Enhancing l-malate production of Aspergillus oryzae FMME218-37 by improving inorganic nitrogen utilization

Microbial l-malate production from renewable feedstock is a promising alternative to petroleum-based chemical synthesis. However, high l-malate production of Aspergillus oryzae was achieved to date using organic nitrogen, with inorganic nitrogen still unable to meet industrial applications. In the current study, we constructed a screening system and nitrogen supply strategy to improve l-malate production with ammonium sulphate [(NH₄)₂SO₄] as the sole nitrogen source. First, we generated and identified a high-producing mutant FMME218-37, which stably boosted l-malate production from 30.73 to 78.12 g/L, using a combined screening system with morphological characteristics. Then, by analyzing the fermentation parameters and physiological characteristics, we further speculated the key factor was the unbalance of carbon and nitrogen absorption. Finally, the titer and productivity of l-malate was increased to 95.2 g/L and 0.57 g/(L h) by regulating the nitrogen supply module to balance carbon and nitrogen absorption, which represented the highest level in A. oryzae with (NH₄)₂SO₄ as nitrogen source achieved to date. Moreover, our findings using a low-cost substrate may lead to building an economical cell factory of A. oryzae for l-malate production.

     

Engineered Bacillus subtilis 168 produces l-malate by heterologous biosynthesis pathway construction and lactate dehydrogenase deletion

In the present work, Bacillus subtilis was engineered to produce l-malate. Initially, the study revealed that the slight fumarase activity under anaerobic conditions is extremely favourable for l-malate one-step fermentation accumulation. Subsequently, an efficient heterologous biosynthesis pathway formed by Escherichia coli phosphoenolpyruvate carboxylase and Saccharomyces cerevisiae malate dehydrogenase was introduced into B. subtilis, which led to 6.04?±?0.19?mM l-malate production. Finally, the l-malate production was increased 1.5-fold to 9.18?±?0.22?mM by the deletion of lactate dehydrogenase. Under two-stage fermentation conditions, the engineered B. subtilis produced up to 15.65?±?0.13?mM l-malate, which was 86.3?% higher than that under anaerobic fermentation conditions. Though the l-malate production by the recombinant was low, this is the first attempt to produce l-malate in engineered B. subtilis and paves the way for further improving l-malate production in B. subtilis.     

Effects of fumarate,l-malate,and anAspergillus oryzae fermentation extract ond-lactate Utilization by the ruminal bacteriumSelenomonas ruminantium

Growth ofSelenomonas ruminantium HD4 in medium that contained 21mm d-lactate was stimulated to varying degrees by 10mm l-malate, 10mm fumarate, and 2% (v/v)Aspergillus oryzae fermentation extract (Amaferm). Amaferm treatment caused the greatest growth stimulation. Initial uptake rates (30s) and long-term uptake rates (30 min) ofd-lactate by whole cells ofS. ruminantium were increased in the presence of 10mm l-malate. Amaferm (25 l/ml) also stimulated long-term uptake rates ofd-lactate, whereas fumarate had no effect. Initial uptake ofd-lactate was depressed in the presence of fumarate or Amaferm. When eitherl-malate, fumarate, or Amaferm was included in thed-lactate growth medium, a homosuccinate fermentation resulted and an inverse relationship was observed between growth (protein synthesis) and succinate production. Recent research demonstrated that Amaferm containsl-malate, and this dicarboxylic acid may be involved in stimulatingd-lactate utilization byS. ruminantium.     

