Operating a full-scale poultry manure anaerobic digester

A full-scale, completely-mixed digester, with a liquid capacity of 587 m³, was constructed to process the manure from 70 000 caged layers. Biogas from the digester was used as fuel for an engine/generator set. The operating temperature was maintained at 35°C using waste heat from the engine. The digester was operated on a 22–24 day HRT. Digester influent averaged 5·90% TS, 5250 ppm TKN, and 3790 ppm NH₃N. Digester effluent averaged 3·11% TS, 5090 ppm TKN, and 4060 ppm NH₃N.Sustained operation of the digester was achieved during the period of study (8/83−4/85). During this period biogas production averaged 0·38 m³ kg⁻¹ VS added (0·58 m³ kg⁻¹ VS destroyed). The CH₄ content averaged 58·0%. The major operational problem encountered was grit accumulation in the digester. This problem was reduced by settling most of the grit from the manure prior to the digester. Biogas production was reduced when concentrated lagoon-liquid was used as make-up water. Approximately 22% of the electricity produced was required for operating the system.     

Influence of lignin on the methanization of lignocellulosic wastes

The effect on anaerobic digestion of reducing the lignin content of vine shoots to 1% (w/w), by treatment with sodium chlorite in an acid medium at 80°C, is reported. The yields of methane obtained were 240 ml of CH₄ g⁻¹ of VS (volatile solids) fed for untreated vine shoots, and 370 ml of CH₄ g⁻¹ of VS fed for treated vine shoots. A mathematical model was used to calculate the kinetic parameters H and μ, and the increased biodegradability of the substrate in which lignin had been removed was confirmed. A study of the mass balances of the process under optimum conditions (temperature = 35°C; loading rate of 1 g litre⁻¹ digester day⁻¹) enabled the percentage of degraded cellulose to be calculated (35·5% for untreated vine shoots, 81·5% for the treated vine shoots), as were the volumes of biogas and methane produced per gram of VS introduced (VS₁) and degraded. The blocking effect of lignin on the methanization process was confirmed.     

The susceptibility of Apodemus agrarius and Rattus losea to the anticoagulant rodenticide,flocoumafen

Flocoumafen had good rodenticidal action against Apodemus agrarius and Rattus losea. The acute oral LD₅₀ for male A. agrarius and R. losea was 1·22 mg kg⁻¹ and 1·36 mg kg⁻¹ respectively. Flocoumafen bait was more toxic to R. losea than to A. agrarius. At bait concentrations of 0·002–0·005%, flocoumafen had a single-feed potency with mortalities of 90–100% for R. losea and 77·8–100% for A. agrarius. Experimental baits prepared using the manufacturing 0·5% master mix of flocoumafen were palatable to both species.     

Algal biomass production,N uptake and N2 fixation in a synthetic medium

An experiment was conducted in the growth chamber to quantify the biomass production, N removal and N₂ fixation from a synthetic medium by Chlamydomonas reinhardtii and Anabaena flos-aquae. Nitrogen was supplied at a concentration of 100 mg liter⁻¹ of NO₃⁻−¹⁵N and NH₄⁺−¹⁵ (3·5 atom %), respectively. After 21 days Chlamydomonas reinhardtii removed an average of 83·8 and 78·7 mg N liter⁻¹ as NO₃⁻ and NH₄⁺, respectively. Averages of 0·89 and 0·71 g liter⁻¹ (first batch), 1·63 and 0·95 g liter⁻ (second batch) algal biomass were collected from NO₃⁻ and NH₄⁺ media, respectively. Uptake rates of 0·11 mg ¹⁵N g⁻¹ algae day⁻¹ from NO₃⁻ medium and 0·10 mg ¹⁵N g⁻¹ algae day⁻¹ from NH₄⁺ medium were calculated. Algal cells grown in NO₃⁻ and NH₄⁺ medium contained 71 and 65 g N kg⁻¹ (first batch), 39 and 58 g N kg⁻¹ (second batch), respectively. Anabaena flos-aquae produced averages of 0·58 and 0·46 g liter⁻¹ (first batch), 0·55 and 0·48 g liter⁻¹ (second batch) after 14 days of growth from NO₃⁻ and NH₄⁺ media, respectively. Blue-green algal biomass contained higher N (81–98 g kg⁻¹) than green algae. Isotope dilution method for determining N₂ fixation indicated that 55% and 77% of total N of blue-green algae grown in NO₃⁻ and NH₄⁺ media, respectively, was derived from the atmosphere.     

