. beijerinckii produced 3.42 g/L of butanol with a yield of 0.28 C-mol butanol/C-mol carbon in the first step and produced 6.94 g/L of butanol with a yield of 0.47 C-mol butanol/C-mol carbon in the second step. This study has showed that decanter cake waste could serve as a low-cost substrate for biobutanol production.     

Enhanced ethanol production via fermentation of rice straw with hydrolysate-adapted Candida tropicalis ATCC 13803

Neutralized hydrolysate and pretreated rice straw obtained from a 2% (w/v) sulfuric acid pretreatment were mixed at 10% (w/v) and subjected to simultaneous saccharification and co-fermentation (SSCF), with cellulase, β-glucosidase, and Candida tropicalis cells at 15 FPU/g-ds, 15 IU/g-ds and 1 × 10⁹ cells/ml, respectively. A 36-h SSCF with adapted cells resulted in YP/S and ethanol volumetric productivity of 0.36 g/g and 0.57 g/l/h, respectively. In addition to ethanol, insignificant amounts of glycerol and xylitol were also produced. Adapted C. tropicalis cells produced nearly 1.6 times more ethanol than non-adapted cells. Ethanol yield (Yp/s), ethanol volumetric productivity and a xylitol concentration of 0.48 g/g, 0.33 g/l/h and 0.89 g/l, respectively, were produced from fermentation of remaining hydrolysate with adapted C. tropicalis cells. The 0.20 g/g ethanol yield and 77% production efficiency from SSCF of pretreated rice straw indicate scale-up potential for the process. This study demonstrated that C. tropicalis produced ethanol and xylitol from a mixed-sugar stream, although cell adaptation affected ethanol and xylitol yields. Scanning electron microscopy indicated agglomeration of cellulose microfibrils and globular deposition of lignin in acid-pretreated rice straw.     

Retinoid compounds associated with water blooms dominated by Microcystis species

Retinoic acids play a critical role in vital physiological processes and vertebrate development, and their derivatives can be produced by some cyanobacterial species into surface waters. This study presents important environmentally-relevant information on total retinoid-like activity of field cyanobacterial biomasses and their surrounding waters. Intracellular and extracellular levels of total retinoid-like activity and retinoic acids have been investigated at a set of independent sites with the occurrence of water bloom dominated by widespread species Microcystis aeruginosa. Twelve samples of biomass and surrounding water from seven localities affected by blooms were studied in comparison with samples from M. aeruginosa laboratory cultures. The method for biomass extraction was optimized and final extracts and samples of surrounding water concentrated by solid phase extraction were assessed using in vitro reporter gene bioassay and chemical analyses for all-trans-retinoic acid (ATRA), 9-cis retinoic acid (9-cis RA) and microcystins RR, LR and YR. Methanol was the most efficient solvent for the extraction of compounds with retinoid-like activity. An in vitro bioassay with the P19/A15 transgenic cell line revealed retinoid-like activity in all cyanobacterial biomasses in the range of 356–2838 ng of retinoid acid equivalents (REQ)/g dry mass (dm), while only three of surrounding water samples exhibited detectable retinoid-like activity, in the range of 12.8–28.7 ng REQ/L. Microcystins were detected in all samples, but they elicited no detectable retinoid-like activity up to 10 mg/L. Chemical analyses detected concentrations up to 340 ng/g dm of all-trans-retinoic acid (ATRA) and 84 ng/g dm 9-cis retinoic acid (9-cis RA) in bloom extracts, and up to 19 ng/L ATRA and 2.2 ng/L 9-cis RA in surrounding water. In most samples, ATRA and 9-cis RA contributed relatively little to the total REQs, which indicates the presence of significant amounts of other compounds with retinoic acid receptor-mediated modes of action. The impact of retinoid-like cyanobacterial metabolites could be of importance namely in smaller water bodies with dense water blooms and low dilution.     

