Production of butanol and isopropanol with an immobilized <Emphasis Type="Italic">Clostridium</Emphasis>

Clostridium beijerinckii optinoii is a Clostridium species that produces butanol, isopropanol and small amounts of ethanol. This study compared the performances of batch and continuous immobilized cell fermentations, investigating how media flow rates and nutritional modification affected solvent yields and productivity. In 96-h batch cultures, with 80 % of the 30 g L^?1 glucose consumed in synthetic media, solvent concentration was 9.45 g L^?1 with 66.0 % as butanol. In a continuous fermentation using immobilized C. beijerinckii optinoii cells, also with 80 % of 30 g L^?1 glucose utilization, solvent productivity increased to 1.03 g L^?1 h^?1. Solvent concentration reached 12.14 g L^?1 with 63.0 % as butanol. Adjusting the dilution rate from 0.085 to 0.050 h^?1 to allow extended residence time in column was required when glucose concentration in fresh media was increased from 30 to 50 g L^?1. When acetate was used to improve the buffer capacity in media, the solvent concentration reached 12.70 on 50 g L^?1 glucose. This continuous fermentation using immobilized cells showed technical feasibility for solvent production.     

Enhanced citric acid production by a yeast <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis> over-expressing a pyruvate carboxylase gene

In this study, after the expression of a pyruvate carboxylase gene (PYC) cloned from Meyerozyma guilliermondii in a marine-derived yeast Yarrowia lipolytica SWJ-1b, a transformant PG86 obtained had much higher PYC activity than Y. lipolytica SWJ-1b. At the same time, the PYC gene expression and citric acid (CA) production by the transformant PG86 were also greatly enhanced. When glucose concentration in the medium was 60.0 g L^?1, CA concentration formed by the transformant PG86 was 34.02 g L^?1, leading to a CA yield of 0.57 g g^?1 of glucose. During a 10-L fed-batch fermentation, the final concentration of CA was 101.0 ± 1.3 g L^?1, the yield was 0.89 g g^?1 of glucose, the productivity was 0.42 g L^?1 h^?1 and only 5.93 g L^?1 reducing sugar was left in the fermented medium within 240 h of the fed-batch fermentation. HPLC analysis showed that most of the fermentation products were CA.     

Engineering rTCA pathway and C4-dicarboxylate transporter for <Emphasis Type="SmallCaps">l</Emphasis>-malic acid production

l-Malic acid is an important component of a vast array of food additives, antioxidants, disincrustants, pharmaceuticals, and cosmetics. Here, we presented a pathway optimization strategy and a transporter modification approach to reconstruct the l-malic acid biosynthesis pathway and transport system, respectively. First, pyruvate carboxylase (pyc) and malate dehydrogenase (mdh) from Aspergillus flavus and Rhizopus oryzae were combinatorially overexpressed to construct the reductive tricarboxylic acid (rTCA) pathway for l-malic acid biosynthesis. Second, the l-malic acid transporter (Spmae) from Schizosaccharomyces pombe was engineered by removing the ubiquitination motification to enhance the l-malic acid efflux system. Finally, the l-malic acid pathway was optimized by controlling gene expression levels, and the final l-malic acid concentration, yield, and productivity were up to 30.25 g L^?1, 0.30 g g^?1, and 0.32 g L^?1 h^?1 in the resulting strain W4209 with CaCO₃ as a neutralizing agent, respectively. In addition, these corresponding parameters of pyruvic acid remained at 30.75 g L^?1, 0.31 g g^?1, and 0.32 g L^?1 h^?1, respectively. The metabolic engineering strategy used here will be useful for efficient production of l-malic acid and other chemicals.     

Co-generation of ethanol and <Emphasis Type="SmallCaps">l</Emphasis>-lactic acid from corn stalk under a hybrid process

Background

Corn stover, as one important lignocellulosic material, has characteristics of low price, abundant output and easy availability. Using corn stover as carbon source in the fermentation of valuable organic chemicals contributes to reducing the negative environmental problems and the cost of production. In ethanol fermentation based on the hydrolysate of corn stover, the conversion rate of fermentable sugars is at a low level because the native S. cerevisiae does not utilize xylose. In order to increase the conversion rate of fermentable sugars deriving from corn stover, an effective and energy saving biochemical process was developed in this study and the residual xylose after ethanol fermentation was further converted to l-lactic acid.

