Lovastatin as a supplement to mitigate rumen methanogenesis: an overview.

Methane from enteric fermentation is the gas with the greatest environmental impact emitted by ruminants. Lovastatin (Lv) addition to feedstocks could be a strategy to mitigate rumen methane emissions via decreasing the population of methanogenic archaea (MA). Thus, this paper provides the first overview of the effects of Lv supplementation, focusing on the inhibition of methane production, rumen microbiota, and ruminal fermentation. Results indicated that Lv treatment had a strong anti-methanogenic effect on pure strains of MA. However, there are uncertainties from in vitro rumen fermentation trials with complex substrates and rumen inoculum.Solid-state fermentation (SSF) has emerged as a cost-effective option to produce Lv. In this way, SSF of agricultural residues as an Lv-carrier supplement in sheep and goats demonstrated a consistent decrease in ruminal methane emissions. The experimental evidence for in vitro conditions showed that Lv did not affect the volatile fatty acids (VFA). However, in vivo experiments demonstrated that the production of VFA was decreased. Lv did not negatively affect the digestibility of dry matter during in vitro and in vivo methods, and there is even evidence that it can induce an increase in digestibility. Regarding the rumen microbiota, populations of MA were reduced, and no differences were detected in alpha and beta diversity associated with Lv treatment. However, some changes in the relative abundance of the microbiota were induced. Further studies are recommended on: (i) Lv biodegradation products and stability, as well as its adsorption onto the solid matter in the rumen, to gain more insight on the "available" or effective Lv concentration; and (ii) to determine whether the effect of Lv on ruminal fermentation also depends on the feed composition and different ruminants.

Screening bacterial phosphate solubilization with bulk-tricalcium phosphate and hydroxyapatite nanoparticles.

Phosphate-solubilizing bacteria can release phosphorus (P) from insoluble minerals and benefit either soil fitness or plant growth. Bulk sized P compounds have been suggested but little is known about solubilization of nanosized materials such as hydroxyapatite nanoparticles (HANP). A screening of the initial 43 strains from vanilla rhizospheres for phosphate solubilization with bulk Ca3(PO4)2 was carried out. Subsequently, 6 strains were selected on bulk rock phosphate (RP) and HANP. Two kinetics experiments were run out regarding evaluation at 5, 10 and 20 days after inoculation (dai). Bacterial biomass production was similar in both experiments; the lowest biomass was found at 20 dai. In all cases, bacteria reduced the original culture medium pH; which was related with phosphate solubilization from the production of organic acids. Citric acid was produced by all strains. Enterobacter cloacae CP 31 was the most interesting bacterium: produced the lowest culture pH at 20 dai (4) with both Ca3(PO4)2 and RP, and 3.7 at 10 dai with HANP correlating with high soluble P concentration (536, 64 and 13 mg L-1 with these P sources, respectively). This bacterium should be tested as an inoculant in plants to reveal its potential as plant promoter growth and HANP to suggest its role in the potential use of nano-P fertilizers.

Effect of nixtamalization processes on mitigation of acrylamide formation in tortilla chips.

Acrylamide can be generated from food components during tortilla chips frying. Thus, the aim of this research was to study different nixtamalization processes as traditional (TNP) with lime [Ca(OH)2], ecological (ENP) with CaCO3, classic nixtamalization (CNP) that uses wood ash and extrusion (EXT) with no Ca+2 source on mitigating the acrylamide formation in deep-fat frying tortilla chips. Acrylamide quantification was done through HPLC-UV. Lower acrylamide content in tortilla chips was for CNP with 46.3 µg/kg, followed by TNP with 55.0 µg/kg, ENP with 694.6 µg/kg and EXP with 1443.4 µg/kg. Differences in acrylamide values among samples can be related to effect of cations (Ca2+, Mg2+, Fe2+, Zn2+, Na+ and K+) present in wood ashes, lime and salts used as raw materials. Correlation of (r = 0.85; p <0.0005) was observed in color of tortilla chips, moisture, texture, blisters, and oil with acrylamide. Nixtamalization process is an effective and inexpensive strategy for acrylamide mitigation.

Structure-activity study of acute neurobehavioral effects of cyclohexane, benzene, m-xylene, and toluene in rats.

