Mixture design as first step for improved glutaminase production in solid-state fermentation by isolated Bacillus

Aim: Investigation of mixture‐design impact on glutaminase production by isolated Bacillus sp. Methods and Results: An augmented simplex centroid design was used to optimize a three (wheat bran, Bengal gram husk and palm seed fibre) component mixture for glutaminase production. Selected substrate materials showed impact on glutaminase production values at individual level by Bengal gram husk [2789 U gds^?1 (gram dry substrate] and in two‐level combination with wheat bran and Bengal gram husk (maximum of 3300 U gds^?1). Conclusion: Bengal gram husk is the most suitable substrate medium for glutaminase production by Bacillus sp. Maximum glutaminase production is achieved using solid‐substrate mixture at two‐level combinations in the ratio of 66 : 34 for Bengal gram husk and wheat bran, respectively. Significance and Impact of the Study: The present study has significance in large‐scale production of glutaminase at commercial level with the use of multi‐substrate rather than single‐substrate/support material.     

Influence of carbon and nitrogen concentration on itaconic acid production by the smut fungus Ustilago maydis

Itaconic acid is a valuable platform compound for the production of bio‐based polymers, chemicals, and fuels. Ustilago maydis is a promising host for the production of itaconic acid from biomass‐derived substrates due to its unicellular growth pattern and its potential to utilize biomass‐derived sugar monomers and polymers. The potential of U. maydis for industrial itaconate production was assessed in pH‐controlled batch fermentations with varying medium compositions. Using 200 g/L glucose and 75 mM ammonium, 44.5 g/L of itaconate was produced at a maximum rate of 0.74 g L^?1 h^?1. By decreasing the substrate concentrations to 50 g/L glucose and 30 mM ammonium, a yield of 0.34 g/g (47 mol%) could be achieved. Itaconate production from xylose was also feasible. These results indicate that high itaconic acid titers can be achieved with U. maydis. However, further optimization of the biocatalyst itself through metabolic engineering is still needed in order to achieve an economically feasible process, which can be used to advance the development of a bio‐based economy.     

Retention of the cyanobacterial neurotoxin β‐N‐methylamino‐l‐alanine in melanin and neuromelanin‐containing cells – a possible link between Parkinson‐dementia complex and pigmentary retinopathy

β‐N‐methylamino‐l ‐alanine (BMAA), a neurotoxic amino acid produced by cyanobacteria, has been suggested to be involved in the etiology of a neurodegenerative disease complex which includes Parkinson‐dementia complex (PDC). In PDC, neuromelanin‐containing neurons in substantia nigra are degenerated. Many PDC patients also have an uncommon pigmentary retinopathy. The aim of this study was to investigate the distribution of ³H‐BMAA in mice and frogs, with emphasis on pigment‐containing tissues. Using autoradiography, a distinct retention of ³H‐BMAA was observed in melanin‐containing tissues such as the eye and neuromelanin‐containing neurons in frog brain. Analysis of the binding of ³H‐BMAA to Sepia melanin in vitro demonstrated two apparent binding sites. In vitro‐studies with synthetic melanin revealed a stronger interaction of ³H‐BMAA with melanin during synthesis than the binding to preformed melanin. Long‐term exposure to BMAA may lead to bioaccumulation in melanin‐ and neuromelanin‐containing cells causing high intracellular levels, and potentially changed melanin characteristics via incorporation of BMAA into the melanin polymer. Interaction of BMAA with melanin may be a possible link between PDC and pigmentary retinopathy.     

