comparação entre processos em SHF e em SSF de bagaço de cana-de-açúcar para a produção de etanol por Saccharomyces cerevisiae

In this work, four different process configurations, including three simultaneous saccharification and fermentation (SSF) schemes and one separate hydrolysis and fermentation (SHF) scheme, were compared, at 8% water-insoluble solids, regarding ethanol production from steam-pretreated and alkali-delignified sugar cane bagasse. Two configurations included a 16 h lasting enzymatic presaccharification prior to SSF, and the third one was a classical SSF without presaccharification. Cellulose conversion was higher for the delignified bagasse, and higher in SSF experiments than in SHF. The highest cellulose-to-ethanol conversion (around 60% in 24 h) and maximum ethanol volumetric productivities (0.29-0.30 g/L.h) were achieved in the presaccharification-assisted SSF.

Hydrothermal pretreatment of sugarcane bagasse using response surface methodology improves digestibility and ethanol production by SSF

Sugarcane bagasse was characterized as a feedstock for the production of ethanol using hydrothermal pretreatment. Reaction temperature and time were varied between 160 and 200A degrees C and 5-20 min, respectively, using a response surface experimental design. The liquid fraction was analyzed for soluble carbohydrates and furan aldehydes. The solid fraction was analyzed for structural carbohydrates and Klason lignin. Pretreatment conditions were evaluated based on enzymatic extraction of glucose and xylose and conversion to ethanol using a simultaneous saccharification and fermentation scheme. SSF experiments were conducted with the washed pretreated biomass. The severity of the pretreatment should be sufficient to drive enzymatic digestion and ethanol yields, however, sugars losses and especially sugar conversion into furans needs to be minimized. As expected, furfural production increased with pretreatment severity and specifically xylose release. However, provided that the severity was kept below a general severity factor of 4.0, production of furfural was below an inhibitory concentration and carbohydrate contents were preserved in the pretreated whole hydrolysate. There were significant interactions between time and temperature for all the responses except cellulose digestion. The models were highly predictive for cellulose digestibility (R (2) = 0.8861) and for ethanol production (R (2) = 0.9581), but less so for xylose extraction. Both cellulose digestion and ethanol production increased with severity, however, high levels of furfural generated under more severe pretreatment conditions favor lower severity pretreatments. The optimal pretreatment condition that gave the highest conversion yield of ethanol, while minimizing furfural production, was judged to be 190A degrees C and 17.2 min. The whole hydrolysate was also converted to ethanol using SSF. To reduce the concentration of inhibitors, the liquid fraction was conditioned prior to fermentation by removing inhibitory chemicals using the fungus Coniochaeta ligniaria.

Produzione di bioetanolo da scarti lignocellulosici della canna da zucchero: condizioni di saccarificazione e fermentazione simultanee (SSF) e aspetti ambientali del processo