Results

In the hybrid process based on the hydrolysate of corn stover, the ethanol concentration and productivity reached 50.50 g L^?1 and 1.84 g L^?1 h^?1, respectively, and the yield of ethanol was 0.46 g g^?1. The following fermentation of l-lactic acid provided a product titer of 21.50 g L^?1 with a productivity of 2.08 g L^?1 h^?1, and the yield of l-lactic acid was 0.76 g g^?1. By adopting a blank aeration before the inoculation of B. coagulans LA1507 and reducing the final cell density, the l-lactic acid titer and yield reached 24.25 g L^?1 and 0.86 g g^?1, respectively, with a productivity of 1.96 g L^?1 h^?1.

Conclusions

In this work, the air pumped into the fermentor was used as both the carrier gas for single-pass gas stripping of ethanol and the oxygen provider for the aerobic growth of B. coagulans LA1507. Ethanol was effectively separated from the fermentation broth, while the residual medium containing xylose was reused for l-lactic acid production. As an energy-saving and environmental-friendly process, it introduced a potential way to produce bioproducts under the concept of biorefinery, while making full use of the hydrolysate of corn stover.

     

Biological CO<Subscript>2</Subscript> fixation using C<Emphasis Type="Italic">hlorella vulgaris</Emphasis> and its thermal characteristics through thermogravimetric analysis

The present research is focused on cultivation of microalgae strain Chlorella vulgaris for bio-fixation of CO₂ coupled with biomass production. In this regard, a single semi-batch vertical tubular photobioreactor and four similar photobioreactors in series have been employed. The concentration of CO₂ in the feed stream was varied from 2 to 12 % (v/v) by adjusting CO₂ to air ratio. The amount of CO₂ capture and algae growth were monitored by measuring decrease of CO₂ concentration in the gas phase, microalgal cell density, and algal biomass production rate. The results show that 4 % CO₂ gives maximum amount of biomass (0.9 g L^?1) and productivity (0.118 g L^?1 day^?1) of C. vulgaris in a single reactor. In series reactors, average productivity per reactor found to be 0.078 g L^?1 day^?1. The maximum CO₂ uptake for single reactor also found with 4 % CO_2, and it is around 0.2 g L^?1 day^?1. In series reactors, average CO₂ uptake is 0.13 g L^?1 day^?1 per reactor. TOC analysis shows that the carbon content of the produced biomass is around 40.67 % of total weight. The thermochemical characteristics of the cultivated C. vulgaris samples were analyzed in the presence of air. All samples burn above 200 °C and the combustion rate become faster at around 600 °C. Almost 98 wt% of the produced biomass is combustible in this range.     

<Emphasis Type="Italic">In vitro</Emphasis> sucrose concentration influences microtuber production and diosgenin content in white yam (<Emphasis Type="Italic">Dioscorea rotundata</Emphasis> Poir)

Dioscorea spp. is an important food crop in many countries and the source of the phytochemical diosgenin. Efficient microtuber production could provide source materials for farm-planting stock, for food markets, and for the production of high-diosgenin-producing cultivars. The first step in this study was optimizing the plant growth regulators for plantlet production, followed by a study of the effects of sucrose concentration on microtuber induction and diosgenin production. Significantly, more shoots (3.5) were produced at 4.65 μM (1 mg L^?1) kinetin (KIN), longer shoots (4.1 cm) were obtained at 2.46 μM (0.5 mg L^?1) indole-3-butyric acid (IBA), and root number (3.9) was significantly higher at 5.38 μM (1 mg L^?1) naphthalene acetic acid (NAA) than in other treatments. Increased sucrose concentrations in the optimized growth medium with 4.65 μM KIN and 5.38 μM NAA had significant effects on microtuber production (p < 0.01) and diosgenin content (p < 0.05). The most microtubers (6.2) were obtained with 100 g L^?1 sucrose, while those on 80 g L^?1 sucrose were the heaviest (0.7 g) and longest (7.4 mm). Microtubers formed in medium with 80 g L^?1 sucrose had significantly higher diosgenin content (3.64% [w/w]) than those in other sucrose treatments (< 2%) and was similar to that of field-grown parent tubers (3.79%). This result indicates an important role for sucrose in both microtuber growth and diosgenin production. Medium containing 4.65 μM KIN and 5.38 μM NAA is recommended for plantlet production, and medium containing 80 g L^?1 sucrose is recommended for microtuber and diosgenin production.     

