Knocking out of tailoring genes eryK and eryG in an industrial erythromycin-producing strain of Saccharopolyspora erythraea leading to overproduction of erythromycin B, C and D at different conversion ratios

Aims: To overproduce erythromycin C, B or D and evaluate the effect of disruption of tailoring genes eryK and eryG in an industrial erythromycin producer. Methods and Results: The tailoring genes eryG and eryK were inactivated individually or simultaneously by targeted gene disruption in an industrial strain Saccharopolyspora erythraea HL3168 E3, resulting in the overproduction of erythromycin C (2·48 g l^?1), B (1·70 g l^?1) or D (2·15 g l^?1) in the mutant strain QL‐G, QL‐K or QL‐KG, respectively. Analysis of the erythromycin congeners throughout the fermentation indicated that, at the end of fermentation, comparatively large amount of erythromycin D (0·67 g l^?1) was accumulated in QL‐G, whereas only small amount of erythromycin D (0·10 g l^?1) was produced in QL‐K. Conclusions: Inactivation of tailoring genes eryG and eryK in the high producer did not affect the biosynthesis of erythromycin. However, erythromycin D could be more efficiently methylated by EryG than be hydroxylated by EryK. Significance and Impact of the Study: Development of the mutant strains provides a method for the economical large‐scale production of potent lead compounds. The information about the accumulation and conversion of erythromycins in the industrial strains may contribute to further improving erythromycin production.     

Spaceflight‐induced enhancement of 2‐keto‐L‐gulonic acid production by a mixed culture of Ketogulonigenium vulgare and Bacillus thuringiensis

Two bacterial strains used for industrial production of 2‐keto‐L‐gulonic acid (2‐KLG), Ketogulonigenium vulgare 2 and Bacillus thuringiensis 1514, were loaded onto the spacecraft Shenzhou VII and exposed to space conditions for 68 h in an attempt to increase their fermentation productivities of 2‐KLG. An optimal combination of mutants B. thuringiensis 320 and K. vulgare 2194 (KB2194‐320) was identified by systematically screening the pH and 2‐KLG production of 16 000 colonies. Compared with the coculture of parent strains, the conversion rate of L‐sorbose to 2‐KLG by KB2194‐320 in shake flask fermentation was increased significantly from 82·7% to 95·0%. Furthermore, a conversion rate of 94·5% and 2‐KLG productivity of 1·88 g l^?1 h^?1 were achieved with KB2194‐320 in industrial‐scale fermentation (260 m³ fermentor). An observed increase in cell number of K2194 (increased by 47·8%) during the exponential phase and decrease in 2‐KLG reductase activity (decreased by 46·0%) were assumed to explain the enhanced 2‐KLG production. The results suggested that the mutants KB2194‐320 could be ideal substitutes for the currently employed strains in the 2‐KLG fermentation process and demonstrated the feasibility of using spaceflight to breed high‐yielding 2‐KLG‐producing strains for vitamin C production.

Significance and Impact of the Study

KB2194‐320, a combination of two bacterial strains bred by spaceflight mutation, exhibited significantly improved 2‐KLG productivity and hence could potentially increase the efficiency and reduce the cost of vitamin C production by the two‐step fermentation process. In addition, a new pH indicator method was applied for rational screening of K2, which dramatically improved the efficiency of screening.     

Improved ethanol production of a newly isolated thermotolerant Saccharomyces cerevisiae strain after high-energy-pulse-electron beam