Improved oxygen transfer and increased l-lactic acid production by morphology control of Rhizopus oryzae in a static bed bioreactor

Rhizopus oryzae was immobilized on a cotton matrix in a static bed bioreactor. Compared with free cells in a stirred tank bioreactor, immobilized R. oryzae in this bioreactor gave higher lactic acid production but lower ethanol production. The highest lactic acid production rate (2.09 g/L h) with the final concentration of 37.83 g/L from 70 g/L glucose was achieved when operating the bioreactor at 700 rpm and 0.5 vvm air. To better understand the relationship between shear effects (agitation and aeration) and R. oryzae morphology and metabolism, oxygen transfer rate, fermentation kinetics, and lactate dehydrogenase activity were determined. In immobilized cell culture, higher oxygen transfer rate and lactic acid production were achieved but lower lactate dehydrogenase activity was found as compared with those in free cell culture operated at the same conditions. These results clearly imply that mass transport was the rate controlling step in lactic acid fermentation by R. oryzae.     

Direct fermentation of potato starch wastewater to lactic acid by Rhizopus oryzae and Rhizopus arrhizus

The biochemical kinetic of direct fermentation for lactic acid production by fungal species of Rhizopus arrhizus 3,6017 and Rhizopus oryzae 2,062 was studied with respect to growth pH, temperature and substrate. The direct fermentation was characterized by starch hydrolysis, accumulation of reducing sugar, and production of lactic acid and fungal biomass. Starch hydrolysis, reducing sugar accumulation, biomass formation and lactic acid production were affected with the variations in pH, temperature, and starch source and concentration. A growth condition with starch concentration approximately 20 g/l at pH 6.0 and 30°C was favourable for both starch saccharification and lactic acid fermentation, resulting in lactic acid yield of 0.87–0.97 g/g starch associated with 1.5–2.0 g/l fungal biomass produced in 36 h fermentation. R. arrhizus 3,6017 had a higher capacity to produce lactic acid, while R. oryzae 2,062 produced more fungal biomass under similar conditions.     

Optimization of liquid-state fermentation conditions for the glyphosate degradation enzyme production of strain Aspergillus oryzae by ultraviolet mutagenesis

This study aimed to obtain strains with high glyphosate-degrading ability and improve the ability of glyphosate degradation enzyme by the optimization of fermentation conditions. Spore from Aspergillus oryzae A-F02 was subjected to ultraviolet mutagenesis. Single-factor experiment and response surface methodology were used to optimize glyphosate degradation enzyme production from mutant strain by liquid-state fermentation. Four mutant strains were obtained and named as FUJX 001, FUJX 002, FUJX 003, and FUJX 004, in which FUJX 001 gave the highest total enzyme activity. Starch concentration at 0.56%, GP concentration at 1,370?mg/l, initial pH at 6.8, and temperature at 30°C were the optimum conditions for the improved glyphosate degradation endoenzyme production of A. oryzae FUJX 001. Under these conditions, the experimental endoenzyme activity was 784.15?U/100?ml fermentation liquor. The result (784.15?U/100?ml fermentation liquor) was approximately 14-fold higher than that of the original strain. The result highlights the potential of glyphosate degradation enzyme to degrade glyphosate.     

Tourmaline ceramic balls stimulate growth and metabolism of three fermentation microorganisms

Effects of tourmaline ceramic balls on growth and metabolism of Saccharomyces cerevisiae, Lactobacillus acidophilus and Aspergillus oryzae were studied. Treatments with 3, 6, 9 or 12 g of tourmaline ceramic balls in a 50 ml culture showed significant stimulation of the growth of the three microorganisms. In optimal treatments with 12 g of tourmaline balls, the growth of S. cerevisiae, L. acidophilus, and A. oryzae was increased by 34, 32 and 10%, respectively. After 72 h fermentation of S. cerevisiae, total carbohydrate content in the culture medium was decreased by 65% and ethanol production was increased by 150%. Total carbohydrate content was decreased by 80% and the pH value was decreased by 0.3, as a result of organic acid production in the medium of L. acidophilus after 72 h fermentation. In the case of A. oryzae, enzyme activities of protease and amylase were increased by 90 and 31%, respectively, after 96 h fermentation. Results indicated that tourmaline stimulates initiation of growth in the early lag stage and increases production of metabolites at a later stage of fermentation. The strong stimulatory effect of tourmaline on growth, utilization of substrates and production of metabolites in the three microorganisms suggests a potential application in the fermentation industry.     