Toluene is a widely misused solvent that causes a variety of behavioral effects in both humans and animals. Preclinical and clinical research has provided evidence that toluene inhalation produces psychoactive effects similar to those caused by other Central Nervous System depressant drugs, but little is known about the consequences of inhaling solvents other than toluene that are also present in commercial products. As part of this research project, we studied the effects of hydrocarbon solvents chemically related to toluene on anxiety-like behavior, passive-avoidance learning, nociception, motor coordination and social interaction. We tested independent groups of adolescent male Wistar rats in the burying behavior task, step through avoidance learning task, hot plate test, shock threshold test, social interaction or rotarod tests after a 30 min exposure to either cyclohexane, benzene, toluene or m-xylene (2000 to 8000 ppm). Control animals breathed only air. Benzene, toluene and m-xylene produced anxiolytic-like actions, impaired learning, caused antinociception and decreased social interaction in a concentration-dependent manner. Locomotor coordination was impaired only with 8000 ppm m-xylene and 8000 ppm toluene. Cyclohexane had no effect on any of the behavioral tasks. Our data suggest that the aromatic ring is critical for solvents to produce a wide variety of behavioral effects.

Phytoremediation assisted by mycorrhizal fungi of a Mexican defunct lead-acid battery recycling site.

A field experiment was conducted during 15 months to study the effects of four arbuscular mycorrhizal fungi (AMF) on the growth of Ricinus communis accession SF7. Plants were established on amended soil (vermicompost:sawdust:soil 1:1:1) severely polluted by lead-acid batteries (LAB) located at Mexico State, Mexico. Plants inoculated with Acaulospora sp., Funneliformis mosseae and Gigaspora gigantea had 100% survival in comparison to non-inoculated plants (57%). These same AMF enhanced palmitic and linoleic acids content in seeds of R. communis. Acaulospora sp. modified rhizosphere soil pH and decreased 3.5 folds Pb foliar concentrations while F. mosseae BEG25 decreased three times Pb soil availability in comparison to non-inoculated plants. Spatial changes in Pb soil availability were observed at the end of this research. No fungal effect on P, Ca, Cu foliar concentrations, soluble sugars, proline, chlorophyll or on the activity of two oxidative stress enzymes was observed. Mycorrhizal colonization from the inoculated fungi was between 40% and 60%, while colonization by native fungi was between 16% and 22%. A similar percentage of foliar total phenolic compounds was observed in non-mycorrhizal plants and those inoculated with G. gigantea and Acaulospora sp. This is the first research reporting effects of AMF on R. communis (castor bean) shrubs when grown on a LAB recycling site suggesting the use of Acaulospora sp. and F. mosseae BEG25 in phytostabilization to ameliorate Pb pollution and decreasing its ecological risk.

Biotransformation of benzo[a]pyrene by the thermophilic bacterium Bacillus licheniformis M2-7.

Benzo[a]pyrene (BaP) is recognized as a potentially carcinogenic and mutagenic hydrocarbon, and thus, its removal from the environment is a priority. The use of thermophilic bacteria capable of biodegrading or biotransforming this compound to less toxic forms has been explored in recent decades, since it provides advantages compared to mesophilic organisms. This study assessed the biotransformation of BaP by the thermophilic bacterium Bacillus licheniformis M2-7. Our analysis of the biotransformation process mediated by strain M2-7 on BaP shows that it begins during the first 3 h of culture. The gas chromatogram of the compound produced shows a peak with a retention time of 17.38 min, and the mass spectra shows an approximate molecular ion of m/z 167, which coincides with the molecular weight of the chemical formula C6H4(COOH)2, confirming a chemical structure corresponding to phthalic acid. Catechol 2,3-dioxygenase (C23O) enzyme activity was detected in minimal saline medium supplemented with BaP (0.33 U mg-1 of protein). This finding suggests that B. licheniformis M2-7 uses the meta pathway for biodegrading BaP using the enzyme C23O, thereby generating phthalic acid as an intermediate.

Biodegradability of Nonionic Surfactant Used in the Remediation of Groundwaters Polluted with PCE.

