Even though the Brazilian ethanol and sugar production system (based on sugarcane industry) have been providing large amounts of bioenergy, the extensive amounts of organic wastes generated cannot be ignored when it comes to sustainability. Using these biomasses to produce biomethane through anaerobic digestion has been proven as a promising way to tackle this issue. This study investigated the biomethane potential of the co-digestion of these biomasses: SF (sugarcane straw : filter cake = 8:2), SFV (sugarcane straw : filter cake : vinasse = 1:4:45), and D (digestate separated from AD of SFV). Three treatments autoclaving (AU), alkaline (AL) treatment using 6% (w/w) NaOH and the combination of these two (AUAL) were then conducted on SF and SFV as pre-treatments; on D as post- treatments. In the biomethane potential tests of untreated material, the highest methane yield was achieved by SFV with 275.28 ± 11 N ml CH4/g VS, followed by SF with 223.25 ± 10 N ml CH4 g-1 VS, substrate D also resulted in a methane potential of 144.69 ± 2 N ml CH4 g-1 VS. As pre-treatments, AL and AUAL both showed increase in methane yield (between 36.0% and 49.1%) and methane production rate. As post-treatments, AU, AL and AUAL showed distinctive results in methane production, with 33.8%, 99.8% and 128.8% increase, respectively. In comparison with pre-treatment, post-treatment showed a better performance in increasing methane production. The following feeding experiments performed in continuous stirred-tank reactors showed that AL treatment led to an average of 248% increase in methane yield. / Sugarcane waste: towards a zero C emission in the Brazilian bioenergy sector

The focus of the current study was on the recovery of carbon from municipal bio-waste streams. Firstly, the relationship between methanogenic pathways and the properties of anaerobic granules was studied using two pilot-scale upflow anaerobic sludge blanket (UASB) reactors with different granule size distribution. UASB1 granules were larger (3-4 mm) with multi-layered internal structure and the archaeal community was dominated by acetoclastic methanogens, while the UASB2 granules were smaller (1-2 mm) without a layered internal structure and the archaeal community was predominated by hydrogenotrophic methanogens. The acetoclastic methanogenic activities of UASB1 (250-437 mL CH4/g VS·d) than UASB2 (150-260 mL CH4/g VS·d), confirming that acetoclastic methanogenesis was more dominant in UASB1. Temperature increase from 20oC to 28oC did not change the microbial community but resulted in increased and stable biogas production for both reactors. There was an increase in chemical oxygen demand (COD) with hydraulic retention time due to increased contact time. The second part of the study focused on anaerobic co-digestion to produce volatile fatty acid (VFA) due to its higher value. The impact of substrate ratio of primary sludge (PS) and external organic waste (OW) and the robustness of the VFA system in the long term were assessed. Lab-scale batch study with different proportions of PS and OW; 0%, 25%, 50%, 75%, 100% of OW in terms of COD and scaled up in a semi-continuous pilot reactor with substrate ratio of 50% OW based on the results of the lab-scale study were performed. There was an increase in VFA production with an increase in OW proportion due to the availability of biodegradable organics. Acetic acid was the most dominant VFA in the batch reactors while in the semi-continuous experiment, caproic acid was dominated (50%). As carbon sources, the VFA-rich liquid attained the highest specific denitrification rate when compared with acetate and methanol. / I kommunala avfallsströmmar finns det en stor potential för resursåtervinning på grund av det höga organiska innehållet vilket kan användas för biobaserade produkter. På grundval av detta så fokuserar denna studie på resursåtervinningen av kol från kommunala avfallsströmmar genom att undersöka nuvarande och nytillkomna tekniker för att få vattenreningssystem att också bli resursåtervinningssystem. Första delen av studien undersöker relationen mellan metanproduktion och karaktäriseringen av anaerobiska granuler med ändamålet att förbättra energiproduktionen genom direkt behandling av kommunalt avloppsvatten. För detta ändamål så användes två UASB (Upflow Anaerobic Sludge Blanket) pilotreaktorer. Reaktorerna kördes med olika stora granuler, olika temperaturinställningar och olika hydrauliska uppehållstider (HRTs). Storlek, mikrobiell struktur, intern mikrostruktur och specifik metanogenaktivitet av de anaerobiska granulerna