Impeller types and feeding modes influence the morphology and protein expression in the submerged culture of<Emphasis Type="Italic">Aspergillus oryzae</Emphasis>

The influences of impeller types on morphology and protein expression were investigated in a submerged culture ofAspergillus oryzae. The impeller types strongly affected mycelial morphology and protein production in batch and fed-batch fermentations. Cells that were cultured by propeller agitation grew in the form of a pellet, whereas cells that were cultured by turbine agitation grew in a freely dispersed-hyphal manner and in a clumped form. Pellet-grown cells showed high levels of protein production for both the intracellular heterologous protein (β-glucuronidase) and the extracellularly homologous protein (α-amylase). The feeding mode of the carbon source also influenced the morphological distribution and protein expression in fed-batch fermentation ofA. oryzae. Pulsed-feeding mainly showed high protein expression and homogeneous distribution of pellet whereas continuous feeding resulted in less protein expression and heterogeneous distribution with pellet and dispersed-hyphae. The pellet growth with propeller agitation paralleling with the pulsed-feeding of carbon source showed a high level of protein production in the submerged fed-batch fermentation of recombinantA. oryzae.     

Zur Frage der Beeinflussung der Glucosevergärung durch l-Malat bei Leuconostoc mesenteroides

Zusammenfassung Es wird gezeigt, daß bei Leuconostoc mesenteroides 39 (ATCC 12291) der gleichzeitige Abbau von l-Malat die Glucosevergärung weder qualitativ noch quantitativ verändert. Bei Verwendung positionsmarkierter Glucose wird auch die Isotopenverteilung in den Gärungsprodukten durch gleichzeitige Malatgabe nicht verändert. Der Malatabbau steuert auch keine Energie zum Wachstum bei, wie die bei l-Malatgabe unveränderten Y_Glucose-Werte zeigen. Die von Doelle (1971) beschriebene verstärkte Milchsäurebildung aus Glucose bei Anwesenheit von Malat konnte auf einen pH-Effekt zurückgeführt werden. Für eine ebenfalls von Doelle (1971) berichtete Bildung von l-Lactat aus Glucose unter dem Einfluß von l-Malat ergab sich kein Anhaltspunkt.

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The effect of l-malate on glucose fermentation by Leuconostoc mesenteroides

Summary It is shown that the simultaneous fermentation of l-malate and d-glucose by Leuconostoc mesenteroides 39 does not lead to quantitatively or qualitatively different fermentation products. When glucose, labelled in different positions is fermented, the distribution of ¹⁴C within the fermentation products is not changed by the addition of l-malate to the fermentation mixture. The l-malate fermentation does not contribute energy for growth, since Y_glucose remains unchanged by adding l-malate to the medium. The increased production of lactic acid from glucose in the presence of l-malate, reported by Doelle (1971), is due to a pH effect. There is no indication of the formation of l(+)-lactate in addition to d(-)-lactate from glucose, when l-malate is present as claimed by Doelle (1971).

     

Potential of solid state fermentation for production of L(+)-lactic acid by Rhizopus oryzae

Production of l(+)-lactic acid by Rhizopus oryzae NRRL 395 was studied in solid medium on sugar-cane bagasse impregnated with a nutrient solution containing glucose and CaCO₃. A comparative study was undertaken in submerged and solid-state cultures. The optimal concentrations in glucose were 120 g/l in liquid culture and 180 g/l in solid-state fermentation corresponding to production of l(+)-lactic acid of 93.8 and 137.0 g/l, respectively. The productivity was 1.38 g/l per hour in liquid medium and 1.43 g/l per hour in solid medium. However, the fermentation yield was about 77% whatever the medium. These figures are significant for l(+)-lactic acid production.     