The objective of this work was to evaluate the degradation of the nonionic surfactant Tween 80 by a PCE-degrading consortium anchored in bioparticles of fluidized bed bioreactors used in onsite remediation. Batch lab-scale bioreactors were set with dominant denitrifying (DN), methanogenic (M), and aerobic (Ab) metabolisms. Tween 80 at 100 mg/L was the sole source of carbon and energy. Denitrifying bioreactors had the highest surfactant removal (70%). Tween removals in M and Ab bioreactors were 53 and 37%, respectively. Removals of organic matter (COD) closely followed the efficiencies reported for Tween. This strongly suggested that degradation of Tween 80 occurred. Positive consequences of Tween degradation in remediation are first, the surfactant will not become an environmental/health liability by remaining as a recalcitrant or toxic substance in aquifers or in treated effluents; and second, savings on aeration could be achieved by conducting Tween 80 degradation in anaerobic conditions, either DN or M.

Effect of the pesticide lindane on the biomass of the microalgae Nannochloris oculata.

This study assesses the growth of the microalgae Nannochloris oculata in the presence of lindane and the ability of N. oculata to remove lindane from media. Algal biomass increased with 0.1 and 0.5 mg L-1 of lindane, and lindane concentrations in the media decreased. N. oculata removed 73% and 68.2% of lindane in the 0.1 and 0.5 mg L-1 media concentrations, respectively. Algal biomass decreased to the level of the control at lindane concentrations greater than 2.5 mg L-1, probably due to toxicity. N. oculata removed lindane from the media at concentrations lower than 1.0 mg L-1. Thus, N. oculata may be useful for lindane bioremediation in contaminated aquatic systems.

Biohydrogen, biomethane and bioelectricity as crucial components of biorefinery of organic wastes: a review.

Biohydrogen is a sustainable form of energy as it can be produced from organic waste through fermentation processes involving dark fermentation and photofermentation. Very often biohydrogen is included as a part of biorefinery approaches, which reclaim organic wastes that are abundant sources of renewable and low cost substrate that can be efficiently fermented by microorganisms. The aim of this work was to critically assess selected bioenergy alternatives from organic solid waste, such as biohydrogen and bioelectricity, to evaluate their relative advantages and disadvantages in the context of biorefineries, and finally to indicate the trends for future research and development. Biorefining is the sustainable processing of biomass into a spectrum of marketable products, which means: energy, materials, chemicals, food and feed. Dark fermentation of organic wastes could be the beach-head of complete biorefineries that generate biohydrogen as a first step and could significantly influence the future of solid waste management. Series systems show a better efficiency than one-stage process regarding substrate conversion to hydrogen and bioenergy. The dark fermentation also produces fermented by-products (fatty acids and solvents), so there is an opportunity for further combining with other processes that yield more bioenergy. Photoheterotrophic fermentation is one of them: photosynthetic heterotrophs, such as non-sulfur purple bacteria, can thrive on the simple organic substances produced in dark fermentation and light, to give more H2. Effluents from photoheterotrophic fermentation and digestates can be processed in microbial fuel cells for bioelectricity production and methanogenic digestion for methane generation, thus integrating a diverse block of bioenergies. Several digestates from bioenergies could be used for bioproducts generation, such as cellulolytic enzymes and saccharification processes, leading to ethanol fermentation (another bioenergy), thus completing the inverse cascade. Finally, biohydrogen, biomethane and bioelectricity could contribute to significant improvements for solid organic waste management in agricultural regions, as well as in urban areas.

Emulsifying activity and stability of a non-toxic bioemulsifier synthesized by Microbacterium sp. MC3B-10.

A previously reported bacterial bioemulsifier, here termed microbactan, was further analyzed to characterize its lipid component, molecular weight, ionic character and toxicity, along with its bioemulsifying potential for hydrophobic substrates at a range of temperatures, salinities and pH values. Analyses showed that microbactan is a high molecular weight (700 kDa), non-ionic molecule. Gas chromatography of the lipid fraction revealed the presence of palmitic, stearic, and oleic acids; thus microbactan may be considered a glycolipoprotein. Microbactan emulsified aromatic hydrocarbons and oils to various extents; the highest emulsification index was recorded against motor oil (96%). The stability of the microbactan-motor oil emulsion model reached its highest level (94%) at 50 °C, pH 10 and 3.5% NaCl content. It was not toxic to Artemia salina nauplii. Microbactan is, therefore, a non-toxic and non-ionic bioemulsifier of high molecular weight with affinity for a range of oily substrates. Comparative phylogenetic assessment of the 16S rDNA gene of Microbacterium sp. MC3B-10 with genes derived from other marine Microbacterium species suggested that this genus is well represented in coastal zones. The chemical nature and stability of the bioemulsifier suggest its potential application in bioremediation of marine environments and in cosmetics.

