Ionic liquids as selectors for controlling the crystallization nucleation of hen egg white lysozyme

Ionic liquids (ILs) have biomaterial applications and are used for protein crystallization. The effect of two imidazolium-based ILs, 1-butyl-3-methylimidazolium chloride ([C₄mim]Cl) and 1,3-dimethylimidazolium iodide ([dmim]I), on the nucleation kinetics of lysozyme was investigated by determining the nucleation induction time, and nucleation parameters were evaluated. The values of interfacial tension calculated for solutions with added 30 g/L ILs [C₄mim]Cl and [dmim]I, and without added ILs were 99.03, 109.7, and 107.3 mJ/m², respectively. Compared with solutions without IL addition, the critical free energy change, size, and molecular number of critical nuclei decreased and the nucleation rate increased after the addition of [C₄mim]Cl. In contrast, the critical free energy change, size, and molecular number of critical nuclei increased and the nucleation rate decreased after the addition of [dmim]I. These new findings provide insights into controlling lysozyme crystallization separation, and present ILs as potentially useful additives for controlling the crystallization of macromolecules.     

Promotive effect of 5-aminolevulinic acid on chlorophyll,antioxidative enzymes and photosynthesis of Pakchoi (<Emphasis Type="Italic">Brassica campestris</Emphasis> ssp<Emphasis Type="Italic">.</Emphasis><Emphasis Type="Italic">chinensis</Emphasis> var. communis Tsen et Lee)

The objective of this article is to study the effect of 5-aminolevulinic acid (ALA) and enhanced chlorophyll content, antioxidative enzymes and photosynthesis rate by foliar application of ALA. We evaluated three concentrations (control-distilled water, T1-50 mg l⁻¹, T2-150 mg l⁻¹, T3-250 mg l⁻¹) of ALA and seven cultivars, “Sanchidaye” (Sa-1), “Lichuandasuomian” (Li-1), “Aijiaohuang” (Ai-1), “Qingyou” No. 4 (Qi-1), “Aikang” No. 5 (Ak-1), “Hanxiao” (Ha-1) and “Shulv” (Sl-1). “Ak-1” showed strongest response of POD (peroxidase) enzyme activity (0.4 U g⁻¹ min⁻¹) in 250 mg l⁻¹ ALA solution. The highest CAT (catalase) activity (0.8 U g⁻¹ min⁻¹) after administration of 250 mg l⁻¹ ALA was observed in “Li-1”. Meanwhile, highest (1.42 mg l⁻¹) total chlorophyll content was also observed in “Ak-1”, when leaves were treated in 50 mg l⁻¹ ALA, “Li-1” and “Ai-1” showed strongest response of specific activity of superoxide dismutase (SOD) in 50 mg l⁻¹ and 50 mg l⁻¹ ALA. Two hundred and fifty milligram per milliliter of ALA-treatment significantly improved the net photosynthetic rate.     

High-frequency adventitious shoots regeneration from leaf of non-heading Chinese cabbage (<Emphasis Type="Italic">Brassica campestris</Emphasis> ssp. <Emphasis Type="Italic">chinensis</Emphasis>) cultured in vitro

