Biogas from microalgae: an overview emphasizing pretreatment methods and their energy return on investment (EROI).

Studies have reported enhancements in methane yield from pretreatment methods that benefit the anaerobic digestion (AD) of microalgae. However, energy return on investment (EROI), i.e., methane production enhancement achieved over energy input, may be unfavorable. Aiming to quantify EROI of AD microalgae pretreatment, about 180 experiments applied to 30 microalgae biomasses were compiled through an extensive literature survey, classified into 4 pretreatments (physical, enzymatic, chemical, and hybrid), and analyzed. Most of these pretreatments enhanced methane yield, especially the enzymatic alternative. EROI was evaluated for the most efficient pretreatments. Only in one thermal pretreatment the energy resulting from the increase in methane production exceeded the energy demanded by the biomass pretreatment (EROI 6.8) and other two thermal pretreatments presented EROI 1. The other pretreatments presented EROI < 1, concluding that none of the evaluated methods was energy-efficient. Feasibility of pretreatment requires advancements in low energy-demanding strategies and outstanding biomass densification.

Reduction of scum accumulation through the addition of low-cost enzymatic extract in the feeding of high-rate anaerobic reactor.

This work evaluates the reduction of scum accumulation on the top surface of upflow anaerobic sludge blanket (UASB) reactors by the addition of hydrolytic enzymes in their feed. For over 1 year, two UASB reactors of 1.4 L were maintained at 30 °C and continuously fed with synthetic domestic wastewater (containing 150 mg/L of soybean oil) under a hydraulic retention time of 10 h. The Control reactor was only fed with synthetic wastewater. Beginning at the 226th day of operation, low-cost hydrolytic enzymes (obtained by solid-state fermentation of Aspergillus terreus, a fungus isolated from a primary sewage sludge) were added into the feed of the other reactor (Test) for a lipase activity of 24 U/L, considerably reducing the formation of scum. In the Test reactor, the scum showed oil and grease (O&G) concentration between 0.8 and 1.3 g/L and an accumulation rate of 20 to 27 mg O&G/d. In the Control reactor, the scum had values twice as high (1.5-2.5 g/L and 34-51 mg O&G/d, respectively) and there were more operational problems. During the entire period of operation, both reactors presented high chemical oxygen demand removal (>80%), with no loss of effluent quality due to the addition of the enzymes.

Study of the recovery of phosphorus from struvite precipitation in supernatant line from anaerobic digesters of sludge.

The goal of this work was to study the effective recovery of phosphorus from the supernatant of anaerobic digestion of sewage sludge by precipitation as struvite. The formation of struvite is envisioned as a promising process for nutrient removal and subsequent recovery, thus providing a strong incentive for its implementation, since the sewage is a renewable source of phosphorus. Struvite precipitation was obtained by controlled addition of Mg(OH)2 or MgCl2. We evaluated the removal of ammonia and phosphate under equimolar conditions of magnesium and magnesium stoichiometric excess of 100 to 200% relative to the limiting reagent, under a stirring speed of 300 rpm at pH 8, 9 and 10. The best condition was MgCl2 in 1:1 molar ratio to phosphate, considering the stoichiometric ratio [PO4(3-)]:[NH4(+)] of 0.13 (presented by raw sample). The results show the best cost-benefit ratio, removal of phosphate of 90.6% and ammonium removal of 29%, resulting in 23 mg l(-1) PO4(3-) and 265 mg l(-1) NH4(+) concentration in effluent.

Evaluation of pH, alkalinity and temperature during air stripping process for ammonia removal from landfill leachate.

The objective of this research was to evaluate the air stripping technology for the removal of ammonia from landfill leachates. In this process, pH, temperature, airflow rate and operation time were investigated. Furthermore, the relationship between the leachate alkalinity and the ammonia removal efficiency during the process was studied. The leachate used in the tests was generated in the Gramacho Municipal Solid Waste Landfill (Rio de Janeiro State, Brazil). The best results were obtained with a temperature of 60(o)C, and they were independent of the pH value for 7 h of operation (the ammonia nitrogen removal was greater than 95%). A strong influence of the leachate alkalinity on the ammonia nitrogen removal was observed; as the alkalinity decreased, the ammonia concentration also decreased because of prior CO2 removal, which increased the pH and consequently favored the NH3 stripping. The air flow rate, in the values evaluated (73, 96 and 120 L air.h(-1).L(-1) of leachate), did not influence the results.