Microbial community and physicochemical dynamics during the production of ‘Chicha’, a traditional beverage of Indigenous people of Brazil

The microbial community of artisanal corn fermentation called Chicha were isolated, purified and then identified using protein profile by Matrix Assisted Laser Desorption Ionization Time-of-Flight Mass Spectrometry (MALDI-TOF) and confirmed by partial ribosomal gene sequencing. Samples from Chicha beverage were chemically characterized by gas and liquid chromatography (HPLC and GC-MS). Aerobic mesophilic bacteria (AMB) (35.8% of total of isolated microorganisms), lactic acid bacteria (LAB) (21.6%) and yeast (42.6%) were identified. Species of the genera Klebsiella, Bacillus, Staphylococcus, Micrococcus, Enterobacter, and Weissella were identified. Rhodotorula mucilaginosa, Lodderomyces elongisporus, Candida metapsilosis, and C. bohicensis were the yeasts found. The LAB isolates detected were responsible for the high concentrations of lactic acid found during the fermentation process (1.2 g L^??1), which is directly related to the decrease in pH values (from 6.95 to 3.70). Maltose was the main carbohydrate detected during corn fermentation (7.02 g L^??1 with 36 h of fermentation). Ethanol was found in low concentrations (average 0.181 g L^??1), making it possible to characterize the beverage as non-alcoholic. Twelve volatile compounds were identified by gas chromatography; belonging to the groups acids, alcohols aldehydes, acetate and others. MALDI-TOF was successfully used for identification of microbiota. Weissella confusa and W. cibaria were detected in the final product (after 36 h of fermentation), W. confusa is often classified as probiotic and deserve further application studies.     

Improving the production yield and productivity of 1,3-dihydroxyacetone from glycerol fermentation using <Emphasis Type="Italic">Gluconobacter oxydans</Emphasis> NL71 in a compressed oxygen supply-sealed and stirred tank reactor (COS-SSTR)

In this study, a compressed oxygen gas supply was connected to a sealed aerated stirred tank reactor (COS-SSTR) bio-system, leading to a high-oxygen pressure bioreactor used to improve the bio-transformative performance in the production of 1,3-dihydroxyacetone (DHA) from glycerol using Gluconobacter oxydans NL71. A concentration of 301.2 ± 8.2 g L^?1 DHA was obtained from glycerol after 32 h of fed-batch fermentation in the COS-SSTR system. The volumetric productivity for this process was 9.41 ± 0.23 g L^?1 h^?1, which is presently the highest obtained level of glycerol bioconversion into DHA. These results show that the application of this bioreactor would enable microbial production of DHA from glycerol at the industrial scale.     

Sweet Sorghum Juice and Bagasse as Feedstocks for the Production of Optically Pure Lactic Acid by Native and Engineered <Emphasis Type="Italic">Bacillus coagulans</Emphasis> Strains

Sweet sorghum is a bioenergy crop that produces large amounts of soluble sugars in its stems (3–7 Mg ha^?1) and generates significant amounts of bagasse (15–20 Mg ha^?1) as a lignocellulosic feedstock. These sugars can be fermented not only to biofuels but also to bio-based chemicals. The market potential of the latter may be higher given the current prices of petroleum and natural gas. The yield and rate of production of optically pure d-(?)- and l-(+)-lactic acid as precursors for the biodegradable plastic polylactide was optimized for two thermotolerant Bacillus coagulans strains. Strain 36D1 fermented the sugars in unsterilized sweet sorghum juice at 50 °C to l-(+)-lactic acid (～150 g L^?1; productivity, 7.2 g L^?1 h^?1). B. coagulans strain QZ19-2 was used to ferment sorghum juice to d-(?)-lactic acid (～125 g L^?1; productivity, 5 g L^?1 h^?1). Carbohydrates in the sorghum bagasse were also fermented after pretreatment with 0.5 % phosphoric acid at 190 °C for 5 min. Simultaneous saccharification and co-fermentation of all the sugars (SScF) by B. coagulans resulted in a conversion of 80 % of available carbohydrates to optically pure lactic acid depending on the B. coagulans strain used as the microbial biocatalyst. Liquefaction of pretreated bagasse with cellulases before SScF (L + SScF) increased the productivity of lactic acid. These results show that B. coagulans is an effective biocatalyst for fermentation of all the sugars present in sweet sorghum juice and bagasse to optically pure lactic acid at high titer and productivity as feedstock for bio-based plastics.     