Effective saccharification of kraft pulp by using a cellulase cocktail prepared from genetically engineered Aspergillus oryzae

Kraft pulp is a promising feedstock for bioproduction. The efficiency of kraft pulp saccharification was improved by using a cellulase cocktail prepared from genetically engineered Aspergillus oryzae. Application of the cellulase cocktail was demonstrated by simultaneous saccharification and fermentation, using kraft pulp and non-cellulolytic yeast. Such application would make possible to do an efficient production of other chemicals from kraft pulp.     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-lactic acid by <Emphasis Type="Italic">Rhizopus oryzae</Emphasis> using semicontinuous fermentation in bioreactor

Semicontinuous fermentation using pellets of Rhizopus oryzae has been recognized as a promising technology for l-lactic acid production. In this work, semicontinuous fermentation of R. oryzae AS 3.819 for l-lactic acid production has been developed with high l-lactic acid yield and volumetric productivity. The effects of factors such as inoculations, CaCO₃ addition time, and temperature on l-lactic acid yield and R. oryzae morphology were researched in detail. The results showed that optimal fermentation conditions for the first cycle were: inoculation with 4% spore suspension, CaCO₃ added to the culture medium at the beginning of culture, and culture temperature of 32–34°C. In orthogonal experiments, high l-lactic acid yield was achieved when the feeding medium was (g/l): glucose, 100; (NH₄)₂SO₄, 2; KH₂PO₄, 0.1; ZnSO₄·7H₂O, 0.33; MgSO₄·7H₂O, 0.15; CaCO₃, 50. Twenty cycles of semicontinuous fermentation were carried out in flask culture. l-lactic acid yield was 78.75% for the first cycle and 80–90% for the repeated cycles; the activities of lactate dehydrogenases (LDH) were 7.2–9.2 U/mg; fermentation was completed in 24 h for each repeated cycle. In a 7-l magnetically stirred fermentor, semicontinuous fermentation lasted for 25 cycles using pellets of R. oryzae AS 3.819 under the optimal conditions determined from flask cultures. The final l-lactic acid concentration (LLAC) reached 103.7 g/l, and the volumetric productivity was 2.16 g/(l·h) for the first cycle; in the following 19 repeated cycles, the final LLAC reached 81–95 g/l, and the volumetric productivities were 3.40–3.85 g/(l·h).     

Production of lactic acid and fungal biomass by Rhizopus fungi from food processing waste streams

This study proposed a novel waste utilization bioprocess for production of lactic acid and fungal biomass from waste streams by fungal species of Rhizopus arrhizus 36017 and R. oryzae 2062. The lactic acid and fungal biomass were produced in a single-stage simultaneous saccharification and fermentation process using potato, corn, wheat and pineapple waste streams as production media. R. arrhizus 36017 gave a high lactic acid yield up to 0.94–0.97 g/g of starch or sugars associated with 4–5 g/l of fungal biomass produced, while 17–19 g/l fungal biomass with a lactic acid yield of 0.65–0.76 g/g was produced by the R. oryzae 2062 in 36–48 h fermentation. Supplementation of 2 g/l of ammonium sulfate, yeast extract and peptone stimulated an increase in 8–15% lactic acid yield and 10–20% fungal biomass.

     

Metabolic engineering of Pichia pastoris X-33 for lycopene production

As an alternative carotenoid producer, non-carotenogenic Pichia pastoris was chosen for a reddish carotenoid lycopene production because it can grow to high cell density without accumulation of ethanol and utilize various classes of organic materials such as methanol as carbon sources. Two synthetic lycopene-pathway plasmids, pGAPZB-EBI* and pGAPZB-EpBpI*p, were designed and constructed. The pGAPZB-EpBpI*p plasmid encoded three carotenogenic enzymes that were engineered to be targeted into peroxisomes of P. pastoris whereas the pGAPZB-EBI* plasmid encoded non-targeted enzymes. After both plasmids were transformed into P. pastoris, the lycopene-producing clone containing the pGAPZB-EpBpI*p plasmid, referred to as Ω, was selected and used for further optimization study. Of the carbon sources tested, glucose resulted in the highest level of lycopene production in complex and minimal media. Batch fermentation of the Ω clone resulted in the production of 4.6 mg-lycopene/g-DCW, with a concentration of 73.9 mg/l of lycopene in minimal medium. For the first time non-carotenogenic yeast P. pastoris was metabolically engineered by heterologously expressing lycopene-pathway enzymes and the lycopene concentration of 73.9 mg/l was obtained. This serves as a basis for the development of biological process for carotenoids using P. pastoris at a commercial production level.     