The influence of total solids content and initial pH on batch biohydrogen production by solid substrate fermentation of agroindustrial wastes.

Hydrogen is a valuable clean energy source, and its production by biological processes is attractive and environmentally sound and friendly. In México 5 million tons/yr of agroindustrial wastes are generated; these residues are rich in fermentable organic matter that can be used for hydrogen production. On the other hand, batch, intermittently vented, solid substrate fermentation of organic waste has attracted interest in the last 10 years. Thus the objective of our work was to determine the effect of initial total solids content and initial pH on H2 production in batch fermentation of a substrate that consisted of a mixture of sugarcane bagasse, pineapple peelings, and waste activated sludge. The experiment was a response surface based on 2(2) factorial with central and axial points with initial TS (15-35%) and initial pH (6.5-7.5) as factors. Fermentation was carried out at 35 °C, with intermittent venting of minireactors and periodic flushing with inert N2 gas. Up to 5 cycles of H2 production were observed; the best treatment in our work showed cumulative H2 productions (ca. 3 mmol H2/gds) with 18% and 6.65 initial TS and pH, respectively. There was a significant effect of TS on production of hydrogen, the latter decreased with initial TS increase from 18% onwards. Cumulative H2 productions achieved in this work were higher than those reported for organic fraction of municipal solid waste (OFMSW) and mixtures of OFMSW and fruit peels waste from fruit juice industry, using the same process. Specific energetic potential due to H2 in our work was attractive and fell in the high side of the range of reported results in the open literature. Batch dark fermentation of agrowastes as practiced in our work could be useful for future biorefineries that generate biohydrogen as a first step and could influence the management of this type of agricultural wastes in México and other countries and regions as well.

Influence of discontinuing feeding degradable cosubstrate on the performance of a fluidized bed bioreactor treating a mixture of trichlorophenol and phenol.

The purpose of our research was to evaluate the effect of eliminating supplementation of sucrose to the reactor influent on the performance of a lab scale partially-aerated methanogenic fluidized bed bioreactor (PAM-FBBR). Two operational stages were distinguished: in the first stage the influent contained a mixture of 120/30/1000 mg/L of 2,4,6-trichlorophenol/phenol/COD-sucrose (TCP/Phe/COD-sucrose); in the second stage only the xenobiotic concentrations were the same 120/30 mg/L of TCP/Phe whereas sucrose addition was discontinued. Removal efficiencies of TCP, Phe, and COD were very high and close for both stages; i.e., η(TCP): 99.9 and 99.9%; η(Phe): 99.9 and 99.9%; η(COD) = 96.46 and 97.48% for stage 1 and stage 2, respectively. Traces of 2,4,6 dichlorophenol (0.05 mg/L) and 4-chlorophenol (0.07-0.26 mg/L) were found during the first 15 days of operation of the second stage, probably due to the adaptation to no co-substrate conditions. Net increase of chloride anion Cl(-) in effluent ranged between 59.5 and 61.5 mg Cl(-)/L that was very close to the maximum theoretical concentration of 62.8 mg Cl(-)/L. PCR-DGGE analysis revealed a richness decrease of eubacterial domain posterior to sucrose elimination from the influent whereas archaeal richness remained almost the same. However, the bioreactor performance was not negatively affected by discontinuing the addition of co-substrate sucrose. Our results indicate that the application of PAM-FBBR to the treatment of groundwaters polluted with chlorophenols and characterized by the lack of easily degradable co-substrates, is a promising alternative for on site bioremediation.

Anthracene decomposition in soils by conventional ozonation.

