Rice recycling: a simple strategy to improve conidia production in solid-state cultures.

Here we studied at a laboratory scale a potential strategy to revalorize the residual rice remaining at the end of a conventional conidia production process in solid-state culture. The conidia production of Trichoderma asperellum Th-T4 (3) and Metarhizium robertsii Xoch-8.1 started with the use of fresh rice (unrecycled rice) as the substrate (cycle one), and continued with the use of recycled rice in successive cycles of conidia production. The rice remaining at the end of the first cycle was reused without any further sterilization or reinoculation. As a result, it was observed that the conidia production and productivity significantly increased in both fungi. Conidia production in T. asperellum Th-T4 (3) increased from 1 × 109 (first cycle) to 2·9 × 109 conidia per gram of initial dry substrate (con⋅gds-1 ) (second cycle using recycled rice), while in M. robertsii Xoch-8.1, this parameter increased form 5·7 × 108 to 1·4 × 109 con⋅gds-1 . Both fungi grew faster and conidiated earlier when recycled rice was used as the substrate, therefore, conidia productivity was also significantly improved. Furthermore, the use of recycled rice did not affect conidia viability. This is the first report about a recycling methodology completely free of extra-processing steps, and useful to increase conidia production and productivity.

Detoxification and mineralization of Acid Blue 74: study of an alternative secondary treatment to improve the enzymatic decolourization.

Many reports describe the decolourization of dyes by fungal enzymes. However, these enzymes do not contribute to dye mineralization but only to its biotransformation into less coloured or colourless molecules persisting in solution. Therefore, it is essential to analyse the identity of the metabolites produced during enzymatic treatments and its biodegradation into an appropriate system. The present work examines the decolourization/detoxification of a simulated effluent (containing Acid Blue 74) by fungal enzymes and proposes a secondary treatment using an anaerobic system to improve the enzymatic decolourization through the complete mineralization of the dye. Ligninolytic enzymes were produced by solid culture using the thermo-tolerant fungus Fomes sp. EUM1. The enzymes produced showed a high rate of decolourization (>95 % in 5 h) and were stable at elevated temperature (40 °C) and ionic strength (NaCl, 50 mM). Isatin-5-sulphonic acid was identified via (1)H-NMR as oxidation product; tests using Daphnia magna revealed the non-toxic nature of this compound. To improve the enzymatic degradation and avoid coupling reactions between the oxidation products, the effluent was subjected to an anaerobic (methanogenic) treatment, which achieved high mineralization efficiencies (>85 %). To confirm the mineralization of isatin-5-sulphonic acid, a specific degradation study, which has not been reported before, with this single compound was conducted under the same conditions; the results showed high removal efficiencies (86 %) with methane production as evidence of mineralization. These results showed the applicability of an anaerobic methanogenic system to improve the enzymatic decolourization/detoxification of Acid Blue 74 and achieve its complete mineralization.

Continuous removal of nonylphenol by versatile peroxidase in a two-stage membrane bioreactor.

The ligninolytic enzymes versatile peroxidase (VP) and manganese peroxidase (MnP) have been previously described as efficient oxidizers of the endocrine disrupting chemical (EDC) nonylphenol at high concentrations of the pollutant. Envisaging the application of an enzymatic technology as a tertiary treatment in wastewater treatment plants, it is important to design a continuous reactor that performs the efficient removal of nonylphenol under environmental conditions. In the present research, a two-stage membrane bioreactor based on the production and use of Mn(3+)-malonate (chemical oxidant) was applied. The bioreactor consisted of an enzymatic reactor (R1) for the production of Mn(3+)-malonate by VP, coupled to an oxidation reactor (R2), where the oxidation of nonylphenol by Mn(3+)-malonate took place. The production of Mn(3+)-malonate in R1 was maintained constant: 500-700 µM with minimal deactivation of the enzyme. The oxidation reactor attained nearly complete removal of nonylphenol, even at a hydraulic retention time (HRT) shorter than 20 min. The operation with real wastewater containing nonylphenol at environmental concentrations (454 nM) was also successful, with a nonylphenol removal of 99.5% at a rate of 0.73 µM h(-1). Moreover, when the HRT of R2 was sharply reduced to 6.8 and 3.6 min, the removal of nonylphenol was maintained beyond 99%, which proves the feasibility of the system to remove the target compound present in a real effluent, even at very short HRTs.