Antioxidant efficacy and adhesion rescue by a recombinant mussel foot protein‐6

Mytilus foot protein type 6 (mfp‐6) is crucial for maintaining the reducing conditions needed for optimal wet adhesion in marine mussels. In this report, we describe the expression and production of a recombinant Mytilus californianus foot protein type 6 variant 1 (rmfp‐6.1) fused with a hexahistidine affinity tag in Escherichia coli and its purification by affinity chromatography. Recombinant mfp‐6 showed high purification yields of 5–6 mg L^?1 cell culture and excellent solubility in low pH buffers that retard oxidation of its many thiol groups. Purified rmfp‐6.1 protein showed high 2,2‐diphenyl‐1‐picrylhydrazyl radical scavenging activity when compared with vitamin C. Using the highly sensitive surface forces apparatus (SFA) technique to measure interfacial surface forces in the nano‐Newton range, we show that rmfp‐6.1 is also able to rescue the oxidation‐dependent adhesion loss of mussel foot protein 3 (mfp‐3) at pH 3. The adhesion rescue is related to a reduction of dopaquinone back to 3,4‐dihydroxyphenyl‐l ‐alanine in mfp‐3, which is the reverse reaction observed during the detrimental enzymatic browning process in fruits and vegetables. Broadly viewed, rmfp‐6.1 has potential as a versatile antioxidant for applications ranging from personal products to antispoilants for perishable foods during processing and storage. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:1587–1593, 2013     

Kinetics of Pyruvate Decarboxylase Deactivation by Benzaldehyde

Based on experimental data, a kinetic model for the deactivation of partially purified pyruvate decarboxylase (PDC) by benzaldehyde (0–200 mM) in MOPS buffer (2.5 M) has been developed. An initial lag period prior to deactivation was found to occur. With first order dependencies of PDC deactivation on exposure time and on benzaldehyde concentration, a reaction time deactivation constant of 2.64×10^?3 h^?1 and a benzaldehyde deactivation coefficient of 1.98×10^?4 mM^?1 h^?1 were determined for benzaldehyde concentrations up to 200 mM. The PDC deactivation kinetic equations established in this study are an essential component in an overall model being developed to describe the enzymatic biotransformation of benzaldehyde and pyruvate to produce the pharmaceutical intermediate (R)-phenylacetylcarbinol (R-PAC).     

Preparation of extracellular domain 3 of human VEGF receptor‐2 and the monitoring of its real‐time binding to VEGF by biosensors

Vascular endothelial growth factor receptor‐2 (VEGFR‐2) plays an important role in stimulating the proliferation of endothelial cells and improving the permeability of blood vessels, which is involved in tumor angiogenesis, a process that is essential for tumor growth and metastasis. In this study, we describe a method for high yield of recombinant extracellular domain 3 (KDR3) of human VEGFR‐2 in an Escherichia coli system with further purification by cation exchange chromatography and immobilized metal affinity chromatography (IMAC). The biological activity of recombinant KDR3 was performed by sequestering VEGF in HUVEC proliferation assay. The real‐time binding of human VEGF to immobilized KDR3 was monitored by a label‐free biosensor, Optical waveguide lightmode spectroscopy (OWLS). Under the given experimental conditions, the association rate constant k_a was 4.2 × 10³ M^?1 s^?1 and the dissociation rate k_d was 5.1 × 10^?3 s^?1. The dissociation constant K_D was then calculated to be 1.2 × 10^?6 M. The obtained values will serve as baseline parameters for the design of improved versions of recombinant soluble VEGF receptors and the evaluation of developed anti‐KDR antibodies. In addition, such a scenario established by the use of OWLS will potentiate the kinetic study of ligand/receptor and antigen/antibody. The receptor discussed here, which block VEGF binding to cell membrane KDR, have potential clinical application in the treatment of cancer and other diseases where pathological angiogenesis is involved. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Light‐Dependent and Aeration‐Independent Gram‐Scale Hydroxylation of Cyclohexane to Cyclohexanol by CYP450 Harboring Synechocystis sp. PCC 6803