Performance improvement of cephalosporin C fermentation by Acremonium chrysogenum with DO-Stat based strategy of co-feeding soybean oil and glucose

Cephalosporin C (CPC) fermentation by Acremonium chrysogenum featured with two major problems: (1) high raw materials cost (low CPC yield from soybean oil) and (2) low oxygen transfer rate between gaseous/aqueous phases leading to low CPC productivity and quality instability of CPC fermentation product due to the accumulation of deacetoxycephalosporin C (DAOC). To solve the problems, in this study, we proposed a novel DO-Stat based co-substrates feeding strategy by simultaneously supplementing soybean oil and glucose, and testified the effectiveness of the strategy in a 7 L bioreactor. The CPC fermentation performance were significantly improved when co-feeding soybean oil and glucose at a weight ratio of 1:0.7, as compared with those when feeding pure soybean oil: (1) final CPC concentration and yield reached higher levels of 37 g/L and 23.5%, the increments were 46% and 82%, respectively; (2) oxygen transfer rate was largely improved, oil consumption rate and CPC productivity were enhanced by 31% and 136%, respectively; and (3) DO could be controlled at adequately high levels so that DAOC accumulation could be minimized and the quality of CPC fermentation product be ensured. The proposed strategy showed application potential in improving the economics of industrial CPC productions.     

A simple approach for the selective enzymatic synthesis of dilauroyl maltose in organic media

A selective synthesis of dilauroyl maltose was developed using lipase-catalyzed condensation of lauric acid and maltose in two-solvent mixtures. The characteristics of different solvent combination were tested and it was found that the combination of acetone with n-hexane has a good selectivity for the synthesis of dilauroyl maltose. The highest diester conversion of 69% (i.e. 36.5 g/L of dilauroyl maltose) was obtained under optimal conditions: 25.65 g/L maltose, 60 g/L lauric acid, 60 g/L molecular sieve and 10 g/L lipase at 150 rpm and 50 °C for 72 h in 10 mL of mixed solvent of acetone:n-hexane (60:40, v/v).     

Ram horn hydrolysate as enhancer of xanthan production in batch culture of Xanthomonas campestris EBK-4 isolate

Ram horns are waste materials from the meat industry. The objective of this study was to investigate the effects of various concentrations of ram horn (RHH) hydrolysate as a supplement on xanthan production from a local isolate of Xanthomonas campestris EBK-4 in batch culture. Firstly, ram horn hydrolysate was reproduced. The production of xanthan was influenced by the RHH. RHH supplementation promoted X. campestris growth, accelerated substrate metabolism, and increased xanthan production. A concentration of 3% v/v RHH resulted in the highest xanthan concentration (25.6 g/L) in 48 h. This value was 49% higher than that of control medium (17.1 g/L) in the absence of RHH in 60 h. The pyruvate content increased with increasing RHH concentrations. The application of RHH resulted in enhancement of xanthan production.     

Metabolic engineering of Escherichia coli for the production of 5-aminovalerate and glutarate as C5 platform chemicals

5-Aminovalerate (5AVA) is the precursor of valerolactam, a potential building block for producing nylon 5, and is a C5 platform chemical for synthesizing 5-hydroxyvalerate, glutarate, and 1,5-pentanediol. Escherichia coli was metabolically engineered for the production of 5-aminovalerate (5AVA) and glutarate. When the recombinant E. coli WL3110 strain expressing the Pseudomonas putida davAB genes encoding delta-aminovaleramidase and lysine 2-monooxygenase, respectively, were cultured in a medium containing 20 g/L of glucose and 10 g/L of l-lysine, 3.6 g/L of 5AVA was produced by converting 7 g/L of l-lysine. When the davAB genes were introduced into recombinant E. coli strainXQ56allowing enhanced l-lysine synthesis, 0.27 and 0.5 g/L of 5AVA were produced directly from glucose by batch and fed-batch cultures, respectively. Further conversion of 5AVA into glutarate could be demonstrated by expression of the P. putida gabTD genes encoding 5AVA aminotransferase and glutarate semialdehyde dehydrogenase. When recombinant E. coli WL3110 strain expressing the davAB and gabTD genes was cultured in a medium containing 20 g/L glucose, 10 g/L l-lysine and 10 g/L α-ketoglutarate, 1.7 g/L of glutarate was produced.     

Enhanced ethanol and chitosan production from wheat straw by Mucor indicus with minimal nutrient consumption