Anthracene decomposition in solid phase by conventional ozonation was investigated employing model and real soil samples. Reaction in a two-phase system (soil-ozone) and a three-phase system (soil-water-ozone) was studied. The total anthracene decomposition in the two studied systems (sand-ozone and burned soil-ozone) was obtained at 15 and 30 min of treatment by ozone, respectively, and the efficiency of ozonation was depended on the water content in treated soil samples. The anthracene degradation in an agricultural soil (free water) was carried up slower (only 30% after 90 min of ozonation), because the real solid samples content organic matter that provokes the additionally ozone consuming. The pre-ozonation of free anthracene agricultural soil depicts the content of the organic matter fraction, which have the ozone reactivity orders as aromatic>aliphatic>polar. In all cases, the ozonation by-products were identified partiality; the majority of by-products formatted react with ozone. Actually some of them were decomposed totally, while others were accumulated. Some products identified in all systems such as anthrone, 9,10-anthraquinone and phthalic acid, are less toxic than the anthracene.

Re-fermentation of washed spent solids from batch hydrogenogenic fermentation for additional production of biohydrogen from the organic fraction of municipal solid waste.

In the first batch solid substrate anaerobic hydrogenogenic fermentation with intermittent venting (SSAHF-IV) of the organic fraction of municipal solid waste (OFMSW), a cumulative production of 16.6 mmol H(2)/reactor was obtained. Releases of hydrogen partial pressure first by intermittent venting and afterward by flushing headspace of reactors with inert gas N(2) allowed for further hydrogen production in a second to fourth incubation cycle, with no new inoculum nor substrate nor inhibitor added. After the fourth cycle, no more H(2) could be harvested. Interestingly, accumulated hydrogen in 4 cycles was 100% higher than that produced in the first cycle alone. At the end of incubation, partial pressure of H(2) was near zero whereas high concentrations of organic acids and solvents remained in the spent solids. So, since approximate mass balances indicated that there was still a moderate amount of biodegradable matter in the spent solids we hypothesized that the organic metabolites imposed some kind of inhibition on further fermentation of digestates. Spent solids were washed to eliminate organic metabolites and they were used in a second SSAHF-IV. Two more cycles of H(2) production were obtained, with a cumulative production of ca. 2.4 mmol H(2)/mini-reactor. As a conclusion, washing of spent solids of a previous SSAHF-IV allowed for an increase of hydrogen production by 15% in a second run of SSAHF-IV, leading to the validation of our hypothesis.

Enzymes involved in the biodegradation of hexachlorocyclohexane: a mini review.

The scope of this paper encompasses the following subjects: (i) aerobic and anaerobic degradation pathways of γ-hexachlorocyclohexane (HCH); (ii) important genes and enzymes involved in the metabolic pathways of γ-HCH degradation; (iii) the instrumental methods for identifying and quantifying intermediate metabolites, such as gas chromatography coupled to mass spectrometry (GC-MS) and other techniques. It can be concluded that typical anaerobic and aerobic pathways of γ-HCH are well known for a few selected microbial strains, although less is known for anaerobic consortia where the possibility of synergism, antagonism, and mutualism can lead to more particular routes and more effective degradation of γ-HCH. Conversion and removals in the range 39%-100% and 47%-100% have been reported for aerobic and anaerobic cultures, respectively. Most common metabolites reported for aerobic degradation of lindane are γ-pentachlorocyclohexene (γ-PCCH), 2,5-dichlorobenzoquinone (DCBQ), Chlorohydroquinone (CHQ), chlorophenol, and phenol, whereas PCCH, isomers of trichlorobenzene (TCB), chlorobenzene, and benzene are the most typical metabolites found in anaerobic pathways. Enzyme and genetic characterization of the involved molecular mechanisms are in their early infancy; more work is needed to elucidate them in the future. Advances have been made on identification of enzymes of Sphingomonas paucimobilis where the gene LinB codifies for the enzyme haloalkane dehalogenase that acts on 1,3,4,6-tetrachloro 1,4-cyclohexadiene, thus debottlenecking the pathway. Other more common enzymes such as phenol hydroxylase, catechol 1,2-dioxygenase, catechol 2,3-dioxygenase are also involved since they attack intermediate metabolites of lindane such as catechol and less substituted chlorophenols. Chromatography coupled to mass spectrometric detector, especially GC-MS, is the most used technique for resolving for γ-HCH metabolites, although there is an increased participation of HPLC-MS methods. Scintillation methods are very useful to assess final degradation of γ-HCH.