Oxygenase‐containing cyanobacteria constitute promising whole‐cell biocatalysts for oxyfunctionalization reactions. Photosynthetic water oxidation thereby delivers the required cosubstrates, that is activated reduction equivalents and O₂, sustainably. A recombinant Synechocystis sp. PCC 6803 strain showing unprecedentedly high photosynthesis‐driven oxyfunctionalization activities is developed, and its technical applicability is evaluated. The cells functionally synthesize a heterologous cytochrome P450 monooxygenase enabling cyclohexane hydroxylation. The biocatalyst‐specific reaction rate is found to be light‐dependent, reaching 26.3 ± 0.6 U g_CDW^?1 (U = μmol min^?1 and cell dry weight [CDW]) at a light intensity of 150 µmol_photons m^?2 s^?1. In situ substrate supply via a two‐liquid phase system increases the initial specific activity to 39.2 ± 0.7 U g_CDW^?1 and stabilizes the biotransformation by preventing cell toxification. This results in a tenfold increased specific product yield of 4.5 g_cyclohexanol g_CDW^?1 as compared to the single aqueous phase system. Subsequently, the biotransformation is scaled from a shake flask to a 3 L stirred‐tank photobioreactor setup. In situ O₂ generation via photosynthetic water oxidation allows a nonaerated process operation, thus circumventing substrate evaporation as the most critical factor limiting the process performance and stability. This study for the first time exemplifies the technical applicability of cyanobacteria for aeration‐independent light‐driven oxyfunctionalization reactions involving highly toxic and volatile substrates.     

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.     

Characterization of an ethanol‐tolerant 1,4‐β‐xylosidase produced by Pichia membranifaciens

Aims: The purification and biochemical properties of the 1,4‐β‐xylosidase of an oenological yeast were investigated. Methods and Results: An ethanol‐tolerant 1,4‐β‐xylosidase was purified from cultures of a strain of Pichia membranifaciens grown on xylan at 28°C. The enzyme was purified by sequential chromatography on DEAE cellulose and Sephadex G‐100. The relative molecular mass of the enzyme was determined to be 50 kDa by SDS‐PAGE. The activity of 1,4‐β‐xylosidase was optimum at pH 6·0 and at 35°C. The activity had a K_m of 0·48 ± 0·06 mmol l^?1 and a V_max of 7·4 ± 0·1 μmol min^?1 mg^?1 protein for p‐nitrophenyl‐β‐d ‐xylopyranoside. Conclusions: The enzyme characteristics (pH and thermal stability, low inhibition rate by glucose and ethanol tolerance) make this enzyme a good candidate to be used in enzymatic production of xylose and improvement of hemicellulose saccharification for production of bioethanol. Significance and Impact of the Study: This study may be useful for assessing the ability of the 1,4‐β‐xylosidase from P. membranifaciens to be used in the bioethanol production process.     

Efficient production of Al(OH)3‐immobilized laccase with a Heterobasidion annosum strain selected by microplate screening

Aims: Wild‐type white rot fungi are the most important production organisms for laccase, a promising oxidative biocatalyst with numerous applications. This study aimed at identifying novel highly productive strains, finding optimal cultivation conditions for laccase production and establishing a simple immobilization procedure. Methods and Results: By using a newly developed 96‐well microplate cultivation method, 23 species of white rot fungi, represented by 29 strains, were directly compared with regard to the amount of secreted laccase. Both, with glucose and spruce saw dust as growth substrate a Heterobasidion annosum strain and a Physisporinus vitreus strain were the most productive (730–2200 U l^?1 of secreted laccase). Cultivation conditions for laccase production with H. annosum were optimized in larger‐scale liquid cultures. Aeration with a sparger lead to a 3·8‐fold increase in laccase activity when compared to nonaerated flask cultures. More than 3000 U l^?1 laccase was produced in glucose medium supplemented with yeast extract and the inducer veratryl alcohol. Culture supernatant was incubated with short‐range ordered Al(OH)₃ particles to directly immobilize and concentrate laccase by adsorption. Active laccase was recovered in 40% yield and the Al(OH)₃‐adsorbed laccase was suitable for repeated decolourization of indigo carmine. Conclusions: Microplate cultivation allowed a large‐scale comparison of the capacity of different fungal species for laccase production. Laccase secretion of a highly productive H. annosum strain was found to vary strongly with different cultivation conditions. Adsorption to Al(OH)₃ proved to be suitable as direct immobilization technique. Significance and Impact of the Study: The microplate screening method simplifies strain and medium development for laccase production. Two novel fungal strains suitable for laccase production were identified. Procedures for simple and efficient production of immobilized H. annosum laccase were established.     