Aims: To isolate thermotolerant Saccharomyces cerevisiae with high‐energy‐pulse‐electron (HEPE) beam, to optimize the mutation strain fermentation conditions for ethanol production and to conduct a preliminary investigation into the thermotolerant mechanisms. Methods and Results: After HEPE beam radiation, the thermotolerant S. cerevisiae strain Y43 was obtained at 45°C. Moreover, the fermentation conditions of mutant Y43 were optimized by L3³ orthogonal experiment. The optimal glucose content and initial pH for fermentation were 20% g l^?1 and 4·5, respectively; peptone content was the most neglected important factor. Under this condition, ethanol production of Y43 was 83·1 g l^?1 after fermentation for 48 h at 43°C, and ethanol yield was 0·42 g g^?1, which was about 81·5% of the theoretical yield. The results also showed that the trehalose content and the expression of the genes MSN2, SSA3 and TPS1 in Y43 were higher than those in the original strain (YE0) under the same stress conditions. Conclusions: A genetically stable mutant strain with high ethanol yield under heat stress was obtained using HEPE. This mutant may be a suitable candidate for the industrial‐scale ethanol production. Significance and Impact of the Study: High‐energy‐pulse‐electron radiation is a new efficient technology in breeding micro‐organisms. The mutant obtained in this work has the advantages in industrial ethanol production under thermostress.     

Conversion of biomass hydrolysates and other substrates to ethanol and other chemicals by Lactobacillus buchneri*

Aims: A Lactobacillus buchneri strain NRRL B‐30929 can convert xylose and glucose into ethanol and chemicals. The aims of the study were to survey three strains (NRRL B‐30929, NRRL 1837 and DSM 5987) for fermenting 17 single substrates and to exam NRRL B‐30929 for fermenting mixed substrates from biomass hydrolysates. Methods and Results: Mixed acid fermentation was observed for all three L. buchneri strains using various carbohydrates; the only exception was uridine which yielded lactate, acetate and uracil. Only B‐30929 is capable of utilizing cellobiose, a desired trait in a potential biocatalyst for biomass conversion. Flask fermentation indicated that the B‐30929 strain can use all the sugars released from pretreated hydrolysates, and producing 1·98–2·35 g l^?1 ethanol from corn stover hydrolysates and 2·92–3·01 g l^?1 ethanol from wheat straw hydrolysates when supplemented with either 0·25× MRS plus 1% corn steep liquor or 0·5× MRS. Conclusions: The L. buchneri NRRL B‐30929 can utilize mixed sugars in corn stover and wheat straw hydrolysates for ethanol and other chemical production. Significance and Impact of the Study: These results are valuable for future research in engineering L. buchneri NRRL B‐30929 for fermentative production of ethanol and chemicals from biomass.     

Effects of pretreated beet molasses on benzaldehyde lyase production by recombinant Escherichia coli BL21(DE3)pLySs

Aims: To investigate the effects of pretreated‐beet molasses on Escherichia coli fermentation using benzaldehyde lyase (BAL) production by recombinant E. coli BL21(DE3)pLySs process as the model system. Methods and Results: The effect of the initial pretreated (hydrolysed) beet molasses concentration was investigated at 16, 24, 30 and 56 g l^?1 at a dissolved oxygen condition of 40% air saturation cascade to airflow, at N = 625 min^?1 and pH_C = 7·2 controlled‐pH operation conditions. The highest cell concentration and BAL activity were obtained as C_X = 5·3 g l^?1 and A = 1617 U cm^?3, respectively, in the medium containing 30 g l^?1 pretreated beet molasses consisting of 7·5 g l^?1 glucose and 7·5 g l^?1 fructose. Production with and without IPTG (isopropyl‐β‐d ‐thiogalactopyranoside) induction using the medium containing 30 g l^?1 of pretreated beet molasses yielded the same amount of BAL production, where the overall cell yield on the substrate was 0·37 g g^?1, and the highest oxygen transfer coefficient was K_La = 0·048 s^?1. Conclusions: Pretreated beet molasses was used in the fermentation with E. coli for the first time and it yielded higher cell and BAL production compared with the glucose‐based medium. Significance and Impact of the Study: Pretreated beet molasses was found to be a good carbon source for E. coli fermentation. Furthermore, IPTG addition was not required to induce recombinant protein production as galactose, one of the monomers of trisaccharide raffinose present in the beet molasses (1·2%), induced the lac promoter.     

