A rotational drum fermentation system with water flushing for enhancing hydrolysis and acidification of solid organic wastes

In this work, fresh soybean meal was used as the substrate for both batch and continuous experiments in a rotational drum fermentation (RDF) system to characterize the acidogenic process of solid organic waste degradation at high unionized volatile acid (U-VA) level and evaluate the effect of water flushing on the acidogenic performance. The experiments were conducted under mesophilic condition with a reaction time of 20 days. The results of the batch experiment showed that U-VA had a growing adverse effect on the volatile acid (VA) production and hydrolysis of the substrate as the initially added U-VA concentration increased (0, 5, 15, 25 g/L). VA formation deteriorated drastically when the initial U-VA concentration exceeded 5 g/L. VS degradation ratios decreased from 43.8% to 7.3%, and the hydrolysis rate constants varied between 28.8 and 3.8 x 10(-3)/d in response to the initial U-VA concentration. In the continuous experiment, two cascade process configurations (CP1 and CP2) without and with VA removal by water flushing, respectively, were developed. The results showed that the hydrolysis rate constants and VS degradation ratios were 13.1 x 10(-3)/d and 23%, respectively, in CP2, while only 9.1 x 10(-3)/d and 16.7% in CP2. Compared to CP1, the VA spectrum varied little in CP2 with water flushing. It suggested that the higher U-VA level had a significant inhibition on the acidogenic process of solid organic waste degradation, and the VA removal by water flushing improved the acidogenic performance.     

Enhancement of hydrolysis and acidification of solid organic waste by a rotational drum fermentation system with methanogenic leachate recirculation

A cascade process of a rotational drum fermentation system with leachate recirculation from a methanogenic to the acidogenic reactor was constructed to enhance the hydrolysis and acidification of solid organic waste. Using fresh soybean meal as substrates, two process configurations, Cascade process 1 and 2, without and with leachate recirculation, respectively were employed to perform the experimental estimation under mesophilic condition and a total HRT of 20 days. An apparent first-order hydrolysis rate constant of 9.0 x 10(-3)/d for Cascade process 1 at pH 4.5-4.6, and 15.8 x 10(-3)/d for Cascade process 2 at pH 4.6-5.2 were obtained. The apparent VS degradation ratios ranged from 16.5% to 21.1% and total VA (as acetic acid) from 14.5 to 16.7 g/L. Occupying ratios for ionized VA decreased from 40.5% to 35.3% for Cascade process 1 and increased to 68.5% for Cascade process 2. However, occupying ratios of acetic acid decreased from 96.1% to 94.3% for Cascade process 1 and to 72.6% for Cascade process 2, whereas propionic acid and butyric acid ratios increased in acidogenesis of Cascade process 2. The leachate recirculation promoted hydrolysis of substrate in Cascade process 2, where apparent hydrolysis rate constant and VS degradation ratio were higher than that of Cascade process 1.     

Improving acidogenic performance in anaerobic degradation of solid organic waste using a rotational drum fermentation system

The effects of leachate from a methanogenic process on acidogenic performance of a solid recycle (SR) process by a rotational drum fermentation (RDF) system were evaluated under mesophilic condition and a hydraulic retention time (HRT) of 20 days. Two SR process configurations, SR1 and SR2, were evaluated, using fresh soybean meal or Okara as substrates. An apparent first-order hydrolysis rate constant of 5.0 x 10(-3)/d for SR1 at pH values of 4.4 and 14.4 x 10(-3)/d for SR2 at pH of 5.0, were obtained. The apparent volatile solids (VS) degradation ratio ranged from 9.6% to 19.4% and total volatile acid (as acetic acid) from 10.8 to 14.9 g/L. Occupying ratios for ionized volatile acid (VA) increased from 30.6% to 63.4% after recycling the leachate to process. However, occupying ratios of acetic acid decreased from 93.3% to 42.0% whereas propionic acid and butyric acid ratios increased in SR2. Integrating the VA production with the hydrolysis rate constants, it is clear that the recirculation of leachate considerably enhanced acidogenic performance of solid recycle process.     