analyserades. Granulerna i UASB1 var 3-4 mm stora med interna multilager av mikrostrukturer som bestod av acetoklastika-metanogen arkéer. Granulerna i UASB2 var 1- 2 mm stora utan interna multilager och bestod av hydrogenotrofa metanogener. Aktiviteten i granulerna i UASB1 var 250-437 mL CH4 /g VS·d och i UASB2 var det 150-260 mL CH4 /g VS·d, vilket bekräftar att de acetoklastisk-metanogesa var mer effektiva i UASB1 än de hydrogenotrofa i UASB2. Att öka temperaturen från 20 o C till 28 o C under försöket medförde ingen förändring av den mikrobiologiska strukturen, men gav en ökning i biogasproduktion i UASB1 och högre och stabilare biogasproduktionshastighet i UASB2. Ökningen av biogasproduktion berodde på en reduktion i metans löslighet i utflödet och stabilare metanogenes. Ökning i HRT resulterade i större reduktion av organiskt material mätt som kemisk syreförbrukning (COD) och större biogasproduktion på grund av längre kontakttid mellan substrat och mikroorganismer. Den andra delen av studien fokuserar på att utveckla ett tillvägagångssätt att få en anaerob rötning att producera flyktiga fettsyror (VFA) istället för biogas. Studien fokuserar på effekten som kvoten mellan substraten primärslam och externt matavfall (OW) har och hur robust VFA-systemet skulle vara i stor skala på lång sikt. Olika kvoter av primärslam och matavfall testades i labbskala i batchstudier med 0 %, 25 %, 50 %, 75 % och 100 % COD OW. Baserat på resultaten från labbskala så kördes 50% COD OW i ett semi-kontinuerligt pilotförsök. Batch-testerna i labbskala visade att högre % COD OW, gav högre VFA produktion på grund av högre koncentration av organiskt material. Ättiksyra var den mest förekommande VFAn i batch-testerna medan kapronsyra var högst förekommande (50%) i det semi-kontinuerliga försöket. Denitrifikationsförsök visade att VFA-rik vätska från pilotskalareaktorerna gav den högsta specifika denitrifikationshastigheten i jämförelse med acetat och metanol. Resultaten visar att värdefulla kolkällor kan återvinnas från kommunalt avfall genom anaerob behandling av kommunalt avloppsvatten och samfermentering av primärslam och matavfall. / <p>QC 2020-06-15</p>

This research sought to optimize anaerobic co-digestion of microalgae biomass harvested from a wastewater treatment pond facility with locally-available wastes. The goal was to produce high methane yields and stable digestion without the need for supplemental alkalinity addition. A key research question was if algae digestion could be improved via the synergistic effects of co-digestion. Cell disruption to increase digestibility was not pursued due to its relatively high mechanical complexity and high energy use. For the wastewater treatment ponds studied, the most practical co-substrates identified were municipal wastewater sludge and food waste (sorted organic municipal waste). Although wastewater sludge does not have a particularly high carbon:nitrogen (C:N) ratio, it readily and stably digests and is available in large quantities at wastewater treatment plants. This research investigated the methane productivity of algae co-digestion with municipal wastewater sludge and food waste in semi-continuous bench-scale anaerobic digesters at 37.5˚C. Digesters fed pure algae biomass loaded at a rate of 4 g Volatile Solids (VS)/L-day with a 20-day residence time exhibited stable digestion and yielded an average of 0.23 L CH4/g VS Introduced. For digesters that contained algae biomass in the feed, the greatest methane yield of 0.40 mL CH4/g VSin was observed in a digester containing 50% algae co-digested with both sorted organic municipal waste (40%), and municipal wastewater sludge (10%) at a loading rate of 2 g VS/L-day with a 20-day residence time. While adding co-substrates increased yields in all digesters, prevention of ammonia toxicity did not appear to be the mechanism. Instead, the co-substrates simply increased the concentration of readily-digestible organic carbon, leading to increased methane yields and productivities. For algae biomass, total ammonia nitrogen concentrations of 3370 mg/L did not appear to inhibit methane yield. Digesters with the same feed contents and residence time loaded at 2 and 4 g VS/L-d had similar yields but total ammonia nitrogen concentrations of 1740 and 3370 mg/L respectively. From the data from these laboratory studies, descriptive models were developed for ammonia nitrogen, alkalinity, volatile fatty acids, yield, biogas quality, and volatile solids destruction. The variables from the descriptive models with p-values above 0.05 were then used to create a compact model.