Development of mixed inoculum for methane enriched biogas production

Inocula were collected from four different sources such as Jajmau tannery waste treatment plant (ITW), Jajmau municipal waste treatment (IMW), Unnao distillery (IDW) and a batch reactor, in which the sludge of a field scale biogas reactor was added to cow dung slurry to develop inoculum (IBS). A combination of these mixed inocula were used for biogas production at 35°C in laboratory scale reactor (10 L capacity) and the average yield of biogas (0.547 Lg^?1 volatile solid (VS)) and methane (0.323 Lg^?1VS) in 41 d was higher in case of mixed inoculum IMW ₁ (IMW+IBS), with maximum methane content in biogas (68% during 27–30 d), as compared to other mixed inocula as well as control i.e. ITW ₁ (ITW+IBS), IDW₁ (IDW+IBS) and IBS. The corresponding yields of gas were biogas (0.505, 0.536 and 0.456 Lg^?1VS), methane (0.288, 0.305, and 0.245 Lg^?1VS) where as, the corresponding maximum methane content in biogas was 62% during 29–33d, 64% during 29–33 d and 62% during 27–29 d in ITW₁, IDW₁ and IBS.     

Ethanol fermentation by an efficient strain,NRRL B-4286, of Zymomonas mobilis

We studied the effect of the initial substrate concentration over the range of 100–250 g·l⁻¹ on the fermentation kinetics in batch cultures of Zymomonas mobilis NRRL B-4286 on glucose, fructose, and sucrose, using an adapted initial inoculum. With increasing concentrations of substrate, parameters related to growth were more rapidly and strongly affected than those related to ethanol production. This strain produced 94.0 g·l⁻¹, 76.9 g·l⁻¹, and 66.5 g·l⁻¹ of ethanol at glucose, fructose, and sucrose concentrations of 200 g·l⁻¹, respectively, more than the amount produced by the efficient strain ZM4 (NRRL B-14023).     

Growth of Methanobacterium thermoautotrophicum on H2CO2: High CH4 productivities in continuous culture

The thermophilic methanogenic bacterium, Methanobacterium thermoautotrophicum, was grown on H₂CO₂. In continuous culture, high CH₄ productivities were obtained (288 litres litre⁻¹ day⁻¹) with 96% CH₄ in the effluent gas, i.e. the productivity was twice as high as that obtained previously by other authors, with pure or mixed cultures; the biomass was 3·6 g dry wt litre⁻¹.     

A novel thermophilic β-mannanase with broad-range pH stability from Lichtheimia ramosa and its synergistic effect with α-galactosidase on hydrolyzing palm kernel meal

β-Mannanase is the key enzyme in the hydrolysis of mannan which has been widely applied in diverse industrial fields such as biobleaching pulps, food and feed industry, bioethanol and pharmaceutical applications. In this study, a novel GH5 family β-mannanase gene (LrMan5B) with 381 amino acid residues was identified from Lichtheimia ramosa, and highly expressed in Pichia pastoris X33. The amino acid sequence shares the highest identity (64%) with the β-mannanase from Rhizomucor miehei. Purified recombinant LrMan5B showed the optimal activity at pH 5.0 and 65 °C. It had broad-range pH stability (retaining >65% activity after incubation at pH 3.0–8.0 at 37 °C for 24 h) and was highly thermostable (retaining >80% activity after incubation at 60 °C for 30 min). LrMan5B displayed the highest catalytic efficiency for locust bean gum and the k_cat/K_m value was 1357.47 mL·mg⁻¹·s⁻¹, followed by guar gum (512.82 mL·mg⁻¹·s⁻¹), konjac glucomannan (454.21 mL·mg⁻¹·s⁻¹), and palm kernel meal (137.00 mL·mg⁻¹·s⁻¹). In order to evaluate the synergistic effect of LrMan5B and α-galactosidase LrAgal36A from L. ramosa, LrAgal36A was supplemented to hydrolyze palm kernel meal with LrMan5B together, showing that the reducing sugar release significantly increased by 21% (compared with the sum of that by hydrolysis of single Lrman5B or LrAgal36A). Due to its favorable enzymatic properties, LrMan5B might own potential applications in the area of food and feed processing.     