Optimal culture conditions for keratinase production by a novel thermophilic Myceliophthora thermophila strain GZUIFR‐H49‐1

Aims: To investigate the effect of medium compositions and culture conditions on keratinase production by a novel thermophilic fungus Myceliophthora thermophila (Apinis) Oorschot strain GZUIFR‐H49‐1. Methods and Results: The thermophilic strain GZUIFR‐H49‐1 with keratinolytic ability was characterized and identified as a strain of M. thermophila on the basis of its morphological characters and molecular analysis of ITS1‐5.8S‐ITS2 rDNA sequence. Among the medium compositions tested, the soluble starch (SS), urea, sodium thiosulfate and CaCl₂ were the most effective C‐source, N‐source, S‐source and mineral ion, respectively, by employing the single‐factor experiment. The urea and pH value were the significant factors (P < 0·05) for the keratinase production in this experiment condition using Plackett–Burman factorial design. The conditions of keratinase production were further optimized by Box–Behnken design. Consequently, there was a 6·4‐fold increase (5100 U l^?1) in the keratinase activity than the initial value (800 U l^?1) by this optimal process. Conclusions: This study indicated that the optimization design proved a useful and powerful tool for the development of optimal medium compositions and culture conditions. Myceliophthora thermophila strain GZUIFR‐H49‐1 was a promising fungus strain for keratinase production. Significance and Impact of the Study: This study characterized a novel thermophilic M. thermophila strain GZUIFR‐H49‐1 with potential applications for keratinase production. These conditions of keratinase production obtained by means of optimization design will be accumulated as potential information for exploration and utilization to the new fungus isolate.     

Optimization of medium for indole-3-acetic acid production using Pantoea agglomerans strain PVM

Aims: To optimize the medium components for the production of indole‐3‐acetic acid (IAA) by isolated bacterium Pantoea agglomerans strain PVM. Methods and Results: Present study deals with the production of an essential plant hormone IAA by a bacterial isolate P. agglomerans strain PVM identified by 16S rRNA gene sequence analysis. The medium containing 8 g l^?1 of meat extract and 1 g l^?1 of l ‐tryptophan (precursor) at optimum pH 7, 30°C and 48‐h incubation gave the maximum production of IAA (2·191 g l^?1). Effect of IAA synthesized on in vitro root induction in Nicotiana tobacum (leaf) explants was compared with that of control. IAA was characterized by high‐performance thin‐layer chromatography, high‐performance liquid chromatography and gas chromatography–mass spectroscopy. Conclusions: Pantoea agglomerans strain PVM was a good candidate for the inexpensive and utmost production of IAA in short period, as it requires simple medium (meat extract and l ‐tryptophan). Significance and Impact of the Study: The present report first time showed the rapid, cost‐effective and maximum production of IAA. No reports are available on the optimization of particular medium components for the production of IAA. This study demonstrates a novel approach for in vitro root induction in N. tobacum (leaf) explants.     