Il presente studio ha avuto l’obiettivo di indagare la produzione di bioetanolo di seconda generazione a partire dagli scarti lignocellulosici della canna da zucchero (bagassa), facendo riscorso al processo enzimatico. L’attività di ricerca è stata svolta presso il Dipartimento di Ingegneria Chimica dell’Università di Lund (Svezia) all’interno di rapporti scambio con l’Università di Bologna. Il principale scopo è consistito nel valutare la produzione di etanolo in funzione delle condizioni operative con cui è stata condotta la saccarificazione e fermentazione enzimatica (SSF) della bagassa, materia prima che è stata sottoposta al pretrattamento di Steam Explosion (STEX) con aggiunta di SO2 come catalizzatore acido. Successivamente, i dati ottenuti in laboratorio dalla SSF sono stati utilizzati per implementare, in ambiente AspenPlus®, il flowsheet di un impianto che simula tutti gli aspetti della produzione di etanolo, al fine di studiarne il rendimento energetico dell’intero processo. La produzione di combustibili alternativi alle fonti fossili oggigiorno riveste primaria importanza sia nella limitazione dell’effetto serra sia nel minimizzare gli effetti di shock geopolitici sulle forniture strategiche di un Paese. Il settore dei trasporti in continua crescita, consuma nei paesi industrializzati circa un terzo del fabbisogno di fonti fossili. In questo contesto la produzione di bioetanolo può portare benefici per sia per l’ambiente che per l’economia qualora valutazioni del ciclo di vita del combustibile ne certifichino l’efficacia energetica e il potenziale di mitigazione dell’effetto serra. Numerosi studi mettono in risalto i pregi ambientali del bioetanolo, tuttavia è opportuno fare distinzioni sul processo di produzione e sul materiale di partenza utilizzato per comprendere appieno le reali potenzialità del sistema well-to-wheel del biocombustibile. Il bioetanolo di prima generazione ottenuto dalla trasformazione dell’amido (mais) e delle melasse (barbabietola e canna da zucchero) ha mostrato diversi svantaggi: primo, per via della competizione tra l’industria alimentare e dei biocarburanti, in secondo luogo poiché le sole piantagioni non hanno la potenzialità di soddisfare domande crescenti di bioetanolo. In aggiunta sono state mostrate forti perplessità in merito alla efficienza energetica e del ciclo di vita del bioetanolo da mais, da cui si ottiene quasi la metà della produzione di mondiale di etanolo (27 G litri/anno). L’utilizzo di materiali lignocellulosici come scarti agricolturali e dell’industria forestale, rifiuti urbani, softwood e hardwood, al contrario delle precedenti colture, non presentano gli svantaggi sopra menzionati e per tale motivo il bioetanolo prodotto dalla lignocellulosa viene denominato di seconda generazione. Tuttavia i metodi per produrlo risultano più complessi rispetto ai precedenti per via della difficoltà di rendere biodisponibili gli zuccheri contenuti nella lignocellulosa; per tale motivo è richiesto sia un pretrattamento che l’idrolisi enzimatica. La bagassa è un substrato ottimale per la produzione di bioetanolo di seconda generazione in quanto è disponibile in grandi quantità e ha già mostrato buone rese in etanolo se sottoposta a SSF. La bagassa tal quale è stata inizialmente essiccata all’aria e il contenuto d’acqua corretto al 60%; successivamente è stata posta a contatto per 30 minuti col catalizzatore acido SO2 (2%), al termine dei quali è stata pretrattata nel reattore STEX (10L, 200°C e 5 minuti) in 6 lotti da 1.638kg su peso umido. Lo slurry ottenuto è stato sottoposto a SSF batch (35°C e pH 5) utilizzando enzimi cellulolitici per l’idrolisi e lievito di birra ordinario (Saccharomyces cerevisiae) come consorzio microbico per la fermentazione. Un obiettivo della indagine è stato studiare il rendimento della SSF variando il medium di nutrienti, la concentrazione dei solidi (WIS 5%, 7.5%, 10%) e il carico di zuccheri. Dai risultati è emersa sia una buona attività enzimatica di depolimerizzazione della cellulosa che un elevato rendimento di fermentazione, anche per via della bassa concentrazione di inibitori prodotti nello stadio di pretrattamento come acido acetico, furfuraldeide e HMF. Tuttavia la concentrazione di etanolo raggiunta non è stata valutata sufficientemente alta per condurre a scala pilota un eventuale distillazione con bassi costi energetici. Pertanto, sono stati condotti ulteriori esperimenti SSF batch con addizione di melassa da barbabietola (Beta vulgaris), studiandone preventivamente i rendimenti attraverso fermentazioni alle stesse condizioni della SSF. I risultati ottenuti hanno suggerito che con ulteriori accorgimenti si potranno raggiungere gli obiettivi preposti. E’ stato inoltre indagato il rendimento energetico del processo di produzione di bioetanolo mediante SSF di bagassa con aggiunta di melassa in funzione delle variabili più significative. Per la modellazione si è fatto ricorso al software AspenPlus®, conducendo l’analisi di sensitività del mix energetico in uscita dall’impianto al variare del rendimento di SSF e dell’addizione di saccarosio. Dalle simulazioni è emerso che, al netto del fabbisogno entalpico di autosostentamento, l’efficienza energetica del processo varia tra 0.20 e 0.53 a seconda delle condizioni; inoltre, è stata costruita la curva dei costi energetici di distillazione per litro di etanolo prodotto in funzione delle concentrazioni di etanolo in uscita dalla fermentazione. Infine sono già stati individuati fattori su cui è possibile agire per ottenere ulteriori miglioramenti sia in laboratorio che nella modellazione di processo e, di conseguenza, produrre con alta efficienza energetica bioetanolo ad elevato potenziale di mitigazione dell’effetto serra.