Using porphyritic andesite as a new additive for improving hydrolysis and acidogenesis of solid organic wastes

The effects of porphyritic andesite on the hydrolysis and acidogenesis of solid organic wastes were investigated by batch and continuous experiments using a rotational drum fermentation system. The results of the batch experiment show that if porphyritic andesite (1%, 3%, and 5% reactants) is added initially, the pH level increases and hydrolysis and acidogenesis are accelerated. The highest surface based hydrolysis constant (26.4 × 10⁻³ kg m⁻² d⁻¹) and volatile solid degradation ratio (43.3%) were obtained at a 1% porphyritic andesite addition. In the continuous experiment, porphyritic andesite elevated the first order hydrolysis constant from 13.10 × 10⁻³ d⁻¹ to 18.82 × 10⁻³ d⁻¹. A particle mean diameter reduction rate of 33.05 μm/d and a volatile solid degradation rate of 3.53 g/L d⁻¹ were obtained under the hydraulic retention time of 4, 8, 12 and 16 d.     

典型有机固废厌氧消化微生物研究现状与发展方向

经过人工富集和驯化的兼性和严格厌氧微生物是厌氧消化工艺的核心。不同厌氧消化体系中存在的问题大多可以通过改变微生物群落的代谢活性来得到有效改善。得益于微生物组学检测技术的快速发展,对厌氧消化系统中微生物多样性的认识获得了极大的拓展,同时在微生物类群间、微生物与环境的互作关系研究方面也取得了一系列新的进展。然而,有机固废厌氧消化系统中,各种微生物以及微生物和物质的相互作用构成了更为复杂的代谢网络,所以目前对这些互作关系的解析尚不完善。本文重点关注了厌氧消化过程中的典型菌群互作关系,阐述了典型有机固废厌氧消化系统中存在的问题及微生物在其中发挥的作用,最后,立足于现有组学技术推动的微生物组研究进展,对未来有机固废厌氧消化系统微生物组的研究提出展望。     

Characteristics and biogas production potential of municipal solid wastes pretreated with a rotary drum reactor

This study was conducted to determine the characteristics and biogas production potential of organic materials separated from municipal solid wastes using a rotary drum reactor (RDR) process. Four different types of wastes were first pretreated with a commercial RDR system at different retention times (1, 2 and 3 d) and the organic fractions were tested with batch anaerobic digesters with 2.6 g VS L(-1) initial loading. The four types of waste were: municipal solid waste (MSW), a mixture of MSW and paper waste, a mixture of MSW and biosolids, and a mixture of paper and biosolids. After 20 d of thermophilic digestion (50+/-1 degrees C), it was found that the biogas yields of the above materials were in the range of 457-557 mL g VS(-1) and the biogas contained 57.3-60.6% methane. The total solid and volatile solid reductions ranged from 50.2% to 65.0% and 51.8% to 66.8%, respectively. For each material, the change of retention time in the RDR from 1 to 3d did not show significant (alpha=0.05) influence on the biogas yields of the recovered organic materials. Further studies are needed to determine the minimum retention time requirements in the RDR system to achieve effective separation of organic from inorganic materials and produce suitable feedstock for anaerobic digesters.     

Production of lipases by solid state fermentation using vegetable oil-refining wastes

Lipases were produced by a microbial consortium derived from a mixture of wastewater sludges in a medium containing solid industrial wastes rich in fats, under thermophilic conditions (temperature higher than 45 °C for 20 days) in 4.5-L reactors. The lipases were extracted from the solid medium using 100 mM Tris–HCl, pH 8.0 and a cationic surfactant agent (cetyltrimethylammonium chloride). Different doses of surfactant and buffer were tested according to a full factorial experimental design. The extracted lipases were most active at 61–65 °C and at pH 7.7–9. For the solid samples, the lipolytic activity reached up to 120,000 UA/g of dry matter. These values are considerably higher than those previously reported in literature for solid-state fermentation and highlight the possibility to work with the solid wastes as effective biocatalysts.     