Exploiting mixtures of H<Subscript>2</Subscript>, CO<Subscript>2</Subscript>, and O<Subscript>2</Subscript> for improved production of methacrylate precursor 2-hydroxyisobutyric acid by engineered <Emphasis Type="Italic">Cupriavidus necator</Emphasis> strains

Current manufacturing of most bulk chemicals through petrochemical routes considerably contributes to common concerns over the depletion of fossil carbon sources and greenhouse gas emissions. Sustainable future production of commodities thus requires the shift to renewable feedstocks in combination with established or newly developed synthesis routes. In this study, the potential of Cupriavidus necator H16 for autotrophic synthesis of the building block chemical 2-hydroxyisobutyric acid (2-HIBA) is evaluated. A novel biosynthetic pathway was implemented by heterologous expression of the 2-hydroxyisobutyryl-coenzyme A (2-HIB-CoA) mutase from Aquincola tertiaricarbonis L108, relying on a main intermediate of strain H16’s C4 overflow metabolism, 3-hydroxybutyryl-CoA. The intention was to direct the latter to 2-HIBA instead or in addition to poly-3-hydroxybutyrate (PHB). Autotrophic growth and 2-HIBA (respectively, PHB) synthesis of wild-type and PHB-negative mutant strains were investigated producing maximum 2-HIBA titers of 3.2 g L^?1 and maximum specific 2-HIBA synthesis rates (q _2-HIBA) of about 16 and 175 μmol g^?1 h^?1, respectively. The obtained specific productivity was the highest reported to date for mutase-dependent 2-HIBA synthesis from heterotrophic and autotrophic substrates. Furthermore, expression of a G protein chaperone (MeaH) in addition to the 2-HIB-CoA mutase subunits yielded improved productivity. Analyzing the inhibition of growth and product synthesis due to substrate availability and product accumulation revealed a strong influence of 2-HIBA, when cells were cultivated at high titers. Nevertheless, the presented results imply that at the time the autotrophic synthesis route is superior to thus far established heterotrophic routes for production of 2-HIBA with C. necator.     

Application of sodium erythorbate to promote the growth of <Emphasis Type="Italic">Chlorella vulgaris</Emphasis>

Sodium erythorbate (NaE) is a common antioxidant in food processing. In this study, the abilities of NaE to reduce photosynthetic oxygen accumulation in culture medium and improve microalgal growth were evaluated using the green microalga Chlorella vulgaris and glucose as a reference. NaE (from 2.0 to 16.0 g L^?1) led to a lower accumulation of dissolved oxygen (DO) in a concentration-dependent manner. A significant negative correlation (p < 0.05) between the optical density (OD₆₈₀) and DO level suggested that algal growth was promoted by NaE through depleting oxygen in the medium. After 12 days of cultivation, maximum OD₆₈₀ and biomass were obtained with a NaE dosage of 8.0 g L^?1 (respectively, 3.99 and 6.26 times greater than in the control without NaE). Compared with this dosage group which maintained an appropriate low DO level (2 to 6 mg L^?1), higher dosage groups showed relatively little growth promotion due to an insufficiency of DO (<2 mg L^?1). When glucose was added into mixotrophic systems for C. vulgaris, to the same total carbon amount as NaE, DO fell rapidly to less than 2 mg L^?1 owing to its greater consumption (43.9%) compared to that of NaE (16.7%). Furthermore, in the NaE treatment, the pigment contents, cell density, and algal biomass were, respectively, 4.17 to 4.44 times, 2.67 times, and 1.21 times greater than in the glucose treatment. These findings indicate that algal autotrophic growth could be enhanced effectively by NaE through the moderate control of DO.     