Enrichment of laccase production by Phoma herbarum isolate KU4 under solid-state fermentation by optimizing RSM coefficients using genetic algorithm

The process parameters were optimized to obtain enhanced enzyme activity from the fungus Phoma herbarum isolate KU4 using rice straw and saw dust as substrate under solid-state fermentation using Response surface methodology (RSM). Genetic algorithm was used to validate the RSM for maximum laccase production. Six variables, viz., pH of the media, initial moisture content, copper sulphate concentration, concentration of tannic acid, inoculum concentration and incubation time were found to be effective and optimized for enhanced production. Maximum laccase production was achieved by RSM at pH 5·0 and 86% of initial moisture content of the culture medium, 150 µmol l⁻¹ of CuSO₄, 1·5% tannic acid and 0·128 g inoculum g⁻¹ dry substrate inoculum size on the fourth day of fermentation. The highest laccase activity was observed as 79 008 U g⁻¹, which is approximately sixfold enhanced production compared to the unoptimized condition (12 085·26 U g⁻¹).     

In vivo pharmacokinetics and in vitro production of cocaethylene in pregnant guinea pigs

Simultaneous exposure to cocaine and ethanol results in the formation of cocaethylene, an active metabolite of cocaine. The concurrent abuse of both cocaine and ethanol is common during human pregnancy, but the kinetics of elimination and formation of this ethyl ester of cocaine have not been studied during pregnancy in any species. In the late gestation guinea pig (61 to 63 days), cocaethylene, at doses of 2 to 4 mg · kg⁻¹, is rapidly eliminated with a half-life of 29 min and a total body clearance of 77 ml · min⁻¹ · kg⁻¹. It is formed enzymatically by hepatic microsomal preparations from fetal, neonatal and maternal guinea pigs. The maximum rate of cocaethylene production (apparent V_max) when either ethanol or cocaine are varied while the other substrate is held constant, increases with age, from the late fetal period (65 days gestation, term 70 days) to adulthood. However, the Michaelis-Menten constant (apparent K_M) does not change with age. The rapid elimination of cocaethylene, coupled with the slow rate of formation (apparent V_max of 140 pmol · min⁻¹ · mg microsomal protein⁻¹) and the small amount of plasma analyzed most likely explains the inability to detect cocaethylene in vivo after concomitant cocaine and ethanol administration.     