Production of biogas from solid organic wastes through anaerobic digestion: a review

Anaerobic digestion treatments have often been used for biological stabilization of solid wastes. These treatment processes generate biogas which can be used as a renewable energy sources. Recently, anaerobic digestion of solid wastes has attracted more interest because of current environmental problems, most especially those concerned with global warming. Thus, laboratory-scale research on this area has increased significantly. In this review paper, the summary of the most recent research activities covering production of biogas from solid wastes according to its origin via various anaerobic technologies was presented.     

微生物在有机固废堆肥中的作用与应用

好氧堆肥是实现有机固体废弃物资源化利用的主流处理方式.堆肥腐熟是一个由微生物主导的生理生化过程,堆料通过微生物发酵实现矿质化、腐殖化和无害化,转变成腐熟的有机肥.传统的好氧堆肥存在发酵周期长、养分损失、恶臭及温室气体排放等不足.在堆肥过程中添加微生物是弥补传统好氧堆肥缺陷、提高堆肥品质和功效的有效方法.近年来,国内外在...     

Estimation of fungal growth in a solid state fermentation system

Summary Of four chemical methods for estimating mycelial biomass in koji fermentation which were examined, the modified method of Ride and Drysdale, was found to be most suitable. The observed level of aldehyde, expressed as glucosamine, is related to fungal dry weight. The assay method correlates chitin levels with some enzyme activities in the fermentation. This method may be applicable for detecting the extent of fungal growth in other solid and semi-solid substrates.     

Production of microbial lipases in a solid state fermentation system

Summary Several filamentous fungi were grown on solid state fermentation systems and selected for their highest yield in lipolytic activity, low protease levels and dairy flavor generation.P. candidum,M. miehei andP. camembertii were the selected ones. A comparison between kinetics in solid and submerged fermentation was performed usingP. candidum, with the solid system giving the highest titers and a stable production.     

Alginate lyase activity and acidogenesis during fermentation of Laminaria hyperborea

The initial hydrolysis and acidogenesis of L. hyperborea fronds wereinvestigated in anaerobic batch fermentations. The main product in theacidogenesis of fronds and fronds added extra substrates was acetate.Addition of extra glucose led to a diauxic development with glucose as thepreferred substrate and delayed initiation of alginate lyase activity. Additionof extra mannitol did not affect the initiation of lyase activity, butmaximum activity was reduced. Addition of products such as acetate andpropionate also resulted in a delayed lyase activity. The fermentation ofpure fronds resulted in a high acetate/CO₂ ratio, suggesting that thehomoacetogenic pathway played an important role in the degradation ofuronic acids. Addition of mannitol or glucose resulted in a much loweracetate/CO₂ ratio and an initial decrease in soluble CODconcentration, probably caused by biomass growth and possibly someH₂ production. Thus, the seasonal changes of mannitol and laminaranin L. hyperborea fronds will result in different digestion characteristicsfor this algae throughout the year.     

The assimilation of organic hazardous wastes by municipal solid waste landfills

Summary Co-disposal of 12 compounds representing major organic classes (aromatic hydrocarbons, halogenated hydrocarbons, pesticides, phenols, and phthalate esters) with shredded municipal solid waste was tested using a laboratory-scale column and pilot-scale lysimeter to characterize transport and transformation phenomena including sorption, volatilization and bioassimilation. Leachate and gases emitted from the lysimeters were examined for identifiable products of biotransformation. The results of this investigation provided a mechanistic evaluation of the attenuating and assimilative capacity of municipal solid waste landfills for specific organic compounds. Physical/chemical organic compound characteristics were related to refuse characteristics and composition to predict compound fate. Such knowledge is useful in developíng landfill management and operational strategies consistent with the need for control of pollutant releases.     