The objective of the present work was selection of cultivar and suitable medium for regenerating shoots from leaf segments of non-heading Chinese cabbage. We evaluated six types of supplemented media with 2.0, 5.0 and 10.0 mg l⁻¹ 6-BA; 1.0 and 2.0 mg l⁻¹ TDZ; 0.1, 0.3, 0.5, 0.8 and 1.0 mg l⁻¹NAA; 3.0, 5.0 and 7.5 mg l⁻¹AgNO₃; 0.01 mg l⁻¹ 2–4, D and 4.0 mg l⁻¹ KT for shoot regeneration and six cultivars “Sanchidaye”, “Liuchuandasuomian”, “Qingyou 4”, “Liangbaiye”, “AiKang 5” and “Hanxiao F3”, furthermore for root formation three types of supplemented media with 0.2, 0.3, 0.5 mg l⁻¹ NAA, and for survival rate two types of base media: turf + vermiculite + manure (1:2:0.2) and soil + vermiculite (1:2). Culturing leaf segments on MS medium supplemented with 2 mg l⁻¹ TDZ; 0.5 mg l⁻¹ NAA and 7.5 mg l⁻¹ AgNO₃ gave the highest number of shoots per leaf segment (66) while roots were best formed on the medium supplemented with 0.2 mg l⁻¹ NAA. Survival rate was highest (61.6%) in the turf: vermiculite: manure (1:2:0.2) medium. The highest percentage of responding leaf segments, number of shoots per leaf segment, rooting percentage and survival rate were observed in “Liuchuandasuomian”. The plantlets were transferred to the soil and grown into mature plants in pots. These results could be used for preliminary selections of cultivars to transfer disease resistance (Bt) gene through agrobacterium in non-heading Chinese cabbage.     

Poly(3-hydroxybutyrate) synthesis from glycerol by a recombinant Escherichia coli arcA mutant in fed-batch microaerobic cultures

Poly(3-hydroxybutyrate) (PHB) synthesis was analyzed under microaerobic conditions in a recombinant Escherichia coli arcA mutant using glycerol as the main carbon source. The effect of several additives was assessed in a semi-synthetic medium by the ‘one-factor-at-a-time’ technique. Casein amino acids (CAS) concentration was an important factor influencing both growth and PHB accumulation. Three factors exerting a statistically significant influence on PHB synthesis were selected by using a Plackett–Burman screening design [glycerol, CAS, and initial cell dry weight (CDW) concentrations] and then optimized through a Box–Wilson design. Under such optimized conditions (22.02 g l⁻¹ glycerol, 1.78 g l⁻¹ CAS, and 1.83 g l⁻¹ inoculum) microaerobic batch cultures gave rise to 8.37 g l⁻¹ CDW and 3.52 g l⁻¹ PHB in 48 h (PHB content of 42%) in a benchtop bioreactor. Further improvements in microaerobic PHB accumulation were obtained in fed-batch cultures, in which glycerol was added to maintain its concentration above 5 g l⁻¹. After 60 h, CDW and PHB concentration reached 21.17 and 10.81 g l⁻¹, respectively, which results in a PHB content of 51%. Microaerobic fed-batch cultures allowed a 2.57-fold increase in volumetric productivity when compared with batch cultures. Electronic supplementary material The online version of this article (doi:) contains supplementary material, which is available to authorized users. An erratum to this article can be found at     

Effects of Carbon Concentrations and Carbon to Nitrogen ratios on Sporulation of Two Biological Control Fungi as Determined by Different Culture Methods

The nematophagous fungus Pochonia chlamydosporia (Clavicipitaceae) and entomopathogenic fungus Beauveria bassiana (Cordycipitaceae) have great potential for biological control. However, a significant barrier to their commercial development as mycopesticides is the high costs associated with production. Carbon (C) concentration and C to nitrogen ratio (C:N ratio) greatly affect fungal growth and sporulation. Effects of C concentration and C:N ratio differed when the fungi were cultivated using two different methods: the conventional (continuous cultivation) method and a novel “two-stage” method. Sporulation of P. chlamydosporia (HSY-12-14) was the highest when the media contained 6 g l⁻¹ C and a C:N ratio of 40:1 or 8 g l⁻¹ C and C:N ratios of 20:1 or 40:1 for the conventional method but 8 g l⁻¹ C and a C:N ratio of only 10:1 with the novel “two-stage” method. Sporulation of B. bassiana (IBC1201) was the highest when the media contained 12 g l⁻¹ C and a C:N ratio of 40:1 with the conventional method but only 4 g l⁻¹ C and a C:N ratio of 5:1 with the novel “two-stage” method. In addition, the nutritional requirements as determined by the conventional method differed for mycelial growth and sporulation. Understanding the effects of nutrition on sporulation can help programs seeking to use these organisms as biological control agents and is essential for their mass production and commercialization.     