Nutritive value of deep stacked and ensiled broiler litter for sheep

Broiler litter was deep stacked and ensiled with water to achieved 40% moisture before being added, with or without 5% sugarcane molasses or with rumen contents, to a basal diet. The influence of stacking and ensiling of broiler litter on the numbers of Salmonella, Shigella, Proteus and total number of colony forming units (CFU) was investigated. Nutritive value of broiler litter processed by deep stacking and ensiling was evaluated in a digestibility trial. The experiment was conducted with 30 wethers allotted to five diets. A basal diet (20% corn grain, 23% wheat bran, 37% cotton seed cake, 18% wheat straw and 2% dicalcium phosphate) was given alone (1) or with broiler litter processed by deep stacking (2), ensiling (3), ensiling with 5% added molasses (4), or ensiling with rumen contents (1:1, wet basis) (5). For Diets 2–5, the ratio of basal diet to silage was 1:1, dry basis. For the digestion trial, diets were given at 20 g dry matter (DM) kg⁻¹ body weight per day. Initial samples of broiler litter showed 2.5 × 10⁸ CFU and Salmonella, Shigella and Proteus were present. The processes of deep stacking and ensiling were equally effective in achieving a complete elimination of all the pathogens. Apparent digestibilities of organic matter (OM) and crude protein (CP) (559.1 g kg⁻¹ and 608.7 g kg⁻¹ DM) were lower (P < 0.05) for diet 2 (deep stacked litter) than for the other waste-containing diets (OM: 578.7 g kg⁻¹, 582.9 g kg⁻¹, 594.1 g kg⁻¹; CP: 688.6 g kg⁻¹, 675.8 g kg⁻¹, 709.0 g kg⁻¹ DM, for Diets 3, 4 and 5, respectively). Among the waste-containing diets, cellulose digestibility (398.7 g kg⁻¹ DM) was higher (P < 0.05) for Diet 5 (ensiled litter-rumen contents). The results indicate that deep stacking and ensiling are equally feasible and effective for eliminating the pathogens and processed broiler litter can be incorporated in the diet of ruminants at levels of up to 50% without any adverse effect on the health of the animals.     

Cyclosporin-A production by Tolypocladium inflatum using solid state fermentation

Tolypocladium inflatum strains are known to produce Cyclosporin-A under submerged culture conditions. In the present study solid state fermentation was used to produce Cyclosporin-A. Tolypocladium inflatum strains when grown on moist wheat bran produced 310–459 mg of Cyclosporin-A kg of bran⁻¹. Tolypocladium inflatum ATCC 34921 which produced 459 mg of Cyclosporin-A kg of bran⁻¹ was improved to produce 1031±27 mg of Cyclosporin-A kg⁻¹ of bran, by subjecting the spores to different mutagenic treatments. The mutated strain, designated Tolypocladium inflatum DRCC 106, produced 4843 mg kg⁻¹ of bran under optimum fermentation conditions in 10 days when grown on wheat bran medium containing millet flour 20%, jowar flour 10%, zinc sulphate 0·15%, ferric chloride 0·25% and cobaltous chloride 0·05%. An inoculum of 60% initial moisture content 70%, initial bran pH 2·0 and incubation temperature 25°C were found to be optimal. Cyclosporin-A thus obtained was purified by solvent extraction, followed by column chromatography. The isolated product complies with the United States Pharmacopoeia specifications.     

Influence of substrate concentration and bicarbonate addition on the anaerobic digestion of an inulin-rich substrate as the ending stage in a dandelion biorefinery scheme

This study was focused on the suitability of dandelion plant as part of a biorefinery scheme in which anaerobic degradation (biomethanization) for biogas production is the ending process. Inulin as the main compound in the tuberous root was selected as substrate and tested at different concentrations (5, 10 and 15 g TS L⁻¹). The presence of bicarbonate as a buffer on anaerobic digestion was assessed as well. Methane production curves were fitted with the modified Gompertz equation. Methane production yield (Y_CH4), specific maximum methane production rate (SR_MAX) and the first-order hydrolysis constant (k_H) were affected by the substrate concentration. Bicarbonate was found not to be determinant for the overall biomethanization process because no significant effect over the Y_CH4was achieved in the presence or absence of bicarbonate; between 0.19 to 0.23 m³ kg^-1 VS added. However, k_Hand SR_MAX were affected by the presence of this inorganic compound. Without the addition of bicarbonate, k_Hand SR_MAX decreased as the TS increased. These results will be key for a dandelion biorefinery proof-of-concept under the proposed conditions.     