Design of a new rotating drum bioreactor operated at atmospheric pressure on the bioremediation of a polluted soil.

This paper reports the effect of the operation and design characteristics of rotating drum bioreactors (RDBs) aerated by natural convection and applied to the treatment of a soil highly polluted with weathered total petroleum hydrocarbons (TPH) (55,000 +/- 2,600 mg/kg). The parameters studied were length to diameter ratio (L/D), rotating speed (N) and lifter type. The highest TPH removal (59.6 +/- 0.7%) was obtained with the RDB of the lowest L/D ratio (1.5). Removals diminished by 27, 36 and 56%, with a ratio increment of 2.1, 3.1 and 5.1, respectively. Increment of the N, at an optimal value and lifter change from straight to helicoidal showed an improvement on the TPH removal of 20 and 30%, respectively. According to these results, slurry surface renewal through the variation of the N and the change of slurry flow was able to improve TPH removal in RDBs operated by natural convection.

Effect of inhibition treatment, type of inocula, and incubation temperature on batch H2 production from organic solid waste.

Two types of induction treatments (heat-shock pretreatment, HSP, and acetylene, Ac), inocula (meso and thermophilic) and incubation temperatures (37 and 55 degrees C) were tested according to a full factorial design 2(3) with the aim of assessing their effects on cumulative H(2) production (P(H), mmol H(2)/mini-reactor), initial H(2) production rate (R(i,H), micromol H(2)/(g VS(i) x h)), lag time (T(lag), h), and metabolites distribution when fermenting organic solid waste with an undefined anerobic consortia in batch mini-reactors. Type of inocula did not have a significant effect on P(H), T(lag), and R(i,H) except for organic acids production: mini-reactors seeded with thermophilic inocula had the highest organic acid production. Concerning the induction treatment, it was found that on the average Ac only affected in a positive way the P(H) and T(lag). Thus, P(H) in Ac-inhibited units (6.97) was 20% larger than those in HSP-inhibited units (5.77). Also, Ac favored a shorter T(lag) for P(H) in comparison with HSP (180 vs. 366). Additionally, a positive correlation was found between H(2) and organic acid production. In contrast, solvent concentration in heat-shocked mini-reactors were slightly higher than in reactors spiked with Ac. Regarding the incubation temperature, on the average mesophilic temperature affected in a positive and very significant way P(H) (10.07 vs. 2.67) and R(i,H) (2.43 vs. 0.76) with minimum T(lag) (87 vs. 459). The positive correlation between H(2) and organic acids production was found again. Yet, incubation temperature did not seem to affect solvent production. A strong interaction was observed between induction treatment and incubation temperature. Thus, Ac-inhibited units showed higher values of P(H) and R(i,H) than that HSP-inhibited units only under thermophilic incubation. Contrary to this, HSP-inhibited units showed the highest values of P(H) and R(i,H) only under mesophilic conditions. Therefore, the superiority of an induction treatment seems to strongly depend on the incubation temperature.

Improvement of biohydrogen production from solid wastes by intermittent venting and gas flushing of batch reactors headspace.

Headspace of batch minireactors was intermittently vented and gas flushed with N2 in order to enhance H2 production (PH) by anaerobic consortia degrading organic solid wastes. Type of inocula (meso and thermophilic), induction treatment (heat-shock pretreatment, HSP, and acetylene, Ac), and incubation temperature (37 and 55 degrees C) were studied by means of a factorial design. On average, it was found that mesophilic incubation had the most significant positive effect on PH followed by treatment with Ac, although the units with the best performance (high values of PH, initial hydrogen production rate, and short lag time) were those HSP-induced units incubated at 37 degrees C (type of inocula was not significant). In this way, after 720 h of incubation PH was inhibited in those units by H2 partial pressure (pH2) of 0.54 atm. Venting and gas flushing with N2 was efficient to eliminate that inhibition achieving additional hydrogen generation in subsequent incubation cycles although smaller than the first one. Thus, four cycles of PH were obtained from the same substrate with neither addition of inocula nor application of induction treatment obtaining an increment of 100% in the generated H2. In those subsequent cycles there was a positive correlation between PH and organic acids/solvent ratio; maximum values were found in the first cycle. Solventogenesis could be clearly distinguished in third and fourth production cycles, probably due to a metabolic shift originated by high organic acid concentrations.