Use of sugarcane molasses “B” as an alternative for ethanol production with wild-type yeast <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> ITV-01 at high sugar concentrations

Molasses “B” is a rich co-product of the sugarcane process. It is obtained from the second step of crystallization and is richer in fermentable sugars (50–65%) than the final molasses, with a lower non-sugar solid content (18–33%); this co-product also contains good vitamin and mineral levels. The use of molasses “B” for ethanol production could be a good option for the sugarcane industry when cane sugar prices diminish in the market. In a complex medium like molasses, osmotolerance is a desirable characteristic for ethanol producing strains. The aim of this work was to evaluate the use of molasses “B” for ethanol production using Saccharomyces cerevisiae ITV-01 (a wild-type yeast isolated from sugarcane molasses) using different initial sugar concentrations (70–291 g L⁻¹), two inoculum sizes and the addition of nutrients such as yeast extract, urea, and ammonium sulphate to the culture medium. The results obtained showed that the strain was able to grow at 291 g L⁻¹ total sugars in molasses “B” medium; the addition of nutrients to the culture medium did not produce a statistically significant difference. This yeast exhibits high osmotolerance in this medium, producing high ethanol yields (0.41 g g⁻¹). The best conditions for ethanol production were 220 g L⁻¹ initial total sugars in molasses “B” medium, pH 5.5, using an inoculum size of 6 × 10⁶ cell mL⁻¹; ethanol production was 85 g L⁻¹, productivity 3.8 g L⁻¹ h⁻¹ with 90% preserved cell viability.     

Anaerobic ethylene glycol degradation by microorganisms in poplar and willow rhizospheres

Although aerobic degradation of ethylene glycol is well documented, only anaerobic biodegradation via methanogenesis or fermentation has been clearly shown. Enhanced ethylene glycol degradation has been demonstrated by microorganisms in the rhizosphere of shallow-rooted plants such as alfalfa and grasses where conditions may be aerobic, but has not been demonstrated in the deeper rhizosphere of poplar or willow trees where conditions are more likely to be anaerobic. This study evaluated ethylene glycol degradation under nitrate-, and sulphate-reducing conditions by microorganisms from the rhizosphere of poplar and willow trees planted in the path of a groundwater plume containing up to 1.9 mol l⁻¹ (120 g l⁻¹) ethylene glycol and, the effect of fertilizer addition when nitrate or sulphate was provided as a terminal electron acceptor (TEA). Microorganisms in these rhizosphere soils degraded ethylene glycol using nitrate or sulphate as TEAs at close to the theoretical stoichiometric amounts required for mineralization. Although the added nitrate or sulphate was primarily used as TEA, TEAs naturally present in the soil or CO₂ produced from ethylene glycol degradation were also used, demonstrating multiple TEA usage. Anaerobic degradation produced acetaldehyde, less acetic acid, and more ethanol than under aerobic conditions. Although aerobic degradation rates were faster, close to 100% disappearance was eventually achieved anaerobically. Degradation rates under nitrate-reducing conditions were enhanced upon fertilizer addition to achieve rates similar to aerobic degradation with up to 19.3 mmol (1.20 g) of ethylene glycol degradation l⁻¹ day⁻¹ in poplar soils. This is the first study to demonstrate that microorganisms in the rhizosphere of deep rooted trees like willow and poplar can anaerobically degrade ethylene glycol. Since anaerobic biodegradation may significantly contribute to the phytoremediation of ethylene glycol in the deeper subsurface, the need for “pump and treat” or an aerobic treatment would be eliminated, hence reducing the cost of treatment.     

