Production of water-soluble yellow pigments via high glucose stress fermentation of Monascus ruber CGMCC 10910

Monascus pigments are secondary metabolites of Monascus species and are mainly composed of yellow pigments, orange pigments and red pigments. In this study, a larger proportion of Monascus yellow pigments could be obtained through the selection of the carbon source. Hydrophilic yellow pigments can be largely produced extracellularly by Monascus ruber CGMCC 10910 under conditions of high glucose fermentation with low oxidoreduction potential (ORP). However, keeping high glucose levels later in the culture causes translation or a reduction of yellow pigment. We presume that the mechanism behind this phenomenon may be attributed to the redox level of the culture broth and the high glucose stress reaction of M. ruber CGMCC 10910 during high glucose fermentation. These yellow pigments were produced via high glucose bio-fermentation without citrinin. Therefore, these pigments can act as natural pigments for applications as food additives.

     

MpigE, a gene involved in pigment biosynthesis in Monascus ruber M7

Monascus pigments (MPs) have been used as food colorants for several centuries in Asian countries. However, MP biosynthesis pathway is still a controversy, and only few related genes have been reported. In this study, the function of MpigE, a gene involved in MP biosynthesis in Monascus ruber M7, was analyzed. The results revealed that the disruption, complementation, and overexpression of MpigE in M. ruber M7 had very little effects on the growth and phenotypes except MPs. The MpigE deletion strain (?MpigE) just yielded four kinds of yellow MPs and very little red pigments, while the wild-type strain M. ruber M7 produced a MP complex mixture including three (orange, red, and yellow) categories of MP compounds. Two of the four yellow MPs produced by ?MpigE were the same as those yielded by M. ruber M7. The MpigE complementation strain (?MpigE::MpigE) recovered the ability to generate orange and red MPs as M. ruber M7. The MP types produced by the MpigE overexpression strain (M7::PtrpC-MpigE) were consistent with those of M. ruber M7, while the color value was about 1.3-fold as that of M. ruber M7 (3,129 U/g red kojic). For the production of citrinin, the disruption of MpigE almost had no influence on the strain, whereas the overexpression of MpigE made citrinin decrease drastically in YES fermentation. This work will make a contribution to the study on the biosynthesis pathway of MPs in M. ruber.     

Production of citrinin by various species ofMonascus

Summary The production of citrinin by variousMonascus species was determinated using various culture mediums and conditions. The maximal production was obtained in fermentor usingM. ruber with concentrations of 380 mg/l. Since citrinin is a toxic product, it is essential that the production of red pigments as food additives fromMonascus sp. avoid the occurrence of citrinin; so, we argue that some nitrogen sources are unfavorable to the production of citrinin.     

Verticillium lecanii spore production in solid-state and liquid-state fermentations

Verticillium lecanii has been recognized as an entomopathogen with high potential in biological control of pests. Two types of cultivation methods, the solid-state fermentation (SSF) and the liquid-state fermentation (LSF), were examined for V. lecanii. In SSF, the substrate types including rice, rice bran, rice husk, and the mixtures of these components were tested. The results showed that both cooked rice with appropriate water addition and rice bran gave significantly higher spore production of 1.5 2 10⁹ spores/g substrate and 1.4 2 10⁹ spores/g substrate, respectively. In LSF, SMAY liquid medium was used as a base, and the effects of environmental conditions on the spore production of V. lecanii were investigated. From the time course study, on the 9th day the spore yield reached 1.2 2 10⁹ spores/ml of broth at 24v°C, 150 rpm for this strain. A series of medium volumes in the shaker-flask have been tested for the requirement of aeration. The largest surface aeration test, one tenth of the medium volume in the shaker-flask for cultivation, gave the highest spore count. The optimal pH value was tested and the initial pH 5 in the SMAY medium produced a high spore density. Finally, V. lecanii spores from SSF and LSF were different in size, shape, and size distribution; while mean spore length from SSF was 6.1 7m, and mean spore length from LSF was 5.0 7m.     