Recently, Mucor indicus was introduced as a promising ethanol producing microorganism for fermentation of lignocellulosic hydrolysates, showing a number of advantages over Saccharomyces cerevisiae. However, high nutrient requirement is the main drawback of the fungus in efficient ethanol production from lignocelluloses. In this study, application of fungal extract as a potential nutrient source replacing all required nutrients in fermentation of wheat straw by M. indicus was investigated. Wheat straw was pretreated with N-methylmorpholine-N-oxide (NMMO) at 120 °C for 1–5 h prior to enzymatic hydrolysis. Hydrolysis yield was improved at least by 6-fold for 3 h pretreated straw compared with that of untreated one. A fungal extract was produced by autolysis of M. indicus biomass, an unavoidable byproduct of fermentation. Maximum free amino nitrogen (2.04 g/L), phosphorus (1.50 g/L), and total nitrogen (4.47 g/L) as well as potassium, magnesium, and calcium in the fungal extract were obtained by autolysis of the biomass at 50 °C and pH 5.0. The fungal extract as a nutrient-rich supplement substituted yeast extract and all other required minerals in fermentation and enhanced the ethanol yield up to 92.1% of the theoretical yield. Besides, appreciate amounts of chitosan were produced as another valuable product of the autolysis.     

Growth tolerance of Zygomycetes Mucor indicus in orange peel hydrolysate without detoxification

The capability of two zygomycetes strains, Mucor indicus and an isolate from tempeh (Rhizopus sp.), to grow on orange peel hydrolysate and their tolerance to its antimicrobial activity, was investigated. Both fungi, in particular M. indicus, tolerated up to 2% d-limonene in semi-synthetic media during cultivation in shake flasks, under aerobic as well as anaerobic conditions. The tolerance of M. indicus was also tested in a bioreactor, giving rise to varying results in the presence of 2% limonene. Furthermore, both strains were capable of consuming galacturonic acid, the main monomer of pectin, under aerobic conditions when no other carbon source was present. The orange peel hydrolysate was based on 12% (dry w/v) orange peels, containing d-limonene at a concentration of 0.6% (v/v), which no other microorganism has been reported to be able to ferment. However, the hydrolysate was utilised by M. indicus under aerobic conditions, resulting in production of 410 and 400 mg ethanol/g hexoses and 57 and 75 mg fungal biomass/g sugars from cultivations in shake flasks and a bioreactor, respectively. Rhizopus sp., however, was slow to germinate aerobically, and neither of the zygomycetes was able to consistently germinate in orange peel hydrolysate, under anaerobic conditions. The zygomycetes strains used in the present study demonstrated a relatively high resistance to the antimicrobial compounds present in orange peel hydrolysate, and they were capable of producing ethanol and biomass in the presence of limonene, particularly when cultivated with air supply.     

Production of lactic acid from soybean stalk hydrolysate with Lactobacillus sake and Lactobacillus casei

In order to make full use of soybean stalk produced in large quantity annually in China, a process is proposed for production of lactic acid from soybean stalk hydrolysate with Lactobacillus sake and Lactobacillus casei. Experiments were conducted using the proposed process and experimental results indicate that the potential of 242 mg (g stalk)⁻¹ fermentable sugar is released from hydrolysate through enzymatic saccharication with a saccharication of 51%. The main sugar released from pretreated soybean stalk through enzymatic hydrolysis was a mixture of glucose, xylose and cellobiose at a ratio of 3.9:1.7:1. Fermentation of soybean stalk hydrolysate by L. sake and L. casei yielded the lactic acid conversion of 48% and 56%, respectively, however, lactic acid conversion increased to 71% by co-inoculation of both strains. L. sake and L. casei were able to degrade glucose, but unable to completely assimilate xylose and cellobiose. The proposed process can be used to produce lactic acid from soybean stalk hydrolysate.     

Changes of ginsenosides in Korean red ginseng (Panax ginseng) fermented by Lactobacillus plantarum M1

To obtain microorganisms for the microbial conversion of ginsenosides in red ginseng powder (RGP), Lactobacillus species (M1–M4 and P1–P4) were isolated from commercial ginseng products. Strain M1 was determined to be L. plantarum by 16S rRNA sequencing. Red ginseng powder (RGP) fermented by L. plantarum M1 had a high total content of ginsenosides (142.4 mg/g) as compared to the control (121.8 mg/g). In particular, the ginsenoside metabolites Rg3, Rg5, Rk1, Compound K (CK), Rh1, and Rg2 showed a high level in the fermented RGP (65.5 mg/g) compared to the control (32.7 mg/g). During fermentation for 7 days, total sugar content decreased from 8.55 mg/g to 4 mg/g, uronic acid content reached its maximum (53.43 μg/g) at 3 days, and total ginsenoside content increased to 176.8 mg/g at 4 days. In addition, ginsenoside metabolites increased from 38.0 mg/g to 83.4 mg/g at 4 days of fermentation. Using everted instestinal sacs of rats, the fermented red ginseng showed a high transport level (10.3 mg of polyphenols/g sac) compared to non-fermented red ginseng (6.67 mg of polyphenols/g sac) after 1 h. These results confirm that fermentation with L. plantarum M1 is very useful for preparing minor ginsenoside metabolites while being safe for foods.     