Hydrolytic properties of a thermostable α‐l‐arabinofuranosidase from Caldicellulosiruptor saccharolyticus

Aims: To characterize of a thermostable recombinant α‐l ‐arabinofuranosidase from Caldicellulosiruptor saccharolyticus for the hydrolysis of arabino‐oligosaccharides to l ‐arabinose. Methods and Results: A recombinant α‐l ‐arabinofuranosidase from C. saccharolyticus was purified by heat treatment and Hi‐Trap anion exchange chromatography with a specific activity of 28·2 U mg^?1. The native enzyme was a 58‐kDa octamer with a molecular mass of 460 kDa, as measured by gel filtration. The catalytic residues and consensus sequences of the glycoside hydrolase 51 family of α‐l ‐arabinofuranosidases were completely conserved in α‐l ‐arabinofuranosidase from C. saccharolyticus. The maximum enzyme activity was observed at pH 5·5 and 80°C with a half‐life of 49 h at 75°C. Among aryl‐glycoside substrates, the enzyme displayed activity only for p‐nitrophenyl‐α‐l ‐arabinofuranoside [maximum k_cat/K_m of 220 m(mol l^?1)^?1 s^?1] and p‐nitrophenyl‐α‐l ‐arabinopyranoside. This substrate specificity differs from those of other α‐l ‐arabinofuranosidases. In a 1 mmol l^?1 solution of each sugar, arabino‐oligosaccharides with 2–5 monomer units were completely hydrolysed to l ‐arabinose within 13 h in the presence of 30 U ml^?1 of enzyme at 75°C. Conclusions: The novel substrate specificity and hydrolytic properties for arabino‐oligosaccharides of α‐l ‐arabinofuranosidase from C. saccharolyticus demonstrate the potential in the commercial production of l ‐arabinose in concert with endoarabinanase and/or xylanase. Significance and Impact of the Study: The findings of this work contribute to the knowledge of hydrolytic properties for arabino‐oligosaccharides performed by thermostable α‐l ‐arabinofuranosidase.     

Semicontinuous sophorolipid fermentation using a novel bioreactor with dual ventilation pipes and dual sieve‐plates coupled with a novel separation system

Sophorolipids (SLs) are biosurfactants with widespread applications. The yield and purity of SLs are two important factors to be considered during their commercial large‐scale production. Notably, SL accumulation causes an increase in viscosity, decrease in dissolved oxygen and product inhibition in the fermentation medium. This inhibits the further production and purification of SLs. This describes the development of a novel integrated system for SL production using Candida albicans O‐13‐1. Semicontinuous fermentation was performed using a novel bioreactor with dual ventilation pipes and dual sieve‐plates (DVDSB). SLs were separated and recovered using a newly designed two‐stage separation system. After SL recovery, the fermentation broth containing residual glucose and oleic acid was recycled back into the bioreactor. This novel approach considerably alleviated the problem of product inhibition and accelerated the rate of substrate utilization. Production of SLs achieved was 477 g l^?1, while their productivity was 1.59 g l^?1 h^?1. Purity of SLs improved by 23.3%, from 60% to 74%, using DVDSB with the separation system. The conversion rate of carbon source increased from 0.5 g g^?1 (in the batch fermentation) to 0.6 g g^?1. These results indicated that the integrated system could improve the efficiency of production and purity of SLs.     

Development of a process for large-scale chromatographic purification of an alginate lyase from Klebsiella pneumoniae

Summary A process for purification of an alginate lyase, produced extracellularly by fermentation of Klebsiella pneumoniae, has been developed. The process includes two chromatographic steps and is well suited to large-scale operation. By hydrophobic interaction chromatography on Phenyl-Sepharose FF, followed by anion exchange chromatography on Q-Sepharose FF in a negative mode, the specific activity was increased from 0.09 units (U) mg ^–1 to more than 50 U mg^–1. Due to an extremely low product concentration in the fermentation broth, and large amounts of contaminating proteins, the chromatographic adsorbents had low capacities with respect to alginate lyase. By adsorption on the cation exchanger S-Sepharose FF, the capacity was so low that the enzyme could not be concentrated. The binding capacity of Phenyl-Sepharose FF was approximately 20-fold higher, and a three to tenfold concentration was obtained. The first stage of the process, hydrophobic interaction chromatography, has been applied to the isolation of alginate lyase from fermentation batches of 180 l. Several runs have resulted in a purified product with an average quantity of 30 000–35 000 U per fermentation, and an average specific activity of 4.5 U mg^–1. Although the raw material employed in this work has been particularly unfavourable, the process developed will also be applicable to raw materials with higher product concentrations. Offprint requests to: I. M. Aasen     