A Fourier-transform infrared spectroscopic analysis of organic matter degradation in a bench-scale solid substrate fermentation (composting) system

The degradation of organic matter was evaluated by a quantitative Fourier transform infrared spectroscopy (FTIR) analysis technique. The degradation process was conducted in a bench-scale reactor under controlled operational conditions of 50 degrees C, with 50-60% moisture content, and subjected to uniform aeration for 325 h. During the composting process, ATP concentration increased from 0.1 to 8 mug/g and the maximum CO(2) evolution and O(2) consumption rates reached 0.04 and 0.085 mmol/g-h, respectively. Polysaccharide content decreased approximately 50% while lignin content remained unchanged. Three regions of the FTIR spectra were used for quantification: 1070-974, 1705-1614, and 2995-2887 cm(-1), which correspond to polysaccharides and aromatic and aliphatic compounds, respectively. The actual spectra quantification consisted of peak identification using a second derivative and curve fitting technique, followed by normalization using the internal standard CaCO(3). The results obtained with the spectra quantification technique was then compared to commonly used wet chemistry extraction procedures. Reasonable correlation between the two techniques was obtained. (c) 1996 John Wiley & Sons, Inc.     

Aerobic processing of solid organic wastes for the production of a peat alternative: a review

Aerobic biodegradation is a process of importance in the recycling of organic matter which provides a means of obtaining a stable product by biological oxidative transformation. The basic process and operating process systems are briefly reviewed. The product may be taken for use at different stages of maturity from sanitisation through to a high level of humification and mineralisation. A highly stabilised product has potential as a substitute for peat, having peat-like characteristics as well as a nutrient status.     

A dynamic simulation of a two-phase anaerobic digestion system for solid wastes

In this article, a two-phase system for the digestion of wastes with a high solid content is simulated. The solids are charged to the hydrolyzer and then leachate recirculation is activated until biodegradation is nearly complete. Several parameters are tested, namely moisture, leachate recirculation flow rate, and hydrolyzer-methanizer volume ratio. The results show that recirculation rate is an important parameter subject to optimization, with optimal values corresponding to hydrolyzer hydraulic retention times below 1 day. The quantity of recirculating water must be the highest possible. As a consequence, the organic load to the methanizer is reduced, making thus possible the use of a smaller methanizer volume.     

Fungal solid state fermentation on agro-industrial wastes for acid wastewater decolorization in a continuous flow packed-bed bioreactor

This study was aimed at developing a process of solid state fermentation (SSF) with the fungi Pleurotus ostreatus and Trametes versicolor on apple processing residues for wastewater decolorization. Both fungi were able to colonize apple residues without any addition of nutrients, material support or water. P. ostreatus produced the highest levels of laccases (up to 9 U g⁻¹ of dry matter) and xylanases (up to 80 U g⁻¹ of dry matter). A repeated batch decolorization experiment was set up with apple residues colonized by P. ostreatus, achieving 50% decolorization and 100% detoxification after 24 h, and, adding fresh wastewater every 24 h, a constant decolorization of 50% was measured for at least 1 month. A continuous decolorization experiment was set up by a packed-bed reactor based on colonized apple residues achieving a performance of 100 mg dye L⁻¹ day⁻¹ at a retention time of 50 h.     

Characterizing mixing in a rotating drum bioreactor for solid-state fermentation

A method, based on the use of wheat bran particles dyed with Rhodamine-WT as tracer particles, was developed to characterize mixing in a 200 l rotating drum bioreactor used for solid state fermentation. The extraction process contributes a 15% relative error in determining Rhodamine concentrations. Extraction efficiency is not affected by autoclaving of the bran and there is no inter-particle transfer of dye during the mixing of bran within the drum. For an unbaffled drum rotated at 5 rpm the axial dispersion coefficient is 9.15 cm² min^–1.     