Effect of lignocellulose degradation products on microbial biomass and lipid production by the oleaginous yeast Cryptococcus curvatus

This work investigated effects of lignocellulose degradation products on cell biomass and lipid production by Cryptococcus curvatus. Furfural was found to have the strongest inhibitory effect. For the three phenolic compounds tested, vanillin was the most toxic, while PHB and syringaldehyde showed comparable inhibitions in the concentration range of 0–1.0 g/L. Generally little significant differences on the relative cell biomass and lipid contents at the same concentrations of tested compounds were observed between glucose and xylose as a sole carbon source. At 1.0 g/L of furfural, the cell biomass and lipid content decreased by 78.4% and 61.0% for glucose as well as 72.0% and 59.3% for xylose, respectively. C. curvatus ceased to grow at concentrations of PHB over 1.0 g/L or vanillin over 1.5 g/L. The strain could survive in the presence of syringaldehyde up to 2.0 g/L for glucose or 1.5 g/L for xylose. The compounds’ negative impact was reduced by an increase in inoculum size and a 10% (v/v) seed was detected to be optimal for cell biomass and lipid production. The results demonstrated C. curvatus could effectively utilize most of the dominant monosaccharides and cellobiose existing in lignocellulosic biomass hydrolysate in the presence of toxic compounds.     

Hyaluronic acid production and molecular weight improvement by redirection of carbon flux towards its biosynthesis pathway

Hyaluronic acid (HA) production in Streptococcus zooepidemicus competes for the carbon source along with biomass formation, lactate formation (via glycolysis) and pentose phosphate pathway (PPP). In our studies, increase in HA molecular weight was observed by redirecting the carbon flux towards HA biosynthesis pathway by partially inhibiting the glycolytic pathway. Batch bioreactor (1.2 L) studies showed that with the addition of 25 μM sodium iodoacetate, 5 g/L tryptophan and 10 g/L pyruvate, which are glycolytic inhibitors, HA molecular weight increased to 3.2, 3.2 and 3.1 MDa respectively compared to control run (2.4 MDa). Yield coefficients Y_HA/S and Y_LA/S showed inverse relationship, indicating competition for glucose between HA and lactic acid formation. Addition of 5 g/L glutamine along with 25 μM sodium iodoacetate also increased the HA concentration to 5.0 g/L from 2.0 g/L in control run. Metabolic flux analysis studies show that concentration and molecular weight of HA is increased by decreasing carbon flux towards glycolysis and PPP and increasing carbon flux towards HA precursor formation. It was observed that specific growth rate of the cells correlated positively to the specific HA production rate and negatively to the molecular weight of HA produced. Addition of antioxidant tannic acid also increased molecular weight to 3.0 MDa.     

Optimization of ultrasound-assisted extraction conditions for total phenols with anti-hyperglycemic activity from Psidium guajava leaves

The high concentration of total phenolic compounds (TPC) in Psidium guajava leaf extracts (GvEx) is correlated to its anti-hyperglycemic activity. In this study, we established the optimum ultrasound extraction conditions for maximizing TPC yield. The response surface methodology (RSM) was employed for empirical model building. The maximum value of TPC (26.12%) was obtained at solvent to solid ratio (v/w) of 12.1, extraction temperature of 59.8 °C, and extraction time of 5.1 min. The anti-hyperglycemic activity of GvEx was compared to the commonly used diabetic drug acarbose. The IC₅₀ of GvEx for α-amylase and α-glucosidase inhibition was 50.5 μg/mL and 34.6 μg/mL, respectively. However, the IC₅₀ of acarbose for α-amylase and α-glucosidase inhibition was 95.3 μg/mL and 1075.2 μg/mL, respectively. In conclusion, GvEx obtained under optimum extraction conditions had higher anti-hyperglycemic activity than acarbose. In addition, the recommended extraction procedures for GvEx save time and are environmentally friendly.     