Dynamical Resonances and SSF Singularities for a Magnetic Schrödinger Operator

We consider the Hamiltonian H of a 3D spinless non-relativistic quantum particle subject to parallel constant magnetic and non-constant electric field. The operator H has infinitely many eigenvalues of infinite multiplicity embedded in its continuous spectrum. We perturb H by appropriate scalar potentials V and investigate the transformation of these embedded eigenvalues into resonances. First, we assume that the electric potentials are dilation-analytic with respect to the variable along the magnetic field, and obtain an asymptotic expansion of the resonances as the coupling constant ϰ of the perturbation tends to zero. Further, under the assumption that the Fermi Golden Rule holds true, we deduce estimates for the time evolution of the resonance states with and without analyticity assumptions; in the second case we obtain these results as a corollary of suitable Mourre estimates and a recent article of Cattaneo, Graf and Hunziker [11]. Next, we describe sets of perturbations V for which the Fermi Golden Rule is valid at each embedded eigenvalue of H; these sets turn out to be dense in various suitable topologies. Finally, we assume that V decays fast enough at infinity and is of definite sign, introduce the Krein spectral shift function for the operator pair (H+V, H), and study its singularities at the energies which coincide with eigenvalues of infinite multiplicity of the unperturbed operator H.

WFF-WFFP-ICSF-CIC: national workshop on capacity-building for the implementation of the voluntary guidelines for securing sustainable small-scale fisheries (SSF guidelines) - report, 21 and 22 March 2016 Multi-Purpose Hall, India International Centre, New Delhi, India

The report of the proceedings of the New Delhi workshop on the SSF Guidelines (Voluntary Guidelines for Securing Sustainable Small-scale Fisheries in the Context of Food Security and Poverty Eradication). The workshop brought together 95 participants from 13 states representing civil society organizations. governments, FAO, and fishworker organizations from both the marine and inland fisheries sectors. This report will be found useful for fishworker organizations, researchers, policy makers, members of civil society and anyone interested in small-scale fisheries, tenure rights, social development, livelihoods, post harvest and trade and disasters and climate change.

Social relations and dynamics shaping the implementation of the voluntary guidelines on small-scale fisheries (SSF guidelines) in South Africa

Integral to achieving the SSF Guidelines goal of targeting the most vulnerable and marginalized persons and eliminating discrimination is the need to have adequate understanding of the power relations and intersectionalities that shape access to and control over marine and other resources according to gender, age, race, ethnicity, labour and migratory status, disability, geographic location and other characteristics relevant in each national contexts. This monograph identifies and explores the key social relations and dynamics in the SSF fisheries sector in South Africa impacting the implementation of the SSF Guidelines. The monograph will be useful for researchers, scientists, fishworker organizations, environmentalists and anyone interested in the protection of marine biodiversity and the promotion of sustainable fisheries management.

SSF guidelines: towards blue growth

A consultation workshop on East Africa recognized that, if applied well, the principles of the SSF Guidelines can advance small-scale fisheries in the region.

SSF guidelines: better understanding needed

The Near East and North Africa Regional Consultation on SSF Guidelines focused on raising awareness and support for implementation of the guidelines.

SSF guidelines: a huge struggle

A recent workshop at New Delhi discussed capacity building for the implementation of the Voluntary Guidelines for Securing Sustainable Small-scale Fisheries (SSF Guidelines).

Procedimientos de auditoría externa, aplicables al cumplimiento del código de conducta relacionado a la prevención y detección del lavado de dinero en las instituciones de intermediación financiera no bancaria reguladas por la SSF.