Densification of Synechococcus subsalsus biomass by chitosan coagulation for biogas production.

This study evaluated the coagulation/flocculation process using chitosan as a natural coagulant to concentrate suspensions of the cyanobacterium Synechococcus subsalsus and enable biogas production from concentrated biomass. The chitosan performance was tested and compared with the inorganic ferric chloride (FeCl3) coagulant. Using the liquid fraction of the coagulation/flocculation process in subsequent biomass cultivations proved viable, with similar growths in culture media with up to 80% of the liquid fraction. At pH 6 and 400 mg/L FeCl3, the biomass concentrated almost seven times, increasing the total suspended solids (TSS) of the suspension from 0.4-0.6 g/L to 2.6-4.0 g/L. With 80 mg/L chitosan and pH 7, the TSS concentration attained values in the range of 7.0-9.7 g/L, an increase of more than 30 times, clearly showing that chitosan has a much higher capacity for biomass concentration at a lower concentration. A ratio of 0.3 g chitosan/g dry mass of the biomass was established to reach the maximum densification. The production of methane from chitosan-densified biomass proved to be feasible. Chitosan-densified biomass showed a two-phase cumulative methane production when digested, with slower methane production and 23% lower methane yield after 30 days of digestion (207 NmL CH4/g CODi) compared to the biomass from cultivation (non-densified, 270 NmL CH4/g CODi). However, optimizing the digestion conditions of the densified biomass should increase the methane yield and reduce process time.

Sustainability of the anaerobic digestion of oil refinery secondary sludge.

Among the waste generated at oil refineries, secondary sludge from biological wastewater treatment processes (activated sludge systems) stands out. This paper aimed to assess the use of anaerobic digestion (AD) to treat sludge by SWOT (Strength, Weakness, Opportunity, and Threat) analysis, ranking the different factors based on sustainability criteria. Additionally, the SWOT factors were matched (TOWS matrix) to help interpret the results. AD was found to be compatible with sustainability. The results demonstrated that the strength of AD (reduced organic load) compensates for its weaknesses (need for operational control and initial implementation costs), thereby avoiding the threat (sludge composition) and making the most of the opportunity (lower disposal cost). AD and co-digestion (added with food waste) used to treat oil refinery sludge showed that around 60% of the factors analyzed were confirmed experimentally. It was concluded that AD should be considered in the sustainable treatment of oil refinery waste activated sludge, especially when mixed with other readily biodegradable wastes.

Anaerobic digestion (AD) is a potential treatment for secondary sludge from refineries.AD is compatible with sustainability.Anaerobic co-digestion of refinery sludge contributed positively to sustainable treatment.The strength (reduced organic load) of AD counteract its weaknesses (operational control and implementation costs).The threat of AD (sludge composition) should be avoided and the opportunity (low disposal cost) leveraged.

Investigation of carbon steel corrosion by oilfield nitrate- and sulfate-reducing prokaryotes consortia in a hypersaline environment.

Microbiologically influenced corrosion (MIC) behavior of the AISI 1020 carbon steel caused by consortia of nitrate-reducing prokaryotes (NRP) and sulfate-reducing prokaryotes (SRP) was investigated separately in hypersaline seawater conditions. Microbiological analysis, surface images, characterization of corrosion products, weight loss, and electrochemical measurements were employed to monitor the corrosion process for 10 days at 40 °C. Compared to abiotic corrosion (control), the extent of corrosion was more aggravated in the conditions with microbial consortia. It corroborates the critical role of microbial activity in corrosion processes in natural and industrial environments since microorganisms are widely spread. Corrosion rates obtained from Tafel extrapolation were statically equal for both microbial consortia (0.093 ± 0.009 mm.y-1); however, the maximum pit depth on the steel surface subjected to NRP-MIC was about 25% deeper (48.5 µm) than that caused by SRP-MIC (32.6 µm). In contrast, SRP activity almost doubled the number of pits on the steel surface (2.7 × 104 ± 4.1 × 103 pits.m-2), resulting in more weight loss than NRP activity. In addition, SRP cells formed nanowires to support direct electron uptake from steel oxidation. This research contributes to the understanding of steel corrosion mechanisms in hypersaline environments with the prevalence of NRP or SRP, as oil reservoirs undergo nitrate injection treatments.