Comparative Fluxome and Metabolome Analysis of Formate as an Auxiliary Substrate for Penicillin Production in Glucose‐Limited Cultivation of Penicillium chrysogenum

During glucose‐limited growth, a substantial input of adenosine triphosphate (ATP) is required for the production of β‐lactams by the filamentous fungus Penicillium chrysogenum. Formate dehydrogenase has been confirmed in P. chrysogenum for formate oxidation allowing an extra supply of ATP, and coassimilation of glucose and formate has the potential to increase penicillin production and biomass yield. In this study, the steady‐state metabolite levels and fluxes in response to cofeeding of formate as an auxiliary substrate in glucose‐limited chemostat cultures at the dilution rates (D) of both 0.03 h^?1 and 0.05 h^?1 are determined to evaluate the quantitative impact on the physiology of a high‐yielding P. chrysogenum strain. It is observed that an equimolar addition of formate is conducive to an increase in both biomass yield and penicillin production at D = 0.03 h^?1, while this is not the case at D = 0.05 h^?1. In addition, a higher cytosolic redox status (NADH/NAD⁺), a higher intracellular glucose level, and lower penicillin productivity are only observed upon formate addition at D = 0.05 h^?1, which are virtually absent at D = 0.03 h^?1. In conclusion, the results demonstrate that the effect of formate as an auxiliary substrate on penicillin productivity in the glucose‐limited chemostat cultivations of P. chrysogenum is not only dependent on the formate/glucose ratio as published before but also on the specific growth rate. The results also imply that the overall process productivity and quality regarding the use of formate should be further explored in an actual industrial‐scale scenario.     

Rapid,robotic, small‐scale protein production for NMR screening and structure determination

Three‐dimensional protein structure determination is a costly process due in part to the low success rate within groups of potential targets. Conventional validation methods eliminate the vast majority of proteins from further consideration through a time‐consuming succession of screens for expression, solubility, purification, and folding. False negatives at each stage incur unwarranted reductions in the overall success rate. We developed a semi‐automated protocol for isotopically‐labeled protein production using the Maxwell‐16, a commercially available bench top robot, that allows for single‐step target screening by 2D NMR. In the span of a week, one person can express, purify, and screen 48 different ¹⁵N‐labeled proteins, accelerating the validation process by more than 10‐fold. The yield from a single channel of the Maxwell‐16 is sufficient for acquisition of a high‐quality 2D ¹H‐¹⁵N‐HSQC spectrum using a 3‐mm sample cell and 5‐mm cryogenic NMR probe. Maxwell‐16 screening of a control group of proteins reproduced previous validation results from conventional small‐scale expression screening and large‐scale production approaches currently employed by our structural genomics pipeline. Analysis of 18 new protein constructs identified two potential structure targets that included the second PDZ domain of human Par‐3. To further demonstrate the broad utility of this production strategy, we solved the PDZ2 NMR structure using [U‐¹⁵N,¹³C] protein prepared using the Maxwell‐16. This novel semi‐automated protein production protocol reduces the time and cost associated with NMR structure determination by eliminating unnecessary screening and scale‐up steps.     

Metabolism in 1,3‐propanediol fed‐batch fermentation by a D‐lactate deficient mutant of Klebsiella pneumoniae