La expresión lavado de dinero empezó a utilizarse a principios del siglo XX para denominar las operación que de alguna manera intentan dar carácter legal a los fondos producto de operaciones ilícitas, para facilitar su ingreso al flujo monetario de una economía. Los legitimadores de capital tienden a utilizar las entidades de negocios más como un conducto que como un medio de expropiación directa de activos. Por esta razón, es mucho menos factible que el lavado de dinero afecte los estados financieros en comparación con otros tipos de fraude como los desfalcos. La legislación aplicable a prevenir la legitimación de capitales en el país está compuesta por: Ley, Reglamento e Instructivo para prevenir el lavado de dinero, así como el Convenio Centroamericano para la prevención y represión de los delitos de tráfico de drogas y delitos conexos. Considerando el nivel de operaciones en las entidades dedicadas al microfinanciamiento en El Salvador (Cajas de Crédito, Asociaciones Cooperativas de Ahorro y Crédito, Bancos de los Trabajadores, otras entidades financieras no bancarias), éstas pueden tornarse vulnerables para que se cometan actividades delictivas generadoras de blanqueo de capitales, ya que a través de la diversidad de usuarios y suministradores de servicios financieros podrían cometerse situaciones delictivas que las afecten negativamente. Con base en lo anterior se realizó un estudio, el cual se presenta en este trabajo y tiene como objetivo contribuir con los organismos reguladores de supervisión y fiscalización, mediante la formulación de procedimientos de auditoria externa dirigidos a evaluar el cumplimiento del Código de Conducta en los intermediarios financiera no bancarios, encaminados a disminuir el riesgo de que sus servicios sean usados para dar legitimidad a fondos que sean producto de actividades ilícitas. La investigación se llevó a cabo en Las Instituciones de Intermediación Financiera no Bancarias, debido a que en la década anterior, la mayoría de las empresas involucradas en hechos generadores del lavado de dinero pertenecieron a este grupo, tales como: FOMIEXPORT (1992), CREDICLUB, FINSEPRO e INSEPRO (1997). Para la definición de la población se tomó como base la totalidad de los intermediarios financieros no bancarios que actualmente están regulados por la Superintendencia del Sistema Financiero, las que en su conjunto son 7 instituciones. En cuanto a la recolección de los datos, ésta se realizó a través de cuestionarios dirigidos a empleados tomados al azar de las Instituciones de Intermediación Financieras no Bancarias. Mediante los datos obtenidos se elaboró el diagnóstico de la investigación, determinando la importancia de que los organismos de supervisión y fiscalización posean procedimientos de auditoria externa dirigidos a evaluar dentro de las entidades antes mencionadas el cumplimiento del Código de Conducta para prevenir y detectar el blanqueo de capitales. Debido a lo anterior, se presenta una propuesta sobre procedimientos de auditoria externa para verificar el cumplimiento del Código de Conducta en la prevención y detección del lavado de dinero; y un modelo de Código de Conducta, para que los organismos de supervisión y fiscalización evalúen que las Instituciones de Intermediación Financiera no Bancarias cumplan con la normativa legal vigente y para que fortalezcan la estructura de control al respecto.

Horizontal subsurface flow constructed wetlands for mitigation of ametryn-contaminated water

The feasibility of using constructed wetlands (CWs) for the mitigation of pesticide runoff has been studied in the last decade. However, a lack of related data was verified when subsurface flow constructed wetlands (SSF CWs) are considered for this purpose. In the present work, SSF CWs were submitted to continuous ametryn addition and evaluated during an I I-week period, with the aim of determining the feasibility of these systems for mitigation of contaminated water. Ametryn was not added to one CW cell in order to provide a control for the experiments. Monitoring of treatment performance was executed by standard water quality parameters, ametryn chromatography quantification and macrophyte (Typha latifolia L) nutritional and agronomic property analysis. Results indicated that 39% of the total initially added amount of ametryn was removed, transferred or transformed. Herbicide metabolism and mineralisation were carried out by chemical and biological mechanisms. No statistic differences were observed in nutritional contents found in the T. latifolia crops of the CWs after the experimental period. Moreover, the biomass production (one valuable source of renewable energy) was equal to 3.3 t.ha(-1) (dry matter) in wetland cells. It was concluded that constructed wetland systems are capable of mitigating water contaminated with ametryn, acting as buffer filters between the emission sources and the downstream superficial water bodies.

Optimal recovery process conditions for manganese-peroxidase obtained by solid-state fermentation of eucalyptus residue using Lentinula edodes

Enzyme production is a growing field in biotechnology and increasing attention has been devoted to the solid-state fermentation (SSF) of lignocellulosic biomass for production of industrially relevant lignocellulose deconstruction enzymes, especially manganese-peroxidase (MnP), which plays a crucial role in lignin degradation. However, there is a scarcity of studies regarding extraction of the secreted metabolities that are commonly bound to the fermented solids, preventing their accurate detection and limiting recovery efficiency. In the present work, we assessed the effectiveness of extraction process variables (pH, stirring rate, temperature, and extraction time) on recovery efficiency of manganese-peroxidase (MnP) obtained by SSF of eucalyptus residues using Lentinula edodes using statistical design of experiments. The results from this study indicated that of the variables studied, pH was the most significant (p < 0.05%) parameter affecting MnP recovery yield, while temperature, extraction time, and stirring rate presented no statistically significant effects in the studied range. The optimum pH for extraction of MnP was at 4.0-5.0, which yielded 1500-1700 IU kg (1) of enzyme activity at extraction time 4-5 h, under static condition at room temperature. (C) 2011 Elsevier Ltd. All rights reserved.