VFAs bioproduction from waste activated sludge by coupling pretreatments with Agaricus bisporus substrates conditioning

A novel strategy for improving volatile fatty acids (VFAs) bioproduction from waste activated sludge (WAS) was developed by coupling pretreatments with conditioning (CPC). Agaricus bisporus substrate (ABS) was used as external carbohydrate additive source of conditioning step. Pretreatment was studied in three ways: alkaline, alkaline-thermal and ultrasonic. WAS hydrolysis and protein degradation was distinctly improved by CPC treatments, resulting in a considerable enhancement of VFAs yield. The maximal VFAs yield was 614 ± 71, 712 ± 49 and 598 ± 19 mg COD/g VSS at pre-optimized alkaline, alkaline-thermal and ultrasonic CPC treatments, respectively, with an increase of 35%, 50% and 38% compared to the yields of pretreated WAS fermentation. Fourier transformed infrared spectroscopy and three-dimensional excitation-emission matrix fluorescence spectroscopy indicated that a synergistic effect occurred in co-digesting WAS and ABS. The conditioning of carbohydrate with feasible pretreatment provided large room for the digestibility improvement and the operation cost reduction in the whole WAS treatment system.     

Improved 2,3-butanediol production from corncob acid hydrolysate by fed-batch fermentation using Klebsiella oxytoca

Corncob acid hydrolysate, detoxed by sequently boiling, overliming and activated charcoal adsorption, was used for 2,3-butanediol production by Klebsiella oxytoca ACCC 10370. The effects of acetate in hydrolysate and pH on 2,3-butanediol production were investigated. It was found that acetic acid in hydrolysate inhibited the growth of K. oxytoca while benefited the 2,3-butanediol yield. With the increase in acetic acid concentration in medium from 0 to 4 g/l, the lag phase was prolonged and the specific growth rate decreased. The acetic acid inhibition on cell growth can be alleviated by adjusting pH to 6.3 prior to fermentation and a substrate fed-batch strategy with a low initial acetic acid concentration. Under the optimum condition, a maximal 2,3-butanediol concentration of 35.7 g/l was obtained after 60 h of fed-batch fermentation, giving a yield of 0.5 g/g reducing sugar and a productivity of 0.59 g/h l.     

Enhanced extraction genistein from pigeon pea [Cajanus cajan (L.) Millsp.] roots with the biotransformation of immobilized edible Aspergillus oryzae and Monacus anka and antioxidant activity evaluation

A new method of enhanced extraction genistein from pigeon pea [Cajanus cajan (L.) Millsp.] roots with the biotransformation of immobilized edible Aspergillus oryzae and Monacus anka, was investigated. It showed that immobilized Aspergillus oryzae and Monacus anka on sodium alginate effectively supported the highest genistein extraction yield by screening microorganism tests. After biotransformation process with immobilized Aspergillus oryzae and Monacus anka under 30 °C, pH 6.0, 2 days, liquid-solid ratio 12: 1 (mL/g), the extraction yield of genistein reached 1.877 mg/g, which was 2.65-fold to that of normal extraction yield. Moreover, IC₅₀ values of the extracts measured by DPPH-radical scavenging test and β-Carotene-linoleic acid bleaching test were 0.737 mg/mL and 0.173 mg/mL (control sample 1.117 mg/mL and 0.216 mg/mL), respectively. SOD (Super Oxygen Dehydrogenises) activity of the extracts treated with immobilized microorganism which was stronger than that of the untreated pigon pea roots (1.44 U/mg) at the concentration of protein (0.9375 μg/mL) was 1.83 U/mg. The developed method could be an alternative method for the enhanced extraction of genistein from plants and could be potentially applied in the food industry     

Degradation of phenol by a halotolerant strain of Penicillium chrysogenum

The lowest 50% lethal (effective) concentration, L(E)C₅₀, of phenol in a battery of seven microbiotests with species representing different trophic levels was 1–10 mg l⁻¹, classifying it as “toxic”. A phenol-degrading microorganism was isolated from soil samples of the salt mine of Clona in Portugal, after enrichment in the presence of phenol and high salt concentration. Based on cultural and morphological characteristics, the strain CLONA2 was identified as belonging to Penicillium chrysogenum. It was found to be a halotolerant fungus able to grow in a nutrient-rich medium with 5.8% NaCl. It degraded at least 300 mg l⁻¹ phenol as sole source of carbon and energy, without accumulation of intermediates. The samples were also tested for toxicity using the Microtox^® assay. Data showed that P. chrysogenum CLONA2 could be effectively utilized to reduce phenol toxicity. The results suggest also that phenol under saline conditions can be successfully mineralized by P. chrysogenum CLONA2.