Comportamiento adsortivo-desortivo del lindano en un suelo agrícola / Adsorptive-desorptive benhaviour of lindane in an agricultural soil

El objetivo de este trabajo fue estudiar el comportamiento adsortivo-desortivo del pesticida lindano en un suelo agrícola con importante contenido de materia orgánica, utilizando el coeficiente de histéresis diferencial (CHPoggi). Además se obtuvo una expresión analítica simple del CHPoggi para el caso mixto, cuando la isoterma de adsorción sigue el modelo lineal y la isoterma de desorción sigue el modelo de Langmuir. Se obtuvo una isoterma de adsorción lineal, q= 3,91·C y una isoterma de desorción de tipo Langmuir, q= (32,9·C)/(1+1,11·C). Utilizando ambas isotermas y la definición del coeficiente de histéresis diferencial, se dedujo una expresión matemática para éste en un punto de interés (qj, Cj) de la forma CHPoggi= a·b/kl , donde a: capacidad máxima de la curva de desorción en mg·kg-1; b: coeficiente relacionado a la razón de crecimiento de la curva de desorción, en l·mg-1; y kl: coeficiente de adsorción lineal en l·kg-1. El valor del coeficiente de histéresis para un punto de interés q= 24,5mg·kg-1 y C= 6,0mg·l-1, utilizando las tangentes de ambas isotermas dió un valor de 6,6, y utilizando la expresión matemática se obtuvo un valor de 8,4 indicando una buena aproximación al primer método al considerar los errores experimentales. El valor de CHPoggi indica que la histéresis lindano-suelo agrícola fue moderada a alta

Remoción de percloroetileno en dos tipos de sistemas anaerobios continuos

Se evaluó y comparó el desempeño de dos reactores mesofílicos metanogénicos de mezcla completa escala laboratorio (RMC1, RMC2) y un reactor metanogénico de lecho fluidizado (RANLEF, con carbón activado granular como soporte) para remoción de percloretileno (PCE) tras adicionar una moderada cantidad de metanol en el afluente. Los reactores fueron operados con cargas de 0,07 y 1gDQO·l-1·d-1, y tiempos de retención hidráulica de 15 y 1d, respectivamente. El diseño experimental consistió en tres períodos de operación: régimen metanogénico con metanol como fuente de C (periodo 1), igual con aclimatación a 20mgPCE·l-1 (periodo 2.1) o 40mgPCE·l-1 (2.2), e igual con 40mgPCE·l-1 en RANLEF y RMC1, y 20mgPCE·l-1 en RMC2 (periodo 3). La eficiencia de PCE y DQO fue más alta en RANLEF en el primer periodo; el CH4 en biogás y el incremento de cloro fueron similares en los tres reactores. Durante el periodo 2.2 la remoción de PCE alcanzó 81% en RANLEF, sugestivo de buena aclimatación a mayor entrada de PCE; la remoción de DQO se mantuvo alta, y el contenido de CH4 en biogás alcanzó un valor medio de 64% v/v, indicando un régimen metanogénico satisfactorio. Los RMCs experimentaron un deterioro drástico en su desempeño al aumentar PCE de 20 a 40mg·l-1, por lo que se regresó el RMC1 a 20mg·l-1. El desempeño de RMC2 se mantuvo bajo, sugiriendo un impacto negativo sobre la metanogénesis y remoción de PCE. En contraste, el RMC1 con 20mg·l-1 se recuperó del estado transitorio negativo, exhibiendo desempeño similar al RANLEF alimentado con 40mg·l-1. En el período 3, el RANLEF con 40mg·l-1 y el RMC1 con 20mg·l-1 mostraron desempeño similar, mientras que el RMC2 con 40mg·l-1 exhibió una disminución en la eficiencia de remoción de DQO, baja productividad de biogás y contenido de CH4 en biogás, pero la remoción de PCE estuvo cerca de RANLEF y RMC1. La eficiencia de descloración del RMC2 fue significativamente menor que la del RANLEF, el cual fue más robusto y estable en el proceso anaerobio de remoción de alta concentración de PCE.