Changes of organic constituents of crop residues and poultry wastes during fermentation for biogas production

Summary Rice straw, maize, and cotton stalks and poultry droppings, both as such and with either wheat straw litter or sawdust litter, were used as substrates for biogasification. Water slurry combinations, each containing a crop residue and a type of poultry wastes, were prepared to achieve a uniform C/N ratio 301 (w/w) and a total solids content 10% (w/v). Biogas generated and its methane component, as well as changes brought about in the major organic constituents of the feedstocks, were monitored in laboratory biogas digesters for 90 days at 35°C. The maximum cumulative volumes of biogas and methane, were respectively 30 and 14 l/l with rice straw plus wheat straw poultry droppings. The minimum volumes were 15 l biogas/l with cotton stalks + sawdust poultry droppings and 8 l methane/l with rice straw + sawdust poultry droppings. Rice straw combinations gave the highest rates of volatile solids disappearance, short-chain fatty acid formation, and NH₄ -N liberation. No consistent trend among the poultry wastes mixed with each crop residue was evident. Changes in water-soluble substances, protein, fats, hemicellulose, cellulose and lignin depended on the components of each feedstock mixture.

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Changement dans les composants organiques des résidus de récolte et des déchets avicoles lors de la fermentation pour la production de biogaz

Résumé La paille de riz, les fanes de maïs et les tiges de coton ainsi que le lisier avicole, comme tels ou en mélange avec la litière de paille de froment ou de sciure ont servi de substrats pour la biométhanisation. On a préparé des combinaisons de boues aqueuses, chacune contenant un résidu de récolte et un type de lisier avicole, de manière à respecter un rapport C/N uniforme de 301 (p/p) et un contenu total en solides de 10% (p/vol.). On a suivi le biogaz produit et son contenu en méthane, ainsi que les changements apparus dans les principaux constituents organiques des substrats, dans des digesteurs de laboratoire pendant 90 jours à 35°C. On a obtenu les volumes cumulés maximum respectivement de 30 l/l de biogaz et de 14/l de méthane pour la paille de riz plus le lisier avicole avec paille de froment. On a obtenu les volumes cumulés minimum de 15l/l de biogaz pour les tiges de coton avec le lisier avicole avec sciure de bois et de 8 l/l de méthane pour la paille de riz et le lisier de poule avec sciure de bois. Les combinaisons avec la paille de riz ont donné les vitesses les plus élevées de disparition des solides volatils, de formation d'acides gras à courte chaîne et de libération d'azote ammoniacal. Il n'y a pas de tendances évidentes pour les lisiers avicoles mélangés avec les divers résidus de récolte. Les changements en substances hydro-solubles, en protéines, graisses, hémicellulose, cellulose et lignine dépendent de la composition de chaque mélange de substrats.

     

Nitrate removal in a packed bed reactor using volatile fatty acids from anaerobic acidogenesis of food wastes

A packed bed reactor (PBR) was fed with nitrate containing synthetic wastewater or effluent from a sequencing batch reactor used for nitrification. The C source introduced into the PBR consisted of volatile fatty acids (VFAs) produced from anaerobic acidogenesis of food wastes. When nitrate loading rates ranged from 0.50 to 1.01 kg N/m³·d, the PBR exhibited 100∼98.8% NO₃ ⁻-N removal efficiencies and nitrite concentrations in the effluent ranged from 0 to 0.6 NO₂ ⁻-N mg/L. When the PBR was further investigated to determine nitrate removal activity along the bed height using a nitrate loading rate less than 1.01 kg N/m³·d, 100% nitrate removal efficiency was observed. Approximately 83.2% nitrate removal efficiency was observed in the lower 50% of the packed-bed height. When reactor performance at a C/N ratio of 4 and a C/N ratio of 5 was compared, the PBR showed better removal efficiency (96.5%) of nitrate and less nitrite concentration in the effluent at the C/N ratio of 5. VFAs were found to be a good alternative to methanol as a carbon source for denitrification of a municipal wastewater containing 40 mg-N/L.