Klebsiella pneumoniae HR526, a new isolated 1,3‐propanediol (1,3‐PD) producer, exhibited great productivity. However, the accumulation of lactate in the late‐exponential phase remained an obstacle of 1,3‐PD industrial scale production. Hereby, mutants lacking D ‐lactate pathway were constructed by knocking out the ldhA gene encoding fermentative D ‐lactate dehydrogenase (LDH) of HR526. The mutant K. pneumoniae LDH526 with the lowest LDH activity was studied in aerobic fed‐batch fermentation. In experiments using pure glycerol as feedstock, the 1,3‐PD concentrations, conversion, and productivity increased from 95.39 g L^?1, 0.48 and 1.98 g L^?1 h^?1 to 102. 06 g L^?1, 0.52 mol mol^?1 and 2.13 g L^?1 h^?1, respectively. The diol (1,3‐PD and 2,3‐butanediol) conversion increased from 0.55 mol mol^?1 to a maximum of 0.65 mol mol^?1. Lactate would not accumulate until 1,3‐PD exceeded 84 g L^?1, and the final lactate concentration decreased dramatically from more than 40 g L^?1 to <3 g L^?1. Enzymic measurements showed LDH activity decreased by 89–98% during fed‐batch fermentation, and other related enzyme activities were not affected. NADH/NAD⁺ enhanced more than 50% in the late‐exponential phase as the D ‐lactate pathway was cut off, which might be the main reason for the change of final metabolites concentrations. The ability to utilize crude glycerol from biodiesel process and great genetic stability demonstrated that K. pnemoniae LDH526 was valuable for 1,3‐PD industrial production. Biotechnol. Bioeng. 2009; 104: 965–972. © 2009 Wiley Periodicals, Inc.     

Optimization of exopolysaccharide production from Armillaria mellea in submerged cultures

Aims: To study the optimization of submerged culture conditions for exopolysaccharide (EPS) production by Armillaria mellea in shake‐flask cultures and also to evaluate the performance of an optimized culture medium in a 5‐l stirred tank fermenter. Methods and Results: Shake flask cultures for EPS optimal nutritional production contained having the following composition (in g l^?1): glucose 40, yeast extract 3, KH₂PO₄ 4 and MgSO₄ 2 at an optimal temperature of 22°C and an initial of pH 4·0. The optimal culture medium was then cultivated in a 5‐l stirred tank fermenter at 1 vvm (volume of aeration per volume of bioreactor per min) aeration rate, 150 rev min^?1 agitation speed, controlled pH 4·0 and 22°C. In the optimal culture medium, the maximum EPS production in a 5‐l stirred tank fermenter was 588 mg l^?1, c. twice as great as that in the basal medium. The maximum productivity for EPS (Q_p) and product yield (Y_P/S) were 42·02 mg l^?1 d^?1 and 26·89 mg g^?1, respectively. Conclusions: The optimal culture conditions we proposed in this study enhanced the EPS production of A. mellea from submerged cultures. Significance and Impact of the Study: The optimal culturing conditions we have found will be a suitable starting point for a scale‐up of the fermentation process, helping to develop the production of related medicines and health foods from A. mellea.     

Effect of an exponential feeding regime on the production of Rhodotorula araucariae epoxide hydrolase in Yarrowia lipolytica

Aims: To evaluate the effect of and exponential feeding regime on the production of epoxide hydrolase (EH) enzyme in recombinant Yarrowia lipolytica in comparison to a constant feed strategy. Methods and Results: An exponential feed model was developed and fermentations were fed at six different exponential rates. A twofold increase in EH productivity and a 15% increase in volumetric EH activity was obtained by applying exponential glucose feed rates in fed‐batch cultivation. These responses were modelled to obtain a theoretical optimum feed rate that was validated in duplicate fermentations. The model optimum of 0·06 h^?1 resulted in a volumetric EH activity of c. 5500 U l^?1 h^?1 and a maximum activity of 206 000 U l^?1. This correlated well with model predictions, with a variance of <10%. Conclusions: The use of an exponential feed strategy at a rate of 0·06 h ^{? 1} yielded best results for all key responses which show a clear improvement over a constant feed strategy. Significance and Impact of the Study: The study was the first evaluation of an exponential feed strategy on recombinant Y. lipolytica for the production of EH enzyme. The results suggest a strategy for the commercial production of a valuable pharmaceutical enzyme.