Tissue kallikrein processes small proenkephalin peptides

Tissue kallikrein may play a role in processing precursor polypeptide hormones. We investigated whether hydrolysis of natural enkephalin precursors, peptide F and bovine adrenal medulla docosapeptide (BAM-22P), by hog pancreatic kallikrein is consistent with this concept. Incubation of peptide F with this tissue kallikrein resulted in the release of Met⁵-enkephalin and Met⁵-Lys⁶-enkephalin. Met⁵-Lys⁶-enkephalin was the main peptide released, indicating that the major cleavage site was between two lysine residues. At 37°C and pH 8.5, the K_M values for formation of Met⁵-enkephalin and Met⁵-Lys⁶-enkephalin were 129 and 191 μM, respectively. Corresponding k_cat values were 0.001 and 0.03 s⁻¹ and k_cat/K_M ratios were 8 and 1.6·10² M⁻¹ · s⁻¹, respectively. Cleavage of peptide F at acidic pH (5.5) was negligible. When BAM-22P was used as a substrate, Met⁵-Arg⁶-enkephalin was released, thus indicating cleavage between two arginine residues. At pH 8.5, K_M was 64 μM, k_cat was 4.5 s⁻¹, and the k_cat/K_M ratio was 7 · 10⁴ M⁻¹ · s⁻¹. At 5.5, the pH of the secretory granules, K_M, k_cat and k_cat/K_M were 184 μM, 1.9 s⁻¹ and 10⁴ M⁻¹ · s⁻¹, respectively. It is unlikely that peptide F could be a substrate for kallikrein in vivo; however, tissue kallikrein could aid in processing proenkephalin precursors such as BAM-22P by cleaving Arg-Arg peptide bonds.     

Phytoremediation Potential of Selected Plants for Nitrate and Phosphorus from Ground Water

The phytoremediation potential of three aquatic plants namely, water lettuce(Pistia stratioes), water hyacinth (Eichhornia crassipes), and water spinach (Ipomoea aquatica) for nitrate N and phosphorus from nutrient treated ground water was assessed. A total of twelve treatment combinations including four levels of nitrate (expressed as nitrate N 0, 20, 40, and 60 mg/l) and three levels of phosphorus (0, 20, and 40 mg/l) were treated for the total volume of 1 and 20 liters of water respectively, for Pistia stratiotes and Eichhornia crassipes. For Ipomoea aquatica ten treatment combinations with five levels of nitrate N (0, 10, 20, 40, and 50 mg/l) and two levels of phosphorus (0 and 5 mg/l) were treated to 3 liters of water. The design used was a two factor factorial with three replicates. Water was analyzed at weekly interval for nitrate N and phosphorus. Pistia stratiotes, Eichhornia crassipes and Ipomoea aquatica had the potential to remove nitrate N between 61.5–91.8%, 40–63.5%, and 29.3–75% during the period of six, three and three and weeks, respectively. In addition, 90–99%, 75–97.2%, and 75–83.3% of phosphorus was removed from water by Pistia stratiotes, Eichhornia crassipes and Ipomoea aquatica respectively, during the same period.     

Cultivation of Lemna gibba under desert conditions. I: Twelve months of continuous cultivation in open ponds

Duckweed, Lemna gibba, was grown in 12 m² shallow ponds in the Negev desert, during 12 months of continuous cultivation, beginning April 1984. Average monthly growth rates varied with the season of the year. The lowest daily yield, 2·6±0·4 g dry weight m⁻² day⁻¹, was obtained during January. Highest daily yields, 7·9±2·6 g dry weight m⁻² day⁻¹ and 7·0±1·2 g dry weight m⁻² day⁻¹, were obtained during September and May. A 35% decline of the yield was seen during midsummer (July), 4·8±1·2 g dry weight m⁻² day⁻¹. The average rate for the year was 5·15±1·7 g dry weight m⁻² day⁻¹. The protein content of the plants ranged from 30 to 38% per unit dry weight.Growth performance is discussed in relation to the prevailing climatic conditions.     

Effects of macrophyte leachate on <Emphasis Type="Italic">Anabaena</Emphasis> sp. and <Emphasis Type="Italic">Chlamydomonas moewusii</Emphasis> growth in freshwater tropical ecosystems

This study reports on the effects of dissolved organic matter (DOM) derived from the aquatic macrophyte Pistia stratiotes (collected from a tropical reservoir) on the mixotrophic growth of two phytoplankton species (Chlamydomonas moewusii and Anabaena sp.). The DOM from P. stratiotes had a mainly aliphatic structure, low molecular weight, low cellulose and lignin content and high carbon content. The addition of DOM (5% v/v) significantly decreased the growth rate of Anabaena sp. but increased the chlorophyll a concentration of C. moewusii. Higher light intensity (100 versus 30 µmol m^?2 s^?1) was important for Anabaena sp., increasing its growth rate and chlorophyll content. The use of DOM from P. stratiotes to mitigate cyanobacterial blooms should be further explored in future studies.     