Effect of fermentation system on the production and properties of tannase of Aspergillus niger van Tieghem MTCC 2425

The tannase-producing efficiency of liquid-surface fermentation (LSF) and solid-state fermentation (SSF) vis-à-vis submerged fermentation (SmF) was investigated in a strain of Aspergillus niger, besides finding out if there was a change in the activity pattern of tannase in these fermentation processes. The studies on the physicochemical properties were confined to intracellular tannase as only this form of enzyme was produced by A. niger in all three fermentation processes. In LSF and SmF, the maximum production of tannase was observed by 120 h, whereas in SSF its activity peaked at 96 h of growth. SSF had the maximum efficiency of enzyme production. Tannase produced by the SmF, LSF and SSF processes had similar properties except that the one produced during SSF had a broader pH stability of 4.5-6.5 and thermostability of 20 degrees-60 degrees C.     

Optimisation of extracellular tannase production from <Emphasis Type="Italic">Paecilomyces variotii</Emphasis>

The tannase production by Paecilomyces variotii was confirmed by high performance thin layer chromatography (HPTLC), and substrate specificity of the tannase was determined by zymogram analysis in sodium dodecyl sulphate-polyacrylamide gel electrophoresis (SDS–PAGE). A clear band of activity observed after electrophoresis of culture filtrate in non-denaturing gels indicated the production of extracellular tannase by P. varoitii. HPTLC analysis revealed that gallic acid was the enzymatic degradation product of tannic acid during the fermentation process. The optimum condition for tannase production was at 72 h of incubation in shaking condition and addition of 1.5% tannic acid, 1% glucose and 0.2% sodium nitrate at temperature of 35°C and pH of 5–7. The production of extracellular tannase from Paecilomyces variotii was investigated under optimized conditions in solid-state fermentation (SSF), submerged fermentation (SmF) and liquid surface fermentation (LSF) processes. The maximum extracellular tannase production was obtained within 60 h of incubation under SSF followed by SmF and LSF.     

Biosynthetic Pathway of Citrinin in the Filamentous Fungus Monascus ruber as Revealed by 13C Nuclear Magnetic Resonance

Carbon isotope distribution of [¹³C]citrinin from Monascus ruber incubated with [¹³C]acetate revealed that the biosynthesis of the toxin originated from a tetraketide, instead of a pentaketide as has been shown for Penicillium and Aspergillus species. The production of polyketide red pigments and citrinin by M. ruber may therefore be regulated at the level of the tetraketide branch point.     

Protein enrichment of apple pomace by co-culture of cellulolytic moulds and yeasts

The co-culture of cellulolytic moulds and yeasts on apple pomace in solid-state fermentation (SSF) and liquid-state fermentation (LSF) increased the protein content of apple pomace. The co-culture of Candida utilis and Aspergillus niger was the best among several combinations and increased the protein content of dried and pectin-extracted apple pomace to 20% and 17%, respectively, under SSF conditions.The authors are with the Microbiology Research Laboratory, Department of Biosciences, Himachal Pradesh University, Shimia-171005, India.     

Platotex: an innovative and fully automated device for cell growth scale-up of agar-supported solid-state fermentation

Among various factors that influence the production of microbial secondary metabolites (MSM), the method of cultivation is an important one that has not been thoroughly investigated. In order to increase microbial throughput and simplify the extraction and workup steps, we performed a study to compare liquid-state fermentation (LSF) with agar-supported solid-state fermentation (AgSF). We found that AgSF is not only more suitable for our applications but offers, for some microbial strains, a higher yield and broader diversity of secondary metabolites. The main limitation of AgSF is the lack of a system to allow production scale-up. In order to overcome this obstacle we developed Platotex, an original fermentation unit offering 2 m² of cultivation surface that combines automatic sterilization, cultivation, and drying steps. Platotex is also able to support both LSF and solid-state fermentation (SSF). Platotex conforms to international security and quality requirements and benefits from total remote automation through industrial communication and control standards.