The role of sucrose and different cytokinins in the in vitro floral morphogenesis of rose (hybrid tea) cv. “First Prize”

Shoots of rose (hybrid tea) cv. “First Prize” were induced to flower in vitro on Murashige and Skoog (MS) medium containing various sucrose concentrations (15, 30 or 45 g l⁻¹) and different phytohormone combinations of different cytokinins [N⁶-benzyladenine (BA); thidiazuron (TDZ) and zeatin] with α-naphthaleneacetic acid (NAA). Results indicate that sucrose is the key factor in floral morphogenesis while cytokinin increases the flowering percentage and helps the normal development of floral buds. From the three cytokinins that were used, BA and zeatin were considered to be more suitable as inductive flowering agents than TDZ. Reduced inorganic and organic salt concentration in MS media had a positive effect on in vitro flowering. The morphology of shoots bearing floral buds varied with different cytokinin treatments. The highest percentage (45%) of flowering was obtained on MS medium supplemented with 3.0 mg l⁻¹ BA, 0.1 mg l⁻¹ NAA and 30 g l⁻¹ sucrose.     

Prospecting the utility of a PMI/mannose selection system for the recovery of transgenic sugarcane (<Emphasis Type="Italic">Saccharum</Emphasis> spp. hybrid) plants

For the first time, the phosphomannose isomerase (PMI, EC 5.3.1.8)/mannose-based “positive” selection system has been used to obtain genetically engineered sugarcane (Saccharum spp. hybrid var. CP72-2086) plants. Transgenic lines of sugarcane were obtained following biolistic transformation of embryogenic callus with an untranslatable sugarcane mosaic virus (SCMV) strain E coat protein (CP) gene and the Escherichia coli PMI gene manA, as the selectable marker gene. Postbombardment, transgenic callus was selectively proliferated on modified MS medium containing 13.6 μM 2,4-D, 20 g l⁻¹ sucrose and 3 g l⁻¹ mannose. Plant regeneration was obtained on MS basal medium with 2.5 μM TDZ under similar selection conditions, and the regenerants rooted on MS basal medium with 19.7 μM IBA, 20 g l⁻¹ sucrose, and 1.5 g l⁻¹ mannose. An increase in mannose concentration from permissive (1.5 g l⁻¹) to selective (3 g l⁻¹) conditions after 3 weeks improved the overall transformation efficiency by reducing the number of selection escapes. Thirty-four vigorously growing putative transgenic plants were successfully transplanted into the greenhouse. PCR and Southern blot analyses showed that 19 plants were manA-positive and 15 plants were CP-positive, while 13 independent transgenics contained both transgenes. Expression of manA in the transgenic plants was evaluated using a chlorophenol red assay and enzymatic analysis.     

Lactic acid production from sugar-cane juice by a newly isolated Lactobacillus sp.

A newly isolated sucrose-tolerant, lactic acid bacterium, Lactobacillus sp. strain FCP2, was grown on sugar-cane juice (125 g sucrose l⁻¹, 8 g glucose l⁻¹ and 6 g fructose l⁻¹) for 5 days and produced 104 g lactic acid l⁻¹ with 90% yield. A higher yield (96%) and productivity (2.8 g l⁻¹ h⁻¹) were obtained when strain FCP2 was cultured on 3% w/v (25 g sucrose l⁻¹, 2 g glucose l⁻¹ and 1 g fructose l⁻¹) sugar-cane juice for 10 h. Various cheap nitrogen sources such as silk worm larvae, beer yeast autolysate and shrimp wastes were also used as a substitute to yeast extract.     

Batch and repeated batch production of l(+)-lactic acid by Enterococcus faecalis RKY1 using wood hydrolyzate and corn steep liquor

Lactic acid production was investigated for batch and repeated batch cultures of Enterococcus faecalis RKY1, using wood hydrolyzate and corn steep liquor. When wood hydrolyzate (equivalent to 50 g l⁻¹ glucose) supplemented with 15–60 g l⁻¹ corn steep liquor was used as a raw material for fermentation, up to 48.6 g l⁻¹ of lactic acid was produced with, volumetric productivities ranging between 0.8 and 1.4 g l⁻¹ h⁻¹. When a medium containing wood hydrolyzate and 15 g l⁻¹ corn steep liquor was supplemented with 1.5 g l⁻¹ yeast extract, we observed 1.9-fold and 1.6-fold increases in lactic acid productivity and cell growth, respectively. In this case, the nitrogen source cost for producing 1 kg lactic acid can be reduced to 23% of that for fermentation from wood hydrolyzate using 15 g l⁻¹ yeast extract as a single nitrogen source. In addition, lactic acid productivity could be maximized by conducting a cell-recycle repeated batch culture of E. faecalis RKY1. The maximum productivity for this process was determined to be 4.0 g l⁻¹ h⁻¹.     