Modelling the growth and ethanol production of Brettanomyces bruxellensis at different glucose concentrations

Aim: To study the effect of glucose concentrations on the growth by Brettanomyces bruxellensis yeast strain in batch experiments and develop a mathematical model for kinetic behaviour analysis of yeast growing in batch culture. Methods and Results: A Matlab algorithm was developed for the estimation of model parameters. Glucose fermentation by B. bruxellensis was studied by varying its concentration (5, 9·3, 13·8, 16·5, 17·6 and 21·4%). The increase in substrate concentration up to a certain limit was accompanied by an increase in ethanol and biomass production; at a substrate concentration of 50–138 g l^?1, the ethanol and biomass production were 24, 59 and 6·3, 11·4 g l^?1, respectively. However, an increase in glucose concentration to 165 g l^?1 led to a drastic decrease in product formation and substrate utilization. Conclusions: The model successfully simulated the batch kinetic observed in all cases. The confidence intervals were also estimated at each phase at a 0·95 probability level in a t‐Student distribution for f degrees of freedom. The maximum ethanol and biomass yields were obtained with an initial glucose concentration of 138 g l^?1. Significance and Impact of the Study: These experiments illustrate the importance of using a mathematical model applied to kinetic behaviour on glucose concentration by B. bruxellensis.     

Enhancement of docosahexaenoic acid production by Schizochytrium sp. using a two-stage oxygen supply control strategy based on oxygen transfer coefficient

Aims: To improve the yield and productivity of docosahexaenoic acid (DHA) by Schizochytrium sp. in terms of the analysis of microbial physiology. Methods and Results: A two‐stage oxygen supply control strategy, aimed at achieving high concentration and high productivity of DHA, was proposed. At the first 40 h, K_La was controlled at 150·1 h^?1 to obtain high μ for cell growth, subsequently K_La was controlled at 88·5 h^?1 to maintain high q_p for high DHA accumulation. Finally, the maximum lipid, DHA content and DHA productivity reached 46·6, 17·7 g l^?1 and 111 mg l^?1 h^?1, which were 43·83%, 63·88% and 32·14% over the best results controlled by constant K_La. Conclusions: This paper described a two‐stage oxygen supply control strategy based on the kinetic analysis for efficient DHA fermentation by Schizochytrium sp. Significance and Impact of the study: This study showed the advantage of two‐stage control strategy in terms of microbial physiology. As K_La is a scaling‐up parameter, the idea developed in this paper could be scaled‐up to industrial process and applied to other industrial biotechnological processes to achieve both high product concentration and high productivity.     

Comparison of supplements* to enhance recovery of heat‐injured Salmonella from egg albumen

Aims: The purpose of this study was to determine the proficiency of supplements to enhance the recovery of Salmonella from heat‐treated liquid egg albumen on solid agar media. Methods and Results: Salmonella‐inoculated albumen, heated at 53·3°C for 4 min, was plated on 39 combinations of solid media with or without the addition of 12 supplements. Greater numbers of Salmonella (P < 0·05) recovered with the addition of 1·0 g l^?1 ferrous sulfate (FeSO₄) than with any other supplements, except for 0·5 or 1·0 g l^?1 3′3′‐thiodipropionic acid (TDP), which recovered equivalent populations. Addition of 1·0 g l^?1 sodium pyruvate or 6·0 g l^?1 yeast extract plus 1·0 g l^?1 sodium pyruvate supported greater resuscitation than unsupplemented tryptic soy agar (TSA) or supplementing with 0·01 or 0·1 g l^?1 N‐propyl gallate, 10 g l^?1 activated charcoal, 0·1 g l^?1 KMnO₄ or 50 mg l^?1 ethoxyquin. The remaining supplements supported recovery of equivalent numbers of Salmonella, which were fewer cells than recovered with 1·0 g l^?1 FeSO₄, yet greater populations than recovered with 50 mg l^?1 ethoxyquin. Conclusion: Supplementation of plating media with FeSO₄, TDP or sodium pyruvate enhanced recovery of sublethally injured Salmonella from albumen. Significance and Impact of the Study: Pasteurizing albumen impedes recovery of pathogens. These results suggest that the addition of supplements to plating media may assist resuscitation and colony development of heat‐injured salmonellae.     