Anaerobic co-digestion of oil refinery waste activated sludge and food waste.

The technology of anaerobic co-digestion to treat the excess biological sludge discharged from activated sludge systems in oil refineries was evaluated in bench scale experiments. Mixing food waste rich in fruits and vegetables with this sludge increased the reduction of volatile solids and biogas yield. An experimental design indicated that the best co-digestion condition was the use of waste activated sludge without previous dewatering (3.5% total solids) and food waste in an 80:20 ratio (% v/v), without the addition of inoculum. After 45 days at 35 °C, this condition resulted in volatile solid (VS) removal of 52% and biogas yield of 80.7 mL biogas/g VSadded, against only 19% and 38.5 mL biogas/g VSadded in mono-digestion of sludge alone. Anaerobic co-digestion demonstrates promising results and the potential for a simple and effective treatment method for excess biological sludge generated at refineries.

Co-digestion of sewage sludge with crude or pretreated glycerol to increase biogas production.

Anaerobic co-digestion of sewage sludge and glycerol from the biodiesel industry was evaluated in three experimental stages. In the first step, the addition of higher proportions of crude glycerol (5-20% v/v) to the sludge was evaluated, and the results showed a marked decrease in pH and inhibition of methane production. In the second step, co-digestion of sludge with either a lower proportion (1% v/v) of crude glycerol or glycerol pretreated to remove salinity resulted in volatile acid accumulation and low methane production. The accumulation of volatile acids due to the rapid degradation of glycerol in the mixture was more detrimental to methanogenesis than the salinity of the crude glycerol. In the third step, much lower amounts of crude glycerol were added to the sludge (0.3, 0.5, 0.7% v/v), resulting in buffering of the reaction medium and higher methane production than in the control (pure sludge). The best condition for co-digestion was with the addition of 0.5% (v/v) crude glycerol to the sewage sludge, which equals 0.6 g glycerol/g volatile solids applied. Under this condition, the specific methane production (mL CH4/g volatile solids applied) was 1.7 times higher than in the control.

Bioconversion of Sugarcane Vinasse into High-Added Value Products and Energy.

Vinasse, a residue from bioethanol production containing high organic matter concentration, was used as substrate in submerged fermentation of Pseudomonas aeruginosa PA1 for biosurfactant production. About 2.7 g/L of rhamnolipids was obtained, with surface tension of 29.2 mN/m and critical micelle concentration of 80.3 mg/L. After separation of rhamnolipid and biomass, residual fermentation media were submitted to anaerobic biodegradation in mesophilic conditions. The residual medium derived from fermentation with vinasse diluted to 1 : 1, without addition of nitrogen, C : N 21, and for 168 h, led to 63.2% chemical oxygen demand (COD) removal and 97.6 mL CH4/g CODremoved. Compared to results obtained with fresh vinasse (73.7% COD removal and 112.4 mL CH4/g CODremoved), it could be concluded that both processes can be integrated in order to add value to the residue and obtain energy, reducing production costs and at the same time environmental impacts related to vinasse disposal.

Pré-tratamento físico-químico e enzimático para efluente de abatedouro / Physico-chemical and enzymatic pre-treatment for wastewater from slaughterhouse

RESUMO O efluente gerado em um abatedouro de aves, contendo gordura (quantificada pela análise de Óleos e Graxas - O&G) na concentração de 1.100 mg.L-1, foi submetido a dois pré-tratamentos para redução da concentração de material orgânico particulado: um tratamento físico-químico convencional (coagulação/floculação com cloreto férrico) ou um tratamento enzimático alternativo (hidrólise enzimática), aplicados isoladamente antes do processo biológico para remoção de material orgânico dissolvido. A hidrólise foi realizada com 0,5% (m/v) de um preparado enzimático sólido (PES - contendo oito unidades de atividade lipásica por grama) produzido pelo fungo Penicillium sp. por 8 h a 30ºC. Diferentes condições foram avaliadas na coagulação/floculação, sendo selecionada a que apresentou melhor remoção de demanda química de oxigênio (DQO) total para alimentação de biorreatores aeróbios e anaeróbios de bancada: pH = 5,0 e 400 mg de FeCl3.6H2O.L-1. Melhores resultados foram alcançados ao se utilizar o pré-tratamento físico-químico, com remoções médias de DQO de 91% nos tratamentos aeróbio e anaeróbio.