Regulation of metabolite production by precursors and elicitors in liquid cultures of <Emphasis Type="Italic">Hypericum perforatum</Emphasis>

Four precursors (l-phenylalanine, l-tryptophan, cinnamic acid and emodin) and one signal elicitor (methyl jasmonate, MeJA) were added to liquid cultures of Hypericum perforatum L. to study their effect on production of hyperforin and hypericins (pseudohypericin and hypericin). The addition of l-phenylalanine (75 to 100 mg l⁻¹) enhanced production of hypericins, but hyperforin levels were decreased. Hypericin, pseudohypericin and hyperforin concentrations were all decreased when l-tryptophan (25 to 100 mg l⁻¹) was added to the medium. However, addition of l-tryptophan (50 mg l⁻¹) with MeJA (100 μM) stimulated hyperforin production significantly (1.81-fold) and resulted in an increased biomass. Cinnamic acid (25, 50 mg l⁻¹) and emodin (1.0 to 10.0 mg l⁻¹) each enhanced hyperforin accumulation in H. perforatum, but did not affect accumulation of hypericins.     

Use of plant growth regulators to control flowering in citrus

With the aim to increase citrus fllowering under tropical conditions, two formulations of 2-chloroethyl phosphonic acid (Ethrel and Flordimex), Alar (succinic acid-2, 2-dimethyl hydrazide) and Cycocel (2-chloroethyl-trimethyl ammonium chloride) were applied during the flower induction period (December) to young “Valencia” orange trees at concentrations of 1000, 2500 and 5000 mg l⁻¹. These treatments effectively increased flowering, mainly at lower concentrations. Treatment using Flordimex at 500 and 1000 mg l⁻¹ concentrations resulted in flowering increase which is analyzed in this paper. Presented at the International Symposium “Plant Growth Regulators” held on June 18–22, 1984 at Liblice, Czechoslovakia.     

Production of ascorbic acid glucoside by alginate-entrapped mycelia of <Emphasis Type="Italic">Aspergillus niger</Emphasis>

The mycelia of Aspergillus niger, cultivated in a medium containing 45 g l⁻¹ maltose, 66 g l⁻¹ yeast extract, and 5 g l⁻¹ K₂HPO₄ at 30°C and 200 rpm, were used as a biocatalyst in the glucosylation of ascorbic acid. Free mycelia from 3-day-old culture, when used in a 6-h reaction with maltose as the acyl donor, gave 16.07 g l⁻¹ ascorbic acid glucoside corresponding to a volumetric productivity of 2.68 g l⁻¹ h⁻¹ and a conversion of 67%. Mycelia from 3-day-old cultures were entrapped in calcium alginate beads and used as a catalyst in the glucosylation of ascorbic acid. An ascorbic acid-to-maltose molar ratio of 1:9 was found to be optimum, and the conversion reached 75% after 12 h. The concentration of ascorbic acid glucoside produced at this molar ratio was 17.95 g l⁻¹, and the productivity was 1.5 g l⁻¹ h⁻¹. The biocatalyst was repeatedly used in a fixed bed bioreactor for the synthesis of ascorbic acid glucoside and approximately 17 g l⁻¹ of ascorbic acid glucoside corresponding to a volumetric productivity of 1.42 g l⁻¹ h⁻¹ was produced in each use. The conversion was retained at 70% in each use. The entrapped mycelia also exhibited exceptionally high reusability and storage stability. The product was purified to 85% by anion exchange and gel permeation chromatography with a final yield of 75%.     