Enhanced hyaluronic acid production of Streptococcus zooepidemicus by an intermittent alkaline-stress strategy

Aims: Enhanced hyaluronic acid (HA) production of Streptococcus zooepidemicus by redirecting carbon flux through an intermittent alkaline‐stress strategy. Methods and Results: pH value was kept at 7·0 for the first 6 h, and then intermittently switched to 8·5 for 1 h and back to 7·0 for 1 h until the end of fermentation at 16 h (one pH switch cycle every 2 h). With this intermittent alkaline‐stress strategy, HA production was increased to 6·5 ± 0·2 g l^?1 from 5·0 ± 0·1 g l^?1 of the control, in which pH was always kept at 7·0. In addition, biomass and lactic acid concentration decreased by 24% and 14%, respectively, while acetic acid concentration increased by 10% under intermittent alkaline stress. The redirection of carbon flux from lactic acid to acetic acid was further supported by the decreased lactate dehydrogenase activity and the increased acetate kinase activity. As indicated by the increased NADH oxidase (NOX) activity, intermittent alkaline‐stress induced a more oxidative intracellular environment which would facilitate HA synthesis. Conclusions: Overproduction of HA was realized by redirecting carbon flux through the proposed intermittent alkaline‐stress strategy. Significance and Impact of the Study: This study clearly demonstrated the importance of metabolic‐pathway‐analysis based fermentation strategy in industrial processes and provided an alternative optimization approach for high viscosity fermentation.     

Ethanol synthesis from glycerol by Escherichia coli redox mutants expressing adhE from Leuconostoc mesenteroides

Aims: Analysis of the physiology and metabolism of Escherichia coli arcA and creC mutants expressing a bifunctional alcohol‐acetaldehyde dehydrogenase from Leuconostoc mesenteroides growing on glycerol under oxygen‐restricted conditions. The effect of an ldhA mutation and different growth medium modifications was also assessed. Methods and Results: Expression of adhE in E. coli CT1061 [arcA creC(Con)] resulted in a 1·4‐fold enhancement in ethanol synthesis. Significant amounts of lactate were produced during micro‐oxic cultures and strain CT1061LE, in which fermentative lactate dehydrogenase was deleted, produced up to 6·5 ± 0·3 g l^?1 ethanol in 48 h. Escherichia coli CT1061LE derivatives resistant to >25 g l^?1 ethanol were obtained by metabolic evolution. Pyruvate and acetaldehyde addition significantly increased both biomass and ethanol concentrations, probably by overcoming acetyl‐coenzyme A (CoA) shortage. Yeast extract also promoted growth and ethanol synthesis, and this positive effect was mainly attributable to its vitamin content. Two‐stage bioreactor cultures were conducted in a minimal medium containing 100 μg l^?1 calcium d ‐pantothenate to evaluate oxic acetyl‐CoA synthesis followed by a switch into fermentative conditions. Ethanol reached 15·4 ± 0·9 g l^?1 with a volumetric productivity of 0·34 ± 0·02 g l^?1 h^?1. Conclusions: Escherichia coli responded to adhE over‐expression by funnelling carbon and reducing equivalents into a highly reduced metabolite, ethanol. Acetyl‐CoA played a key role in micro‐oxic ethanol synthesis and growth. Significance and Impact of the Study: Insight into the micro‐oxic metabolism of E. coli growing on glycerol is essential for the development of efficient industrial processes for reduced biochemicals production from this substrate, with special relevance to biofuels synthesis.     