Simultaneous saccharification and ethanol fermentation of oxalic acid pretreated corncob assessed with response surface methodology

Response surface methodology was used to evaluate optimal time, temperature and oxalic acid concentration for simultaneous saccharification and fermentation (SSF) of corncob particles by Pichia stipitis CBS 6054. Fifteen different conditions for pretreatment were examined in a 2(3) full factorial design with six axial points. Temperatures ranged from 132 to 180 degrees C, time from 10 to 90 min and oxalic acid loadings from 0.01 to 0.038 g/g solids. Separate maxima were found for enzymatic saccharification and hemicellulose fermentation, respectively, with the condition for maximum saccharification being significantly more severe. Ethanol production was affected by reaction temperature more than by oxalic acid and reaction time over the ranges examined. The effect of reaction temperature was significant at a 95% confidence level in its effect on ethanol production. Oxalic acid and reaction time were statistically significant at the 90% level. The highest ethanol concentration (20 g/l) was obtained after 48 h with an ethanol volumetric production rate of 0.42 g ethanol l(-1) h(-1). The ethanol yield after SSF with P. stipitis was significantly higher than predicted by sequential saccharification and fermentation of substrate pretreated under the same condition. This was attributed to the secretion of beta-glucosidase by P. stipitis. During SSF, free extracellular beta-glucosidase activity was 1.30 pNPG U/g with P. stipitis, while saccharification without the yeast was 0.66 pNPG U/g. Published by Elsevier Ltd.

Approach to designing rotating drum bioreactors for solid-state fermentation on the basis of dimensionless design factors

The development of large-scale solid-stale fermentation (SSF) processes is hampered by the lack of simple tools for the design of SSF bioreactors. The use of semifundamental mathematical models to design and operate SSF bioreactors can be complex. In this work, dimensionless design factors are used to predict the effects of scale and of operational variables on the performance of rotating drum bioreactors. The dimensionless design factor (DDF) is a ratio of the rate of heat generation to the rate of heat removal at the time of peak heat production. It can be used to predict maximum temperatures reached within the substrate bed for given operational variables. Alternatively, given the maximum temperature that can be tolerated during the fermentation, it can be used to explore the combinations of operating variables that prevent that temperature from being exceeded. Comparison of the predictions of the DDF approach with literature data for operation of rotating drums suggests that the DDF is a useful tool. The DDF approach was used to explore the consequences of three scale-up strategies on the required air flow rates and maximum temperatures achieved in the substrate bed as the bioreactor size was increased on the basis of geometric similarity. The first of these strategies was to maintain the superficial flow rate of the process air through the drum constant. The second was to maintain the ratio of volumes of air per volume of bioreactor constant. The third strategy was to adjust the air flow rate with increase in scale in such a manner as to maintain constant the maximum temperature attained in the substrate bed during the fermentation. (C) 2000 John Wiley & Sons, Inc.

Biochemical properties of an extracellular beta-D-fructofuranosidase II produced by Aspergillus phoenicis under Solid-Sate Fermentation using soy bran as substrate

The filamentous fungus A. phoenicis produced high levels of beta-D-fructofuranosidase (FFase) when grown for 72 hrs under Solid-State Fermentation (SSF), using soy bran moistened with tap water (1:0.5 w/v) as substrate/carbon source. Two isoforms (I and II) were obtained, and FFase II was purified 18-fold to apparent homogeneity with 14% recovery. The native molecular mass of the glycoprotein (12% of carbohydrate content) was 158.5 kDa with two subunits of 85 kDa estimated by SDS-PAGE. Optima of temperature and pH were 55 degrees C and 4.5. The enzyme was stable for more than 1 hr at 50 degrees C and was also stable in a pH range from 7.0 to 8.0. FFase II retained 80% of activity after storage at 4 degrees C by 200 hrs. Dichroism analysis showed the presence of random and beta-sheet structure. A. phoenicis FFase II was activated by Mn(2+), Mg(2+) and Co(2+), and inhibited by Cu(2+), Hg(2+) and EDTA. The enzyme hydrolyzed sucrose, inulin and raffinose. K(d) and V(max) values were 18 mM and 189 U/mg protein using sucrose as substrate.