Engineering cell morphology by CRISPR interference in Acinetobacter baylyi ADP1

Microbial production of intracellular compounds can be engineered by redirecting the carbon flux towards products and increasing the cell size. Potential engineering strategies include exploiting clustered regularly interspaced short palindromic repeats interference (CRISPRi)-based tools for controlling gene expression. Here, we applied CRISPRi for engineering Acinetobacter baylyi ADP1, a model bacterium for synthesizing intracellular storage lipids, namely wax esters. We first established an inducible CRISPRi system for strain ADP1, which enables tightly controlled repression of target genes. We then targeted the glyoxylate shunt to redirect carbon flow towards wax esters. Second, we successfully employed CRISPRi for modifying cell morphology by repressing ftsZ, an essential gene required for cell division, in combination with targeted knock-outs to generate significantly enlarged filamentous or spherical cells respectively. The engineered cells sustained increased wax ester production metrics, demonstrating the potential of cell morphology engineering in the production of intracellular lipids.     

Isoenzyme pattern and subcellular localisation of enzymes involved in fumaric acid accumulation by Rhizopus oryzae

Summary Electrophoretic studies of fumarase and nicotine adenine dinucleotide (NAD)-malate dehydrogenase were carried out in the fumaric acid-accumulating fungus Rhizopus oryzae. The analyses revealed two fumarase isoenzymes, one localised solely in the cytosol and the other found both in the cytosol and in the mitochondrial fraction. The activity of the cytosolic isoenzyme of fumarase was higher during the acid production stage than during growth. Addition of cycloheximide inhibited fumaric acid production and decreased the activity of the cytosolic isoenzyme of fumarase. These results suggested that de novo protein synthesis is required for increase in the activity of the cytosolic isoenzyme and that such an increase in activity is essential for fumaric acid accumulation. Three distinct isoenzymes of NAD-malate dehydrogenase could be detected in R. oryzae. No changes were observed in the isoenzyme pattern of malate dehydrogenase during fumaric acid production.     

A novel multi-stage preculture strategy of Rhizopus oryzae ME-F12 for fumaric acid production in a stirred-tank reactor

This study has developed a novel multi-stage preculture strategy to control the morphology of filamentous Rhizopus oryzae in a 3.3-l stirred-tank reactor (STR), consequently enhancing the fumaric acid production. Using multi-stage precultures as inoculum, the morphology of R. oryzae was maintained as large clumps, small fluffy pellets, and entangled filaments. The highest fumaric acid production of 42.5 g/l with a yield of 55.6% was obtained in association with the small fluffy pellets which were formed in the third preculture at pH 3.0. The results indicated that the use of the multi-stage precultures as inoculum in the STR is a promising approach for commercial production of fumaric acid.     

Permeabilization and lysis of Pseudomonas pseudoalcaligenes cells by Triton X-100 for efficient production of d-malate

Pseudomonas pseudoalcaligenes can only form d-malate from maleate after incubation of the cells with a solvent or a detergent. The effect of the detergent Triton X-100 on d-malate production was studied in more detail. The longer the cells were incubated with Triton X-100, the higher was the d-malate production activity, until the maximal malease activity was reached. Incubation of P. pseudoalcaligenes cells with Triton X-100 also resulted in an increase in the protein concentration of the supernatant, indicating that cell lysis had occurred. The rate at which the d-malate production activity increased was dependent on the Triton X-100 concentration and on the cell density. Also the rate at which lysis occurred depended on the Triton X-100 concentration.