Performance was evaluated and compared in two lab-scale mesophilic methanogenic complete mix reactors (RMC1, RMC2) and a methanogenic fluidized bed reactor (RANLEF) for removal of perchloroethylene (PCE) when fed a moderate concentration of methanol. The RMCs and RANLEF were operated at loading rates of 0.07 and 1gCOD·l-1·d-1, and hydraulic retention times of 15 and 1 day, respectively. The experimental design consisted of three periods of operation: methanogenic regime with methanol as carbon source (1); same with acclimation to 20 (2.1) or 40mgPCE·l-1 (2.2); and same with 40mgPCE·l-1 in RANLEF and RMC1 and 20 mgPCE·l-1 in RMC2 (3). In the first period both PCE and COD removals were higher in RANLEF; biogas CH4 content and chloride increase were similar in the three reactors. During period 2.2, PCE removal increased up to 81% in RANLEF, suggesting a good acclimation to the higher inflow PCE concentration; COD reduction remained high, and CH4 in biogas indicated a satisfactory methanogenic regime. The RMCs experienced drastic performance impairments upon increase of inflow PCE (20 to 40mg·l-1), and RMC1 was returned to operate with 20mgPCE·l-1. RMC2 performance remained poor, showing a drastic deterioration of methanogenesis and PCE removal. By contrast, RMC1 with 20mgPCE·l-1 recovered from the negative transient state and exhibited similar performance to that of RANLEF fed 40mg·l-1. In period 3, RANLEF with 40mg·l-1 and RMC1 with 20mg·l-1 showed similar performances, whereas RMC2 kept with 40mg·l-1 exhibited impaired COD removal, lower biogas productivity and CH4 biogas content, but a PCE removal very close to RANLEF and RMC1. The dehalogenation efficiency of RMC2 was significantly lower than that of the RANLEF, which appears to be a more robust and stable anaerobic process for the effective removal of high concentrations of PCE.

Avaliou-se e comparou-se o desempenho de dois reatores mesofílicos metanogênicos de mistura completa escala laboratório (RMC1, RMC2) e um reator metanogênico de leito fluidizado (RANLEF, com carvão ativado granular como suporte) para remoção de percloretileno (PCE) depois de adicionar uma moderada quantidade de metanol no afluente. Os reatores foram operados com cargas de 0,07 e 1gDQO·l-1·d-1, e tempos de retenção hidráulica de 15 e 1d, respectivamente. O projeto experimental consistiu em três períodos de operação: regime metanogênico com CH4 como fonte de carbono (1), igual com aclimatação a 20mgPCE·l-1 (2.1) ou 40mgPCE·l-1 (2.2), e igual com 40mgPCE·l-1 em RANLEF e RMC1, e 20mgPCE·l-1 em RMC2 (3). A eficiência de PCE e DQO foi mais alta em RANLEF no primeiro período; o CH4 em biogás e o incremento de cloro foram similares nos três reatores. Durante o período 2.2 a remoção de PCE alcançou 81% em RANLEF, sugestivo de boa aclimatação a maior entrada de PCE; a remoção de DQO se manteve alta, e o conteúdo de CH4 em biogás alcançou um valor médio de 64% v/v, indicando um regime metanogênico satisfatório. Os RMCs experimentaram um deterioro drástico no seu desempenho ao aumentar PCE de 20 a 40mg·l-1, pelo que se regressou o RMC1 a 20mg·l-1. O desempenho de RMC2 se manteve baixo, sugerindo um impacto negativo sobre a metanogênesis e remoção de PCE. Em contraste, o RMC1 com 20mg·l-1 se recuperou do estado transitório negativo, exibindo desempenho similar ao RANLEF alimentado com 40mg·l-1. No período 3, o RANLEF com 40mg·l-1 e o RMC1 com 20mg·l-1 mostraram desempenho similar, enquanto que o RMC2 com 40mg·l-1 exibiu uma diminuição na eficiência de remoção de DQO, baixa produtividade de biogás e conteúdo de CH4 em biogás, mas a remoção de PCE esteve perto de RANLEF e RMC1. A eficiência de descloração do RMC2 foi significativamente menor que a do RANLEF, o qual foi mais robusto e estável no processo anaeróbio de remoção de alta concentração de PCE.