Increased synthesis of α‐tocopherol,paramylon and tyrosine by Euglena gracilis under conditions of high biomass production

Aims: To analyse the production of different metabolites by dark‐grown Euglena gracilis under conditions found to render high cell growth. Methods and Results: The combination of glutamate (5 g l^?1), malate (2 g l^?1) and ethanol (10 ml l^?1) (GM + EtOH); glutamate (7·15 g l^?1) and ethanol (10 ml l^?1); or malate (8·16 g l^?1), glucose (10·6 g l^?1) and NH₄Cl (1·8 g l^?1) as carbon and nitrogen sources, promoted an increase of 5·6, 3·7 and 2·6‐fold, respectively, in biomass concentration in comparison with glutamate and malate (GM). In turn, the production of α‐tocopherol after 120 h identified by LC‐MS was 3·7 ± 0·2, 2·4 ± 0·1 and 2 ± 0·1 mg [g dry weight (DW)]^?1, respectively, while in the control medium (GM) it was 0·72 ± 0·1 mg (g DW)^?1. For paramylon synthesis, the addition of EtOH or glucose induced a higher production. Amino acids were assayed by RP‐HPLC; Tyr a tocopherol precursor and Ala an amino acid with antioxidant activity were the amino acids synthesized at higher concentration. Conclusions: Dark‐grown E. gracilis Z is a suitable source for the generation of the biotechnologically relevant metabolites tyrosine, α‐tocopherol and paramylon. Significance and Impact of the Study: By combining different carbon and nitrogen sources and inducing a tolerable stress to the cell by adding ethanol, it was possible to increase the production of biomass, paramylon, α‐tocopherol and some amino acids. The concentrations of α‐tocopherol achieved in this study are higher than others reported previously for Euglena, plant and algal systems. This work helps to understand the effect of different carbon sources on the synthesis of bio‐molecules by E. gracilis and can be used as a basis for future works to improve the production of different metabolites of biotechnological importance by this organism.     

Ethanol fermentation with Kluyveromyces marxianus from Jerusalem artichoke grown in salina and irrigated with a mixture of seawater and freshwater

Aims: To study fuel ethanol fermentation with Kluyveromyces marxianus ATCC8554 from Jerusalem artichoke (Helianthus tuberosus) grown in salina and irrigated with a mixture of seawater and freshwater. Methods and Results: The growth and ethanol fermentation of K. marxianus ATCC8554 were studied using inulin as substrate. The activity of inulinase, which attributes to the hydrolysis of inulin, the main carbohydrate in Jerusalem artichoke, was monitored. The optimum temperatures were 38°C for growth and inulinase production, and 35°C for ethanol fermentation. Aeration was not necessary for ethanol fermentation with the K. marxianus from inulin. Then, the fresh Jerusalem artichoke tubers grown in salina and irrigated with 25% and 50% seawater were further examined for ethanol fermentation with the K. marxianus, and a higher ethanol yield was achieved for the Jerusalem artichoke tuber irrigated with 25% seawater. Furthermore, the dry meal of the Jerusalem artichoke tubers irrigated with 25% seawater was examined for ethanol fermentation at three solid concentrations of 200, 225 and 250 g l^?1, and the highest ethanol yield of 0·467, or 91·5% of the theoretical value of 0·511, was achieved for the slurry with a solid concentration of 200 g l^?1. Conclusions: Halophilic Jerusalem artichoke can be used for fuel ethanol production. Significance and Impact of the Study: Halophilic Jerusalem artichoke, not competing with grain crops for arable land, is a sustainable feedstock for fuel ethanol production.     

Use chemometric techniques in the optimization of a specific bioassay for betalactams in milk