ABSTRACT The effluent generated in a poultry slaughterhouse, containing fat (quantified by oil and grease - O&G analysis) at a concentration of 1,100 mg.L-1, was subjected to two pre-treatments to reduce the particulate organic matter concentration: a conventional physicochemical treatment (coagulation/flocculation with ferric chloride) or an alternative enzymatic treatment (enzymatic hydrolysis), applied alone prior to the biological process for removing dissolved organic material. Hydrolysis was performed with 0.5% (m/v) of a solid enzymatic preparation (SEP - containing 8 lipase activity units per gram) produced by the fungus Penicillium sp. for 8 h at 30ºC. Different conditions were evaluated in the coagulation/flocculation, and the one with the best total COD removal for feeding bench top aerobic and anaerobic bioreactors was selected: pH = 5.0 and 400 mg FeCl3.6H2O.L-1. Better results were achieved when using the physicochemical pre-treatment with average COD removals of 91% in aerobic and anaerobic treatments.

Production of CO2 in crude oil bioremediation in clay soil

The aim of the present work was to evaluate the biodegradation of petroleum hydrocarbons in clay soil a 45-days experiment. The experiment was conducted using an aerobic fixed bed reactor, containing 300g of contaminated soil at room temperature with an air rate of 6 L/h. The growth medium was supplemented with 2.5 percent (w/w) (NH4)2SO4 and 0.035 percent (w/w) KH2PO4. Biodegradation of the crude oil in the contaminated clay soil was monitored by measuring CO2 production and removal of organic matter (OM), oil and grease (OandG), and total petroleum hydrocarbons (TPH), measured before and after the 45-days experiment, together with total heterotrophic and hydrocarbon-degrading bacterial count. The best removals of OM (50 percent), OandG (37 percent) and TPH (45 percent) were obtained in the bioreactors in which the highest CO2 production was achieved.

Inibição de lodo biológico anaeróbio por constituintes de efluente de laboratório de controle de poluição / Inhibition of anaerobic biological sludge by effluent constituents of pollution control laboratory

Nos laboratórios de controle de poluição, análises de rotina para a caracterização de efluentes e monitoramento dos reatores de tratamento empregam soluções concentradas de H2SO4, contendo metais pesados como cromo, prata e mercúrio, e compostos orgânicos como fenol. Embora os microrganismos metanogênicos possam tolerar a presença de algumas substâncias ou elementos tóxicos presentes em efluentes, os mesmos podem apresentar sensibilidade a determinados compostos químicos. O trabalho teve como objetivo caracterizar o efluente do Laboratório de Tecnologia Ambiental da Escola de Química da Universidade Federal do Rio de Janeiro (LTA/UFRJ) e determinar quais constituintes desse efluente seriam inibitórios para microrganismos anaeróbios no tratamento do esgoto gerado no campus. O efluente apresenta uma produção média semanal de 43,4 L, com pH 0,7, 1350 mg/L de DQO, 33500 mg SO4(2-)/L; 28,2 mg Hg/L; 82,1 mg Cr total/L; 30,8 mg Cu/L; 57,4 mg Fe total/L; 16,2 mg Al/L e 2,44 g Na/L. Os parâmetros analisados apresentaram elevada variabilidade ao longo do estudo, em função das análises e pesquisas realizadas naquele período. No planejamento experimental realizado, observou-se que os principais efeitos sobre o percentual de inibição da atividade metanogênica específica (AME) foram os elementos sódio, cromo, fenol e sulfato e as interações sulfato-mercúrio e sulfato-sódio. Os efeitos dos demais elementos (cobre, mercúrio, alumínio e ferro), analisados separadamente e em interações, não foram significativos para um nível de confiança de 95 por cento na distribuição t de Student. Os resultados apontam para a necessidade de um tratamento específico para os efluentes de laboratório, já que as Universidades devem ser exemplos de combate à poluição e de incentivo ao controle ambiental.