Cultivation of <Emphasis Type="Italic">Chlorella vulgaris</Emphasis> with swine wastewater and potential for algal biodiesel production

In this study, an alga-based simultaneous process of treating swine wastewater (SWW) and producing biodiesel was explored. Chlorella vulgaris (UTEX-265) was employed as a model species, and a SWW-based medium was prepared by dilution with tap water. Chlorella vulgaris grew well in the SWW-based medium, and at optimum dilution ratios, it exceeded the conventional culture medium in terms of biomass concentration and productivity. In eightfold diluted SWW, which supported the maximum growth, biomass productivity was 0.247 g L^?1 day^?1, while the productivity was merely 0.165 g L^?1 day^?1 in standard tris-acetate-phosphorous (TAP) algal medium. In addition, fatty acid methyl ester (FAME) productivity was greater in the SWW-based medium (0.067 versus 0.058 g L^?1 day^?1). This enhanced productivity resulted in more than 95 % removal of both nitrogen and phosphorous. All these show that C. vulgaris cultivation is indeed possible in a nutrient-rich wastewater with appropriate dilution, and in so doing, the wastewater can effectively be treated.     

Carbon dioxide and poultry waste utilization for production of polyhydroxyalkanoate biopolymers by <Emphasis Type="Italic">Nostoc muscorum</Emphasis> Agardh: a sustainable approach

The new paradigm is to view wastes as resources for sustainable development. In this regard, the feasibility of poultry waste and CO₂ utilization for cultivation of a filamentous nitrogen-fixing cyanobacterium, Nostoc muscorum Agardh, was investigated for production polyhydroxyalkanoates, the biodegradable polymers. This cyanobacterium showed profound rise in biomass yield with up to 10 % CO₂ supply in airstream with an aeration rate of 0.1 vvm. Maximum biomass yield of 1.12 g L^?1 was recorded for 8 days incubation period, thus demonstrating a CO₂ biofixation rate of 0.263 g L^?1 day^?1 at 10 % (v/v) CO₂-enriched air. Poultry litter (PL) supplementation also had a positive impact on the biomass yield. The nutrient removal efficiency of N. muscorum was reflected in the significant reduction in nutrient load of PL over the experimental period. A maximum poly(3-hydroxybutyric acid-co-3-hydroxyvaleric acid) [P(3HB-co-3HV)] copolymer yield of 774 mg L^?1 (65 % of dry cell wt.), the value almost 11-fold higher than the control, was recorded in 10 g L^?1 PL-supplemented cultures with 10 % CO₂ supply under the optimized condition, thus demonstrating that N. muscorum has good potential for CO₂ biomitigation and poultry waste remediation while simultaneously producing eco-friendly polymers.     

Xylitol production by genetically modified industrial strain of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> using glycerol as co-substrate

Xylitol is commercially used in chewing gum and dental care products as a low calorie sweetener having medicinal properties. Industrial yeast strain of S. cerevisiae was genetically modified to overexpress an endogenous aldose reductase gene GRE3 and a xylose transporter gene SUT1 for the production of xylitol. The recombinant strain (XP-RTK) carried the expression cassettes of both the genes and the G418 resistance marker cassette KanMX integrated into the genome of S. cerevisiae. Short segments from the 5′ and 3′ delta regions of the Ty1 retrotransposons were used as homology regions for integration of the cassettes. Xylitol production by the industrial recombinant strain was evaluated using hemicellulosic hydrolysate of the corn cob with glucose as the cosubstrate. The recombinant strain XP-RTK showed significantly higher xylitol productivity (212 mg L^?1 h^?1) over the control strain XP (81 mg L^?1 h^?1). Glucose was successfully replaced by glycerol as a co-substrate for xylitol production by S. cerevisiae. Strain XP-RTK showed the highest xylitol productivity of 318.6 mg L^?1 h^?1 and titre of 47 g L^?1 of xylitol at 12 g L^?1 initial DCW using glycerol as cosubstrate. The amount of glycerol consumed per amount of xylitol produced (0.47 mol mol^?1) was significantly lower than glucose (23.7 mol mol^?1). Fermentation strategies such as cell recycle and use of the industrial nitrogen sources were demonstrated using hemicellulosic hydrolysate for xylitol production.     