No description available.

No description available.

Le traitement biologique des eaux usées urbaines et industrielles reste une activité ayant un impact négatif sur l’environnement et sur le changement climatique par l’émission des gaz à effet de serre (GES), notamment le CO2. Les changements innovants au niveau des procédés de traitement des eaux usées par l’intégration des flocs de microalgues-bactéries ont abouti à des procédés multitrophiques sans apport d’O2 et sans dégagement du CO2. Il s'agit d'une étude de faisabilité de ces flocs-MaB pour la photobioremédiation des polluants (organiques et minéraux) et pour la production de biomasse valorisable en bioénergie dans le cadre de l'économie circulaire. En présence de la lumière, les flocs-MaB ont été intégrés dans des photobioréacteurs à biomasse fixe afin d'assurer un traitement durable des eaux usées grâce aux échanges symbiotiques entre les micro-oragnismes en terme de nutriments et de gaz. L'encapsulation des flocs-MaB dans des billes de PVA-alginate a montré l'effet des conditions physico-chimiques et hydrodynamiques sur l'élimination des polluants et l'évolution multicellulaire des flocs au sein des réacteurs à multi-échelles. Par ailleurs, la biomasse multitrophique immobilisée sur des supports biodégradables d'olive (OPP) et sur des disques en PVC a assuré une meilleure performance des bioréacteurs à lit fluidisé et à disques rotatifs, respectivement, pour la bioremédiation des eaux usées. Les propriétés des supports (porosité, rugosité et structure) et les comportements hydrodynamiques ont été contrôlés pour favoriser l'attachement des biofilms multitrophiques. Le développement de biofilm montre l'effet des interactions multitrophiques entre les microalgues et les bactéries sur l'élimination des composés organiques (DCO) et nutriments (ammonium et phosphore). La biomasse des flocs-MaB a été récupérée et réutilisée pour le traitement du digestat liquide à l'issu du digesteur et pour améliorer la production de biométhane par une co-digestion anaérobie. Ce procédé multitrophique et intégré permet d'obtenir Zéro déchet à la sortie du processus / The biological treatment of urban and industrial wastewaters represents a process with a negative impact on the environment and on climate change through the emission of greenhouse gases (GHG), particularly CO2. In the presence of light, microalgae-bacteria flocs (MaB-flocs) have been integrated into photobioreactors with fixed biomass to ensure a sustainable wastewater treatment without O2 supply and CO2 release. The entrapment of flocs in PVA-alginate beads has shown the effect of physicochemical and hydrodynamic conditions on the elimination of pollutants and the multicellularity evolution within multi-scale bioreactors. In addition, the immobilization of biomass on biodegradable olive carriers and on PVC disks provided a better performance of fluidized bed and rotating discs bioreactors, respectively, for the bioremediation of wastewater. The properties of the supports (porosity, roughness, and structure) and the hydrodynamic behaviors have favored the attachment of multitrophic biofilms. Biofilm development shows the effect of multitrophic interactions between microalgae and bacteria on the organic compounds (COD) and nutrients (ammonium and phosphorus) removals. The MaB-flocs biomass was recovered and reused for the treatment of the digestate and to improve the production of biomethane by anaerobic co-digestion. This integrated multitrophic technology makes it possible to obtain zero wastes at the end of the process

Because of the increasing trends in energy consumption and increased environmental awareness, greater focus has been placed on improvement and development of renewable energy sources. An already proven and accepted method is biogas production from anaerobic digestion at municipal wastewater treatment plants. In the waste water treatment process solid material and dissolved pollutants are separated from the water, forming a sludge. The sludge is separated from the process and stabilized during anaerobic digestion or aerobic aeration. Most often, mesophilic anaerobic digestion is used. Because of degradation by microorganisms, biogas with a high content of methane is formed during the digestion. To optimize the process different studies with co-digestion with sludge and other substrate have been made. It has been showed, in earlier research studies, that co-digestion with microalgae and sewage sludge results in a synergistic effect with increased biogas production. As the