Aims: A microbiological bioassay using Geoacillus stearothermophilus was optimized to detect betalactams at concentrations near to the Maximum Residue Limits (MRLs), with low cross‐specificity for tetracycline. Methods and Results: A factorial design (3 × 4) was used to evaluate the effects of concentration of spores (2·0 × 10⁶, 4·0 × 10⁶ and 8·0 × 10⁶ spores ml^?1) and incubation time (3·0, 3·5, 4·0 and 4·5 h) on the response of the bioassay. Then, desirability function to raise the detection capabilities (CC_β) of tetracyclines and increase sensitivity to betalactams was implemented. Significant effects of Log[S] and incubation time [It] on the CC_β of betalactams and tetracyclines were observed. Finally, high value of global desirability (D = 0·853), adequate betalactams CC_β (3·8 μg l^?1 of penicillin ‘G’, 27 μg l^?1 of oxacillin, 8·1 μg l^?1 of ampicillin, 48 μg l^?1 of cloxacillin) and high tetracyclines CC_β (5260 μg l^?1 chlortetracycline, 1550 μg l^?1 of oxytetracycline, 1070 μg l^?1 of tetracycline) were calculated. Conclusions: The application of chemometric tools allows the optimization of a bioassay that detects betalactam residues in milk. The more robust conditions have been achieved in Log[S] = 6·30 and [It] = 4·20 h. Significance and Impact of the Study: The logistic regression model and the desirability function are adequate chemometric techniques to improve the properties of the methods, because it is possible to increase sensitivity and decrease cross‐specificity simultaneously.     

Use of ceramic-based cell immobilization to produce 1,3-propanediol from biodiesel-derived waste glycerol with Klebsiella pneumoniae

Aims: The feasibility of the continuous production of a valuable bioplastic raw material, namely 1,3‐propanediol (1,3‐PDO) from biodiesel by‐product glycerol, using immobilized cells was investigated. In addition, the effect of hydraulic retention time (HRT) was also analysed. Methods and Results: Ceramic balls and ceramic rings were used for the immobilization of a locally isolated strain; Klebsiella pneumoniae (GenBank no. 27F HM063413 ). HRT of 1 h is the best one in terms of volumetric production rate (g 1,3‐PDO l^?1 h^?1). The results indicated that ceramic‐based cell immobilization achieved a 2‐fold higher production rate (10 g 1,3‐PDO l^?1 h^?1) in comparison with suspended cell system (4·9 g 1,3‐PDO l^?1 h^?1). Conclusions: Continuous cultures with immobilized cells revealed that 1,3‐PDO production was more effective and more stable than suspended culture systems. Furthermore, cell immobilization had also obvious benefits especially for resistance of the production for extreme conditions (high organic loading rates, cell washouts). The results were important for understanding the significance of continuous immobilization process among other well‐known 1,3‐PDO fermentation processes. Significance and Impact of the Study: This work is a promising process for further studies, as the immobilized micro‐organism was able to reach high volumetric production rates at short HRT, it has an important role in tolerating and converting glycerol during fermentation. Therefore, HRT is a very significant operational parameter (P value <0·05) directly affecting the bioreactor performance and production rate.     

Enhanced solid‐state citric acid bio‐production using apple pomace waste through surface response methodology

Aims: To evaluate the potential of apple pomace (AP) supplemented with rice husk for hyper citric acid production through solid‐state fermentation by Aspergillus niger NRRL‐567. Optimization of two key parameters, such as moisture content and inducer (ethanol and methanol) concentration was carried out by response surface methodology. Methods and Results: In this study, the effect of two crucial process parameters for solid‐state citric acid fermentation by A. niger using AP waste supplemented with rice husk were thoroughly investigated in Erlenmeyer flasks through response surface methodology. Moisture and methanol had significant positive effect on citric acid production by A. niger grown on AP (P < 0·05). Higher values of citric acid on AP by A. niger (342·41 g kg^?1 and 248·42 g kg^?1 dry substrate) were obtained with 75% (v/w) moisture along with two inducers [3% (v/w) methanol and 3% (v/w) ethanol] with fermentation efficiency of 93·90% and 66·42%, respectively depending upon the total carbon utilized after 144 h of incubation period. With the same optimized parameters, conventional tray fermentation was conducted. The citric acid concentration of 187·96 g kg^?1 dry substrate with 3% (v/w) ethanol and 303·34 g kg^?1 dry substrate with 3% (v/w) methanol were achieved representing fermentation efficiency of 50·80% and 82·89% in tray fermentation depending upon carbon utilization after 120 h of incubation period. Conclusions: Apple pomace proved to be the promising substrate for the hyper production of citric acid through solid‐state tray fermentation, which is an economical technique and does not require any sophisticated instrumentation. Significance and Impact of the Study: The study established that the utilization of agro‐industrial wastes have positive repercussions on the economy and will help to meet the increasing demands of citric acid and moreover will help to alleviate the environmental problems resulting from the disposal of agro‐industrial wastes.     