Improved production of <Emphasis Type="Italic">Oroxylum indicum</Emphasis> (L.) Kurz by altering the salts of the medium

The present study was conducted to test the effects of KNO₃, KH₂PO₄, and CaCl₂ on shoot multiplication, root proliferation, and accumulation of phytochemicals in in vitro cultures of Oroxylum indicum. The results indicate that modifying the MS salt formulation in relation to particular inorganic nutrients highly affected shoot multiplication, root proliferation, and accumulation of flavonoids in in vitro cultures. A concentration of 0.60 g L^?1 CaCl₂ resulted in the highest frequency of shoot regeneration (5.6 shoots per explant). A concentration of 0.40 g L^?1 CaCl₂ resulted in the highest frequency of root regeneration (7.8 roots per shoot). Modifications of the concentrations of inorganic salts were also found to be advantageous for production media for both multiple shoots and shoot-derived root in vitro cultures. Multiple shoots generated on shoot induction medium with a concentration of 0.60 g L^?1 CaCl₂ and roots generated on root induction medium with a concentration of 1.5 g L^?1 KNO₃ yielded about a five times higher flavonoid level than cultures generated on control medium respectively.     

Enhancing ethanol production from cellulosic sugars using <Emphasis Type="Italic">Scheffersomyces (Pichia) stipitis</Emphasis>

Studies were performed on the effect of CaCO₃ and CaCl₂ supplementation to fermentation medium for ethanol production from xylose, glucose, or their mixtures using Scheffersomyces (Pichia) stipitis. Both of these chemicals were found to improve maximum ethanol concentration and ethanol productivity. Use of xylose alone resulted in the production of 20.68 ± 0.44 g L^?1 ethanol with a productivity of 0.17 ± 0.00 g L^?1 h^?1, while xylose plus 3 g L^?1 CaCO₃ resulted in the production of 24.68 ± 0.75 g L^?1 ethanol with a productivity of 0.21 ± 0.01 g L^?1 h^?1. Use of xylose plus glucose in combination with 3 g L^?1 CaCO₃ resulted in the production of 47.37 ± 0.55 g L^?1 ethanol (aerobic culture), thus resulting in an ethanol productivity of 0.39 ± 0.00 g L^?1 h^?1. These values are 229 % of that achieved in xylose medium. Supplementation of xylose and glucose medium with 0.40 g L^?1 CaCl₂ resulted in the production of 44.84 ± 0.28 g L^?1 ethanol with a productivity of 0.37 ± 0.02 g L^?1 h^?1. Use of glucose plus 3 g L^?1 CaCO₃ resulted in the production of 57.39 ± 1.41 g L^?1 ethanol under micro-aerophilic conditions. These results indicate that supplementation of cellulosic sugars in the fermentation medium with CaCO₃ and CaCl₂ would improve economics of ethanol production from agricultural residues.     

Unexpected survival of sharptooth catfish <Emphasis Type="Italic">Clarias gariepinus</Emphasis> (Burchell 1822) during acute rotenone toxicity trials will complicate management of invasions

The sharptooth catfish Clarias gariepinus is an emerging global invader for which control strategies might include the use of piscicides such as rotenone. Experimental exposure demonstrated that C. gariepinus was less susceptible to rotenone than most other fish species, with unexpected survival observed at rotenone concentrations of 87.5 and 100 µg L^?1. C. gariepinus were also observed exhibiting avoidance behaviour to rotenone treated water and were found to be capable of recovering from rotenone exposure. As such, effective eradication might not be attainable even at a dose exceeding 100 µg L^?1 with exposures of longer than 24 h. This exposure scenario may pose an unacceptable risk to non-target fauna and highlights the difficulty associated with managing current and future invasions.     