microalgae are microorganisms which use photosynthesis they contain stored energy from sun light. The stored energy will be available when the microalgae are digested in mesophilic conditions. In contrast to other biomass suitable for co-digestion microalgae have the advantage of being able to grow in waste water and reduce the pollutants in the water phase. Cultivation of microalgae will therefore not compete with the cultivation of food production and at the same time has the possibility to decrease the electricity- and heat consumption at the wastewater treatment plants. The aim of this study was to investigate how a possible synergetic effect between microalgae and sewage sludge effects the biogas production and the process stability. The microalgae was cultivated in municipal waste water from the WWTP in Umeå (Sweden) and the sludge was collected from the WWTP in Västerås (Sweden). The fermenters used was of the type DOLLY© and the active volume was 5 dm3. The temperature in the fermenters was kept at 37 °C and the study was divided into two periods. During the first period the hydraulic retention time was 15 days and the organic loading rate 2.4 g VS dm-3 d-1. During the second period the hydraulicretention time was kept at 10 days and the organic loading rate was 3.5 g VS dm-3 d-1. The result showed an increase with 54.6 % in methane production per reduced VS in the fermenter with co-digestion compared to the fermenter where only sludge was digested. Period one showed the highest increase. The result also showed a good process stability for both fermenters during the whole experiment. This study shows that there are reasons for continued investigations about co-digestion with microalgae and sewage sludge for an increased biogas production. / På grund av ökande el- och värmeförbrukning och ökat miljöengagemang har större fokus lagts på förbättring och utveckling av förnyelsebara källor för el- och värmeproduktion. En redan beprövad och accepterad metod för framställning av förnyelsebar energi är från biogasproduktion vid kommunala reningsverk. Vid rening av avloppsvatten avskiljs fasta partiklar och lösta föroreningar och bildar ett slam som separeras från vattnet. Slammet kan sedan stabiliseras anaerobt genom rötning eller aerobt genom luftning. En ofta använd metod vid konventionella reningsverk är mesofil anaerob rötning. Vid rötningen bryts material ner av mikroorganismer och genererar biogas som framförallt innehåller metan och koldioxid. För att optimera en sådan process och därmed kunna utvinna mer gas har det tidigare undersökts hur samrötning med olika material påverkar biogasproduktionen. Det har visat sig i forskningsförsök att samrötning med mikroalger och orötat blandslam ger en synergieffekt och mer biogas produceras. Mikroalgerna innehåller lagrad energi från solljus, då de är fotosyntesiserande organismer. Den lagrade energin har visat sig bli tillgänglig vid mesofil anaerob nedbrytning. Till skillnad från annan biomassa som undersökts för samrötning kan mikroalgerna odlas på avloppsreningsverken och fungera som en del av reningsprocessen då mikroalgerna tar upp näringsämnen ur vattnet de växer i. På det sättet undviks konkurrens om odlingsmark för livsmedel och så blir reningsprocessen på avloppsreningsverken mer el- och värmeeffektiv. Syftet med studien var att undersöka om eventuell synergieffekt mellan mikroalgerna och slammet påverkar biogasproduktionen och processtabiliteten vid mesofil anaerob rötning. Mikroalgerna som användes var odlade på mekaniskt renat spillvatten från Umeås reningsverk och slammet som användes hämtades ifrån Västerås reningsverk. Rötkamrarna som användes var av modellen DOLLY© med en aktiv volym på 5 dm3. Temperaturen i rötkamrarna hölls kring 37°C och studien var uppdelad i två perioder. Under period ett var den hydrauliska uppehållstiden 15 dygn och den organiska belastningen 2,4 g VS dm-3 d-1, medan period två hade en hydraulisk uppehållstid på 10 dygn och en organisk belastning på 3,5 g VS dm-3 d-1. Resultaten visade att metangasproduktionen per tillförd mängd organiskt material var lägre vid samrötning jämfört med rötning av enbart slam. Metangasproduktionen per reducerad mängd organiskt material ökade med upp till 54,6 % vid samrötningen jämfört med rötning av enbart slam. Period ett gav upphov till den största ökningen. Processen hölls stabil även vid inblandning av mikroalger, under både period ett och två. Studien visar att det finns ett underlag för fortsatta studier kring samrötning av mikroalger och slam för en ökad biogasproduktion.