Production and purification of 2-phenylethanol by Saccharomyces cerevisiae using tobacco waste extract as a substrate

2-phenylethanol (2-PE), which is extracted naturally from plant or biotechnology processing, is widely used in the food and cosmetics industries. Due to the high cost of 2-PE production, the valorization of waste carbon to produce 2-PE has gained increasing attention. Here, 2-PE was produced by Saccharomyces cerevisiae using tobacco waste extract (TWE) as the substrate. Considering the toxicity of nicotine and its inhibition of 2-PE, the tolerance of S. cerevisiae was first evaluated. The results suggested that the production of 2-PE by S. cerevisiae in TWEs could be carried out at 2·0 mg ml⁻¹ nicotine concentrations and may be inhibited by 1·0 mg ml⁻¹ 2-PE. Thus, the compounds in the TWEs prepared at different temperatures were detected, and the results revealed that the TWEs prepared at 140°C contained 2·18 mg ml⁻¹ of nicotine, had total sugar concentrations of 26·8 mg ml⁻¹ and were suitable for 2-PE production. Due to feedback regulation, the 2-PE production was only 1·11 mg ml⁻¹, and the remaining glucose concentration remained at 13·78 mg ml⁻¹, which indicated insufficient glucose utilization. Then, in situ product recovery was further implemented to remove this inhibition; the glucose utilization (the remaining concentration decreased to 3·64 mg ml⁻¹) increased, and the 2-PE production increased to 1·65 mg ml⁻¹. The 2-PE produced in the fermentation broth was first isolated by elution from the resin with 75% ethanol and then by removing the impurities with 2·5% activated charcoal, and pure 2-PE was identified by gas chromatography mass spectrometry. The results of this study suggest that TWE could be an alternative carbon source for 2-PE production. This could provide an outlet tobacco waste as well as reducing the price of natural 2-PE, although more strategies need to be explored to improve the production yield of 2-PE by using TWE.     

Improved performance of a hybrid design over an anaerobic filter for the treatment of dairy industry wastewater at laboratory scale

A combined system designed by converting the flow mixing chamber of an anaerobic filter into an UASB resulted in an increased efficiency of removal of organic matter of 92% and in a gas production of 4.64 l·l⁻¹·d⁻¹, at the highest organic loading rate tested compared with that of the unmodified anaerobic filter. Both reactors were tested using dairy industry wastewater at identical operating conditions at 30°C and organic loading rate between 1 to 8 g COD·l⁻¹·d⁻¹.     

Influence of the concentrations of d-xylose and yeast extract on ethanol production by Pachysolen tannophilus

To determine the most favorable conditions for the production of ethanol by Pachysolen tannophilus, this yeast was grown in batch cultures with various initial concentrations of two of the constituents of the culture medium: d-xylose (s_o), ranging from 1 g·l⁻¹ to 200 g·l⁻¹, and yeast extract (l_o), ranging from 0 g·l⁻¹ to 8 g·l⁻¹. The most favorable conditions proved to be initial concentrations of S_o=25 g·l⁻¹ and l_o=4 g·l⁻¹, which gave a maximum specific growth rate of 0.26 h⁻¹, biomass productivity of 0.023 g·l⁻¹·h⁻¹, overall biomass yield of 0.094 g·g⁻¹, specific xylose-uptake rate (q_s) of 0.3 g·g⁻¹·h⁻¹ (for t=50 h), specific ethanol-production rate (q_E) of 0.065 g·g⁻¹·h⁻¹ and overall ethanol yield of 0.34 g·g⁻¹; q_s values decreased after the exponential growth phase while q_E remained practically constant.