Process Engineering for High-Cell-Density Cultivation of Lipid Rich Microalgal Biomass of <Emphasis Type="Italic">Chlorella</Emphasis> sp. FC2 IITG

In the present study, process engineering strategy was applied to achieve lipid-rich biomass with high density of Chlorella sp. FC2 IITG under photoautotrophic condition. The strategy involved medium optimization, intermittent feeding of limiting nutrients, dynamic change in light intensity, and decoupling growth and lipid induction phases. Medium optimization was performed using combinations of artificial neural network or response surface methodology with genetic algorithm (ANN-GA and RSM-GA). Further, a fed-batch operation was employed to achieve high cell density with intermittent feeding of nitrate and phosphate along with stepwise increase in light intensity. Finally, mutually exclusive biomass and lipid production phases were decoupled into two-stage cultivation process: biomass generation in first stage under nutrient sufficient condition followed by lipid enrichment through nitrogen starvation. The key findings were as follows: (i) ANN-GA resulted in an increase in biomass titer of 157 % (0.95 g L^?1) in shake flask and 42.8 % (1.0 g L^?1) in bioreactor against unoptimized medium at light intensity of 20 μE m^?2 s^?1; (ii) further optimization of light intensity in bioreactor gave significantly improved biomass titer of 5.6 g L^?1 at light intensity of 250 μE m^?2 s^?1; (iii) high cell density of 13.5 g L^?1 with biomass productivity of 675 mg L^?1 day^?1 was achieved with dynamic increase in light intensity and intermittent feeding of limiting nutrients; (iv) finally, two-phase cultivation resulted in biomass titer of 17.7 g L^?1 and total lipid productivity of 313 mg L^?1 day^?1 which was highest among Chlorella sp. under photoautotrophic condition.     

Promotion of shoot regeneration of <Emphasis Type="Italic">Swertia chirata</Emphasis> by biosynthesized silver nanoparticles and their involvement in ethylene interceptions and activation of antioxidant activity

A complete protocol for the in vitro induction of Eclipta alba tetraploids has been optimized to enhance the wedelolactone content, an anti-cancerous compound. The effects of different concentrations of colchicine (0, 0.01, 0.05, 0.1, 0.2 and 0.3%; w/v) along with treatment durations (12, 24, 36 and 48 h) were investigated on shoot tip (ST) and nodal segment (NS). The treated explants were then incubated on Murashige and Skoog (MS) medium having 1.5 mg L^?1 N⁶-benzylaminopurine and 0.5 mg L^?1 α-napthalene acetic acid for shoot regeneration and afterward root was induced on 1.0 mg L^?1 indole-3-acetic acid enriched ½MS medium. The tetraploids of E. alba were proficiently induced by the treatment of 0.1% colchicine for 24 h. The highest tetraploid induction efficiency was obtained from ST (30.56%) in comparison to the NS (22.22%). Analysis by spectrophotometry and flow cytometry showed that colchicine treated plants contained higher quantity of DNA than diploid plants. Cytological studies demonstrated doubled the chromosome number in tetraploids (2n?=?4x?=?44) than diploids (2n?=?2x?=?22). The ploidy level enhancement lead to alteration of other traits, like increased plant height, stem diameter, leaf size, stomatal size and chlorophyll content. As determined through high performance thin-layer chromatography, the ultimate achievement of this technique is the higher accumulation of wedelolactone in tetraploid plants (300.32 µg g^?1 dry weight) in evaluation to in vitro diploid (131.31 µg g^?1 dry weight) and in vivo diploid mother plants (93.26 µg g^?1 dry weight), thus improving the pharmaceutical value of E. alba.     

Non-water miscible ionic liquid improves biocatalytic production of geranyl glucoside with <Emphasis Type="Italic">Escherichia coli</Emphasis> overexpressing a glucosyltransferase

Whole cells of Escherichia coli overexpressing a glucosyltransferase from Vitis vinifera were used for the glucosylation of geraniol to geranyl glucoside. A high cell density cultivation process for the production of whole-cell biocatalysts was developed, gaining a dry cell mass concentration of up to 67.6 ± 1.2 g L^?1 and a glucosyltransferase concentration of up to 2.7 ± 0.1 g protein L^?1 within a process time of 48 h. Whole-cell batch biotransformations in milliliter-scale stirred-tank bioreactors showed highest conversion of geraniol at pH 7.0 although the pH optimum of the purified glucosyltransferase was at pH 8.5. The biocatalytic batch process performance was improved significantly by the addition of a water-immiscible ionic liquid (N-hexylpyridinium bis(trifluoromethylsulfonyl)imid) for in situ substrate supply. The so far highest final geranyl glucoside concentration (291 ± 9 mg L^?1) and conversion (71 ± 2 %) reported for whole-cell biotransformations of geraniol were achieved with 5 % (v/v) of the ionic liquid.