Isolation of <Emphasis Type="Italic">Aspergillus oryzae</Emphasis> mutants for heterologous protein production from a double proteinase gene disruptant

The recombinant Pichia pastoris harboring an improved methionine adenosyltransferase (MAT) shuffled gene was employed to biosynthesize S-adenosyl-l-methionine (SAM). Two l-methionine (l-Met) addition strategies were used to supply the precursor: the batch addition strategy (l-Met was added separately at three time points) and the continuous feeding strategies (l-Met was fed continuously at the rate of 0.1, 0.2, and 0.5 g l⁻¹ h⁻¹, respectively). SAM accumulation, l-Met conversion rate, and SAM productivity with the continuous feeding strategies were all improved over the batch addition strategy, which reached 8.46 ± 0.31 g l⁻¹, 41.7 ± 1.4%, and 0.18 ± 0.01 g l⁻¹ h⁻¹ with the best continuous feeding strategy (0.2 g l⁻¹ h⁻¹), respectively. The bottleneck for SAM production with the low l-Met feeding rate (0.1 g L⁻¹ h⁻¹) was the insufficient l-Met supply. The analysis of the key enzyme activities indicated that the tricarboxylic acid cycle and glycolytic pathway were reduced with the increasing l-Met feeding rate, which decreased the adenosine triphosphate (ATP) synthesis. The MAT activity also decreased as the l-Met feeding rate rose. The reduced ATP synthesis and MAT activity were probably the reason for the low SAM accumulation when the l-Met feeding rate reached 0.5 g l⁻¹ h⁻¹.     

Production of uridine 5′-monophosphate by Corynebacterium ammoniagenes ATCC 6872 using a statistically improved biocatalytic process

Attempts were made with success to develop a two-step biocatalytic process for uridine 5′-monophosphate (UMP) production from orotic acid by Corynebacterium ammoniagenes ATCC 6872: the strain was first cultivated in a high salt mineral medium, and then cells were harvested and used as the catalyst in the UMP production reaction. Effects of cultivation and reaction conditions on UMP production were investigated. The cells exhibited the highest biocatalytic ability when cultivated in a medium containing corn steep liquor at pH 7.0 for 15 h in the exponential phase of growth. To optimize the reaction, both “one-factor-at-a-time” method and statistical method were performed. By “one-factor-at-a-time” optimization, orotic acid, glucose, phosphate ion (equimolar KH₂PO₄ and K₂HPO₄), MgCl₂, Triton X-100 were shown to be the optimum components for the biocatalytic reaction. Phosphate ion and C. ammoniagenes cell were furthermore demonstrated as the most important main effects on UMP production by Plackett–Burman design, indicating that 5-phosphoribosyl-1-pyrophosphate (PRPP) synthesis was the rate-limiting step for pyrimidine nucleotides production. Optimization by a central composition design (CCD) was then performed, and up to 32 mM (10.4 g l⁻¹) UMP was accumulated in 24 h from 38.5 mM (6 g l⁻¹) orotic acid. The yield was threefold higher than the original UMP yield before optimization.     

Enhanced hydrogen production from glucose using ldh- and frd-inactivated Escherichia coli strains

We improved the hydrogen yield from glucose using a genetically modified Escherichia coli. E. coli strain SR15 (ΔldhA, ΔfrdBC), in which glucose metabolism was directed to pyruvate formate lyase (PFL), was constructed. The hydrogen yield of wild-type strain of 1.08 mol/mol glucose, was enhanced to 1.82 mol/mol glucose in strain SR15. This figure is greater than 90 % of the theoretical hydrogen yield of facultative anaerobes (2.0 mol/mol glucose). Moreover, the specific hydrogen production rate of strain SR15 (13.4 mmol h⁻¹ g⁻¹ dry cell) was 1.4-fold higher than that of wild-type strain. In addition, the volumetric hydrogen production rate increased using the process where cells behaved as an effective catalyst. At 94.3 g dry cell/l, a productivity of 793 mmol h⁻¹ l⁻¹ (20.2 l h⁻¹ l⁻¹ at 37 °C) was achieved using SR15. The reported productivity substantially surpasses that of conventional biological hydrogen production processes and can be a trigger for practical applications.     