Steps Toward High‐Performance PLA: Economical Production of d‐Lactate Enabled by a Newly Isolated Sporolactobacillus terrae Strain

Optically pure d ‐lactate production has received much attention for its critical role in high‐performance polylactic acid production. However, the current technology can hardly meet the comprehensive demand of industrialization on final titer, productivity, optical purity, and raw material costs. Here, an efficient d ‐lactate producer strain, Sporolactobacillus terrae (S. terrae) HKM‐1, is isolated for d ‐lactate production. The strain HKM‐1 shows extremely high d ‐lactate fermentative capability by using peanut meal, soybean meal, or corn steep liquor powder as a sole nitrogen source; the final titers (205.7 g L^?1, 218.9 g L^?1, and 193.9 g L^?1, respectively) and productivities (5.56 g L^?1 h^?1, 5.34 g L^?1 h^?1, and 3.73 g L^?1 h^?1, respectively) of d ‐lactate reached the highest level ever reported. A comparative genomic analysis between S. terrae HKM‐1 and previously reported d ‐lactate high‐producing Sporolactobacillus inulinus (S. inulinus) CASD is conducted. The results show that many unrelated genetic features may contribute to the superior performance in d ‐lactate production of S. terrae HKM‐1. This d ‐lactate producer HKM‐1, along with its fermentation process, is promising for sustainable d ‐lactate production by using agro‐industrial wastes.     

Statistical optimization of simple culture conditions to produce biomass of an ochratoxigenic mould biocontrol yeast strain

Aim: To maximize biomass production of an ochratoxigenic mould–controlling strain of Lachancea thermotolerans employing response surface methodology (RSM). Methods and Results: Using Plackett–Burman screening designs (PBSD) and central composite designs (CCD), an optimized culture medium containing (g l^?1): fermentable sugars (FS), 139·2, provided by sugar cane molasses (CMz), (NH₄)₂HPO₄ (DAP), 9·0, and yeast extract (YE), 2·5, was formulated. Maximal cell concentration obtained after 24 h at 28°C was 24·2 g l^?1cell dry weight (CDW). The mathematical model obtained was validated in experiments performed in shaken‐flask cultures and also in aerated bioreactors. Maximum yield and productivity values achieved were, respectively, of 0·23 g CDW/g FS in a medium containing (g l^?1): FS, 87·0; DAP, 7·0; YE, 1·0; and of 0·96 g CDW l^?1 h^?1 in a medium containing (g l^?1): FS, 150·8 plus DAP, 6·9. Conclusions: Optimized culture conditions for maximizing yeast biomass production determined in flask cultures were applicable at a larger scale. The highest yield values were attained in media containing relatively low‐CMz concentrations supplemented with DAP and YE. Yeast extract would not be necessary if higher productivity is the aim. Significance and Impact of the Study: Cells of L. thermotolerans produced aerobically could be sustainably produced in a medium just containing cheap carbon, nitrogen and phosphorus sources. Response surface methodology allowed the fine‐tuning of cultural conditions.     

Competitive exclusion as a mode of action of a novel Bacillus cereus aquaculture biological agent

