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1.
Appl Microbiol Biotechnol ; 97(23): 9993-10002, 2013 Dec.
Article in English | MEDLINE | ID: mdl-24077725

ABSTRACT

A simplified submerged airlift cultivation was established for the production of biomass from Agaricus subrufescens. In this work, soluble polysaccharides extracted from fungal mycelium, fruiting bodies, and the residual culture media were concentrated by nanofiltration. Total and high molar mass polysaccharides and soluble solids were determined in the concentrate for the three extracts. Additionally, the permeate flow, the influences of temperature and pressure, and the resistance to the permeate flow during filtration were also evaluated. Ayield of 5.5 g/L of biomass with 35%glucose conversion was obtained when 0.5 g/L of initial inoculum was employed. Average specific speed of growth was 0.4/day, with biomass productivity of about 0.76 g/(L day). Nanofiltration has yielded polysaccharide increases of 85, 82, and 92% in the extracts from fruiting bodies, mycelium, and liquid media, respectively. A reduction in the permeate flow was observed during filtration, and it was compensated by higher pressures and temperatures. The higher resistance to the permeate flux was caused by polarization due to concentration (polarized gel layer), reaching values of 88% for the culture media. Maximal resistance caused by the membrane reached values of 40% for the extract from the fruiting bodies. On the other hand, resistance caused by fouling was responsible for less than 3.5%. In conclusion, nanofiltration is efficient to concentrate these functional compounds extracted from A. subrufescens and can, therefore, be applied in different biotechnological areas.


Subject(s)
Agaricus/metabolism , Filtration/methods , Polysaccharides/isolation & purification , Polysaccharides/metabolism , Agaricus/chemistry , Agaricus/growth & development , Culture Media/chemistry , Culture Media/metabolism , Fermentation , Fruiting Bodies, Fungal/chemistry , Fruiting Bodies, Fungal/growth & development , Fruiting Bodies, Fungal/metabolism , Molecular Weight , Mycelium/chemistry , Mycelium/growth & development , Mycelium/metabolism , Polysaccharides/chemistry
2.
Appl Microbiol Biotechnol ; 97(1): 123-33, 2013 Jan.
Article in English | MEDLINE | ID: mdl-22820522

ABSTRACT

The interest upon products obtained from fungi has increased during the recent years. Among the most noticeable, nutraceuticals, enzymes, and natural drugs occupy a privileged position. Fungal biomass for the obtainment of those products can be produced either by solid-state fermentation (SSF) or submersed fermentation. SSF has been employed for the production of spawn on pretreated wheat grains with the objective of increasing the fungal polysaccharide (glucomannans) contents. Among the important factors for the production of spawn, time of cooking, time of resting after grain cooking, consequently grain moisture, substrate pH, temperature of incubation, and initial inoculum amount are among the most significant. For wheat grains, cooking time of 21 min followed by a 24-min resting time has been shown as optimal for the production of glucomannans by the fungus Agaricus subrufescens (=Agaricus brasiliensis). Amendments of CaSO(4) (up to 3 %) and CaCO(3) (up to 1 %) had an important influence on the substrate pH. In general, better results for glucomannan production were obtained when no supplement was added or when up to 0.25 % CaCO(3) (pH 6.6) has been added to the mix. Our results demonstrate that the inoculum amount necessary for the best polysaccharide levels is around 10.3 %, while the best temperature is around 27.2 °C. Besides using the spawn for its main purpose, it could potentially and alternatively be used as nutraceutical due to the high levels of glucomannan observed (6.89 %), a compound technically proven to be a potent immunostimulatory and antitumoral agent.


Subject(s)
Agaricus/metabolism , Mannans/metabolism , Triticum/metabolism , Calcium Carbonate/metabolism , Calcium Sulfate/metabolism , Culture Media/chemistry , Fermentation , Hydrogen-Ion Concentration , Temperature , Time Factors
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