Induction of somatic embryogenesis in Azadirachta indica

A modified culture protocol has been developed for the induction of somatic embryogenesis in Azadirachta indica (neem). Embryogenic calluses were initiated from cotyledons or hypocotyls using a Murashige and Skoog (MS) agar medium supplemented with 0.5 mg l⁻¹ α-napthaleneacetic acid (NAA), 1 mg l⁻¹ 6-benzylaminopurine (BA), 1 g l⁻¹ casein hydrolysate, and 50 g l⁻¹ sucrose. The calluses, when transferred to a liquid medium similar to the agar medium but with NAA replaced by 0.5 mg l⁻¹ indole-3-acetic acid (IAA), formed globular structures which further developed a rudimentary root, after 4 to 5 weeks incubation. Subsequently, these highly differentiated tissues when transferred into a hormone-free MS medium containing 1 g l⁻¹ casein hydrolysate and 50 g l⁻¹ sucrose, active embryo masses started to appear after 1 to 2 weeks. The embryo production was found to improve more than 2 fold by adding 0.2 mg l⁻¹ zeatin to the medium. This revised version was published online in June 2006 with corrections to the Cover Date.     

Simultaneous bioconversion of glucose and xylose to ethanol by Saccharomyces cerevisiae in the presence of xylose isomerase

Simultaneous isomerisation and fermentation (SIF) of xylose and simultaneous isomerisation and cofermentation (SICF) of a glucose/xylose mixture was carried out by Saccharomyces cerevisiae in the presence of xylose isomerase. The SIF of 50 g l⁻¹ xylose gave an ethanol concentration and metabolic yield of 7.5 g l⁻¹ and 0.36 g (g xylose consumed)⁻¹. These parameters improved to 13.4 g l⁻¹ and 0.40 respectively, when borate was added to the medium. The SICF of a mixture of 50 g l⁻¹ glucose and 50 g l⁻¹ xylose gave an ethanol concentration and metabolic yield of 29.8 g l⁻¹ and 0.42 respectively, in the presence of borate. Temperature modulation from 30 °C to 35 °C during fermentation further enhanced the above parameters to 39 g l⁻¹ and 0.45 respectively. The approach was extended to the bioconversion of sugars present in a real lignocellulose hydrolysate (peanut-shell hydrolysate) to ethanol, with a fairly good yield. Received: 14 May 1999 / Received revision: 27 September 1999 / Accepted: 2 October 1999     

Enhanced l-lysine production in threonine-limited continuous culture of Corynebacterium glutamicum by using gluconate as a secondary carbon source with glucose

In order to improve the production rate of l-lysine, a mutant of Corynebacterium glutamicum ATCC 21513 was cultivated in complex medium with gluconate and glucose as mixed carbon sources. In a batch culture, this strain was found to consume gluconate and glucose simultaneously. In continuous culture at dilution rates ranging from 0.2 h⁻¹ to 0.25 h⁻¹, the specific l-lysine production rate increased to 0.12 g g⁻¹ h⁻¹ from 0.1 g g⁻¹ h⁻¹, the rate obtained with glucose as the sole carbon source [Lee et al. (1995) Appl Microbiol Biotechnol 43:1019–1027]. It is notable that l-lysine production was observed at higher dilution rates than 0.4 h⁻¹, which was not observed when glucose was the sole carbon source. The positive effect of gluconate was confirmed in the shift of the carbon source from glucose to gluconate. The metabolic transition, which has been characterized by decreased l-lysine production at the higher glucose uptake rates, was not observed when gluconate was added. These results demonstrate that the utilization of gluconate as a secondary carbon source improves the maximum l-lysine production rate in the threonine-limited continuous culture, probably by relieving the limiting factors in the lysine synthesis rate such as NADPH supply and/or phosphoenolpyruvate availability. Received: 16 May 1997 / Received revision: 28 August 1997 / Accepted: 29 August 1997