M. Tech. (Civil Engineering, Faculty of Engineering and Technology), Vaal University of Technolog / Textile industry effluents are carcinogenic and highly recalcitrant hence difficult to degrade especially through biological methods. Abattoir effluents are classified under high-strength wastewaters because of their characteristic high organic load hence highly biodegradable. Anaerobic co-digestion is the concept of degrading two effluent streams with complementary characteristics in order to improve the substrate removal rate. The feasibility of co-digesting abattoir and textile wastewater in a UASB reactor was evaluated at mesophilic and ambient temperature conditions. Preliminary experiments were conducted in 500 ml batch reactors to evaluate the optimum abattoir to textile synthetic wastewater ratio. The effect of COD, TVFA, alkalinity and pH on biogas yield was examined at both ambient and mesophilic temperatures. Anaerobic co-digestion of abattoir to textile wastewater in the ratio determined in the batch process was carried out in a 3 L UASB reactor by a continuous process. The continuous biodegradation process was executed at three different HRTs (22, 18 and 14 hrs) over a 60 day operation period. UASB reactor efficiency was achieved at organic loads ranging from 3.0 – 10.8 gCOD L-1 day-1. Continuous mode experiments were carried out at influent flow rates which corresponded to HRTs ranging between 1 to 8 days in order to evaluate the steady state operating parameters for the co-digestion process. The abattoir to textile effluent ratio was found to be 60:40 respectively. The COD, TVFA, alkalinity and pH and biogas yield followed a similar pattern over time at both mesophilic and ambient temperature conditions. Experimental data adequately fit the Grau first order kinetic model and average COD removal efficiencies of 85% and BOD5 of around 96% were achieved. The average biogas yield remained essentially constant, around 0.19 L/g CODremoved. The co-digested mixture was found to be biodegradable judging from the BOD:COD ratio of 0.53. TCOD removal efficiency decreased from 93% to 16% as HRT decreased from 8 days to 1 day. The kinetics of a UASB reactor co-digesting the mixture of synthetic abattoir and textile wastewater was evaluated in this study using Grau second order multicomponent substrate removal kinetic model. The Grau second order kinetic model, whose kinetic coefficient (ks) was 0.389, was found to be suitable for predicting the performance of a lab-scale UASB reactor.