Aims: To determine the contribution of potential modes of action of a Bacillus cereus aquaculture biological control agent in inhibition of the fish pathogen, Aeromonas hydrophila. Methods and Results: When B. cereus was tested in plate well inhibition studies, no production of antimicrobial compounds was detected. Bacillus cereus had a high growth rate (0·96 h^?1), whereas Aer. hydrophila concentration decreased by c. 70% in co‐culture experiments. In nutrient limitation studies, B. cereus had a significantly higher growth rate when cultured under glucose (P < 0·05) and iron (P < 0·01) limitation in comparison with Aer. hydrophila. Bacillus cereus glucose (0·30 g l^?1 h^?1) and iron (0·60 mg l^?1 h^?1) uptake rates were also significantly higher (P < 0·01) than the Aer. hydrophila glucose (0·14 g l^?1 h^?1) and iron (0·43 mg l^?1 h^?1) uptake rates. Iron uptake was facilitated by siderophore production shown in time profile studies where relative siderophore production was c. 60% through the late exponential and sporulation phases. Conclusions: Competitive exclusion by higher growth rate, competition for organic carbon and iron, facilitated by siderophore production, could be identified as mechanisms of pathogen growth inhibition by B. cereus. Significance and Impact of the Study: This study is the first elucidation of the mechanism of action of our novel B. cereus biological agent in growth attenuation of pathogenic Aer. hydrophila. This study enhances the application knowledge and attractiveness for adoption of B. cereus NRRL 100132 for exploitation in aquaculture.     

Comparison of culture methods on exopolysaccharide production in the submerged culture of Cordyceps militaris and process optimization

Aims: To improve exopolysaccharides (EPS) production of Cordyceps militaris (C. militaris), effects of different culture method on mycelial biomass and EPS production in the submerged culture of C. militaris were investigated. Methods and Results: A new two‐stage fermentation process for EPS production of C. militaris was designed in this work. Central composite design (CCD) was utilized to optimize the two‐stage fermentation process. The results showed that the two‐stage fermentation process for EPS production was superior to other culture method (conventional static culture and shake culture). CCD revealed that the optimum values of the test variables for EPS production were shaken for 140 h followed by 130‐h static culture. The maximum EPS production reached 3·2 g l^?1 under optimized two‐stage culture and was about 2·3‐fold and 1·6‐fold in comparison with those of original static culture and shake culture. Conclusions: It was indicated that a new two‐stage culture method obtained in this work possessed a high potential for the industrial production for EPS of C. militaris. Significance and Impact of the Study: The fundamental information obtained in this work is complementary to those of previous investigations on the submerged culture of C. militaris for the production of bioactive metabolites.     

Xylitol production from a mutant strain of Candida tropicalis

Aims: To characterize the kinetics of growth, sugar uptake and xylitol production in batch and fed‐batch cultures for a xylitol assimilation‐deficient strain of Candida tropicalis isolated via chemical mutagenesis. Methods and Results: Chemical mutagenesis using nitrosoguanidine led to the isolation of the xylitol‐assimilation deficient strain C. tropicalis SS2. Shake‐flask fermentations with this mutant showed a sixfold higher xylitol yield than the parent strain in medium containing 25 g l^?1 glucose and 25 g l^?1 xylose. With 20 g l^?1 glycerol, replacing glucose for cell growth, and various concentrations of xylose, the studies indicated that the mutant strain resulted in xylitol yields from xylose close to theoretical. Under fully aerobic conditions, fed‐batch fermentation with repeated addition of glycerol and xylose resulted in 3·3 g l^?1 h^?1 xylitol volumetric productivity with the final concentration of 220 g l^?1 and overall yield of 0·93 g g^?1 xylitol. Conclusions: The xylitol assimilation‐deficient mutant isolated in this study showed the potential for high xylitol yield and volumetric productivity under aerobic conditions. In the evaluation of glycerol as an alternative low‐cost nonfermentable carbon source, high biomass and xylitol yields under aerobic conditions were achieved; however, the increase in initial xylose concentrations resulted in a reduction in biomass yield based on glycerol consumption. This may be a consequence of the role of an active transport system in the yeast requiring increasing energy for xylose uptake and possible xylitol secretion, with little or no energy available from xylose metabolism. Significance and Impact of the Study: The study confirms the advantage of using a xylitol assimilation‐deficient yeast under aerobic conditions for xylitol production with glycerol as a primary carbon source. It illustrates the potential of using the xylose stream in a biomass‐based bio‐refinery for the production of xylitol with further cost reductions resulting from using glycerol for yeast growth and energy production.