A indústria de laticínios no Brasil gerou no 2014 em torno de 88,5 bilhões de litros de efluente, o resíduo gorduroso (RG) separado no tratamento deste efluente, atualmente carece de tratamento. A digestão anaeróbia (DA) é uma opção de tratamento a partir da qual é possível, entre outras coisas, obter biogás, fonte renovável de energia, que representa uma importante alternativa para compor a matriz energética do país. No entanto, resíduos lipídicos, além de gerar lodos de difícil manejo, descompõem-se em ácidos graxos de cadeia longa (AGCL) que inibem os microrganismos metanogênicos. Como estratégia para tratar efetivamente este resíduo, avaliou se um sistema de co-digestão anaeróbia empregando RG advindo da caixa de gordura de um laticínio, e, bagaço de cana de açúcar (BCA) pré-tratado em condições sub e supercríticas de CO2: (i) 40°C / 70 bar (ii) 60°C / 200 bar e (iii) 80°C / 200 bar, com e sem adição de NaOH, respectivamente. Dos pré-tratamentos avaliados, destaca-se o pré-tratamento com CO2 a 60°C e 200bar pelo qual foi possível remover 8,07% de lignina. A produção metanogênica advinda da digestão anaeróbia de bagaço de cana de açúcar foi aumentada em todos os casos nos quais o material foi pré-tratado com CO2 sub e supercrítico, com exceção do caso no qual se utilizou elevada temperatura e NaOH como modificador de polaridade. Os resíduos advindos da caixa de gordura apresentaram elevado potencial metanogênico na faixa de concentração de substrato estudada, sem que nenhuma inibição fosse verificada. A co-digestão de resíduos gordurosos e bagaço de cana, pré-tratados ou não, não apresentou vantagem com relação à mono-digestão dos materiais. / The dairy industry in Brazil generated in 2014 around 88.5 billion litters of effluent, the fatty residue, separated in the treatment of this effluent, currently lacks treatment. Anaerobic digestion is a treatment option from which it is possible, among other things, to obtain biogas, a renewable source of energy, which represents an important alternative to fix the country\'s energy matrix. However, lipid residues form sludges that are difficult to manage and decompose into long chain fatty acids (LCFAs) that are inhibitory to methanogenic microorganisms. As a strategy to effectively treat this residue, we evaluated an anaerobic co-digestion system employing fatty residues from a fat box of a dairy plant, and sugarcane bagasse pre-treated under sub and supercritical CO2 conditions: (i) 40°C / 70 bar (ii) 60°C / 200 bar and (iii) 80°C / 200 bar, with and without addition of NaOH respectively. Of this pre-treatments, stood out the one with CO2 at 60°C and 200 bar by which was achieved the removal of 8.07% of lignin. The methanogenic production from the anaerobic digestion of sugarcane bagasse was increased in all cases in which the material was pre-treated with sub and supercritical CO2, with the exception to the cases in which high temperatures and NaOH were combined. The residues from the dairy fat box showed high methanogenic potential in the concentration range evaluated and no inhibition was verified. The co-digestion of the greasy residues and the sugarcane bagasse with and without pre-treatment, did not present advantage in compare to the mono-digestion of the materials.

A presente pesquisa teve como proposta avaliar o reator anaeróbio, operado de forma descontínua ou descontínua alimentada, contendo biomassa imobilizada em suporte inerte e com recirculação da fase líquida (AnSBBR) aplicado à produção de biohidrogênio a partir da codigestão de glicerina (efluente da produção de biodiesel) e soro de leite (efluente da produção de laticínios). A estabilidade, os índices de desempenho (referentes à produtividade e rendimento molar do hidrogênio) e o fator de conversão (entre biogás produzido e matéria orgânica consumida) foram analisados em função da composição afluente (porcentagem de cada substrato alimentado ao sistema), da variação da carga orgânica, do tempo de enchimento e da temperatura (20, 25, 30 e 35ºC). Os ensaios foram realizados em diferentes proporções dos substratos utilizando-se variadas cargas orgânicas volumétricas (10,3; 17,1 e 24,0 gDQO.L-1.d-1), as quais foram modificadas em função: (i) da concentração afluente (3, 5 e 7 gDQO.L-1) e (ii) do tempo de ciclo (4, 3 e 2 h, ou seja, 6, 8 e 12 ciclos diários). Também foram realizados ensaios para a produção de biometano a partir da codigestão proposta nesta pesquisa (com COAV de 7,6 gDQO.L-1.d-1) em diferentes proporções de mistura. Para a produção de biometano, a condição com 75% de soro e 25% de glicerina (base DQO) obteve os melhores resultados: produtividade molar de 101,8 molCH4.m-3.d-1 e rendimento por carga aplicada de 13,3 molCH4.kgDQO-1; o que representa um aumento de produtividade de cerca de 9% e 30% quando comparado com a digestão anaeróbia de soro e glicerina puros, respectivamente. A produção de metano no melhor ensaio aconteceu predominantemente pela rota hidrogenotrófica. Para a produção de biohidrogênio, a maior produtividade e rendimento do reator foram obtidas no ensaio operado com razão de mistura de 75% soro e 25% glicerina, com 7 gDQO.L-1 de concentração afluente, tempo de ciclo de 3 h e tempo de enchimento de 1,5 h (modo batelada alimentada - COAV de 23,9 kgDQO.m-3.d-1), a 30°C: foi obtida uma produtividade molar de 129,0 molH2.m-3.d-1 e rendimento de 5,4 molH2.kgDQO-1. Esses resultados representam um aumento de produtividade de 145% em relação a mono-digestão do soro na condição inicial, o que indica o benefício significativo da adição de glicerina ao afluente, provavelmente devido à sua capacidade tamponante, e a otimização das condições operacionais. A adição de glicerina e o aumento da COAV balancearam as rotas de produção de hidrogênio, sendo produzido de forma mais equilibrada pelas vias do ácido acético, butírico e valérico. A caracterização do consórcio microbiano desse ensaio indicou que a comunidade microbiana presente no AnSBBR foi dominada por Ethanoligenens e Megasphaera. / The current research evaluated an anaerobic reactor, operated in batch or fed-batch mode, containing immobilized biomass in inert support and with recirculation of the liquid phase (AnSBBR), applied to the production of biohydrogen co-digesting glycerin (effluent from biodiesel production process) and whey (effluent from dairy industry). Stability, performance (regarding productivity and molar hydrogen yield) and conversion factor (between biogas produced and organic matter consumed) were analyzed according to the percentage of each substrate fed to the system, organic loading rate, filling time and temperature (20, 25, 30 and 35ºC). Assays were carried out using different substrates proportions and organic loading rates (10.3; 17.1 and 24.0 gCOD.L-1.d-1), which have been modified in function of: (i) influent concentration (3, 5 and 7 gCOD.L-1) and (ii) cycle length (4, 3 and 2 h, i.e. 6, 8 and 12 cycles daily). Assays were also carried out aiming for biomethane production using the proposed co-digestion (with AVOL of 7.6 gDQO.L-1.d-1) with different proportions of substrate mixture. For biomethane production, the assay conducted with 75% whey and 25% glycerin (COD basis) obtained the best results: molar productivity of 101.8 molCH4.m-3.d-1 and yield per applied load of 13.3 molCH4. kgCOD-1; which is an increase in productivity of about 9% and 30% when compared with the anaerobic mono-digestion of whey and glycerin, respectively. Methane production in this assay came mainly from the hydrogenotrophic route. For biohydrogen production, the highest productivity and yield were achieved in the assay operated with 75% whey and 25% glycerin, with 7 gCOD.L-1 of influent concentration, 3 h of cycle time and filling time of 1.5 h (fed batch mode - AVOL of 23.9 kgCOD.m-3.d-1), at 30°C: a molar productivity of 129.0 molH2.m-3.d-1 and yield of 5.4 molH2.kgCOD-1 were obtained. These results represent a productivity increase of 145% in relation to whey mono-digestion at its initial condition, which indicates the significant benefit of glycerin addition to the influent, probably due to its buffering capacity, and improvement of operational conditions. The addition of glycerin and the increase in AVOL balanced the hydrogen production routes, since hydrogen was produced similarly by the acetic, butyric and valeric acid routes. The characterization of the microbial consortium of this assay indicated that the microbial community present in the AnSBBR was dominated by Ethanoligenens and Megasphaera.