Effects of temperature and initial pH on biohydrogen production from food-processing wastewater using anaerobic mixed cultures

This study attempted to determine the optimal temperature and initial cultivation pH by conducting a series of batch tests in stirred-tank bioreactor using fructose-producing wastewater as an organic substrate. The bioreactor temperature was controlled at 35–55°C with an initial pH of 4–8. Hydrogen production efficiency was assessed using specific hydrogen production potential (SHPP) and the maximum specific hydrogen production rate (SHPR_m). Experimental results indicated that temperature and initial pH markedly affected SHPP and SHPR_m, volatile fatty acids distribution as well as the ratio of butyrate/acetate (BHu/HAc). Two-fold higher SHPP and SHPR_m were obtained at thermophilic condition (55°C) than those at mesophilic condition (35°C). The optimal initial pH was 6 for hydrogen production with peak values of SHPP of 166.8 ml-H₂/g-COD and SHPR_m of 26.7 ml-H₂/g-VSS-h for fructose-processing wastewater. Molasses-processing wastewater had a higher SHPP (187.0 ml-H₂/g-COD) and SHPR_m (42.7 ml-H₂/gVSS-h) than fructose-processing wastewater at pH 6. The DGGE profiles indicated that molasses-processing wastewater is a better substrate than fructose-processing wastewater for growth of hydrogen-producing bacteria due to the high staining intensity of bands.     

Exploitation of olive oil mill wastewater for combined biohydrogen and biopolymers production

The present study aimed to the investigation of the feasibility of the combined biohydrogen and biopolymers production from OMW (Olive oil Mill Wastewater), using a two stage system. H₂ and volatile fatty acids (VFAs) were produced via anaerobic fermentation and subsequently the acidified wastewater was used as substrate for aerobic biodegradable polymer production. Two different bioreactors, one of CSTR type and a SBR were used for the anaerobic and the aerobic process respectively. The anaerobic reactor was operated at different hydraulic retention times (HRTs) with OMW, diluted 1:4 (v/v) with tap water, as feed. The main VFAs produced were acetate, butyrate and propionate, in different ratios depending on the HRT. Valerate, isovalerate and isobutyrate were also detected in small quantities. Selective effluents of the acidogenic/hydrogen producing reactor were subsequently used as feed for the aerobic reactor. The aerobic reactor was inoculated with an enriched PHAs producing bacteria culture, and was operated in sequential cycles of nitrogen offer (growth phase) and nitrogen limitation (PHAs accumulation phase). The operational program of the SBR was determined according to the results from batch test, and its performance was evaluated for a period of 100 days. During the accumulation phase butyrate was consumed preferably, indicating that the dominant PHA produced is polyhydroxybutyrate. The higher yield of PHAs observed was 8.94% (w/w) of dry biomass weight.     

Improvement of biohydrogen production by Enterobacter cloacae IIT-BT 08 under regulated pH

The present study investigates the effect of pH and intermediate products formation on biological hydrogen production using Enterobacter cloacae IIT-BT 08. Initial pH was found to have a profound effect on hydrogen production potential, while regulating the pH 6.5 throughout the fermentation was found to increase the cumulative hydrogen production rate and yield significantly. Modified Gompertz equation was used to fit the cumulative hydrogen production curves to obtain the hydrogen production potential P, the hydrogen production rate R and lag phase λ. At regulated pH 6.5, higher H(2) yield (3.1molH(2)mol(-1) glucose), specific hydrogen production potential (798.1mL/g) and specific rate of H(2) production (72.1mLL(-1)h(-1)g(-1)) were obtained. The volatile fatty acid profile showed butyrate, ethanol and acetate as the major end metabolites of fermentation under the operating pH conditions tested; however, their pattern of distribution was pH dependent. At the optimum pH of 6.5, the acetate to butyrate ratio (A/B ratio) was found to be higher than that at any other pH. The study also investigates the effect of sodium ions on biohydrogen production potential. It was also found that sodium ion concentration up to 250mM enhanced the hydrogen production potential; however, any further increase in the metal ion concentration had an inhibitory effect.     

Continuous production of non-alcohol beer by immobilized yeast at low temperature

Summary A system for production of non-alcohol beer is described. A limited fermentation is carried out with immobilized cells ofSaccharomyces cerevisiae in a packed bed reactor. In the reactor, combined stress factors such as low temperature (2–4°C) and anaerobic conditions limit cell metabolism. Of the available sugars only a small amount of glucose is metabolized, resulting in low concentrations of ethanol (<0.08%). The absence of oxygen affects the redox balance of the yeast cell, and thus stimulates formation of esters and higher alcohols. Products are formed by reduction of wort aldehydes, as well as reduction of intracellular metabolites. Despite the stress conditions, biomass increases during prolonged production periods. In batch experiments,S. cerevisiae strain W34 grows at low temperatures and a mininum growth temperature of –2 °C was found, indicating that a further reduction of temperature during production will not inhibit growth. The characteristics of the system allow its use in very different applications. Potential applications of the immobilized system are discussed.This paper is dedicated to Professor Herman Jan Phaff in honor of his 50 years of active research which still continues.     

Thermophilic biohydrogen production from glucose with trickling biofilter

Thermophilic H2 production from glucose was studied at 55-64 degrees C for 234 days using a continuous trickling biofilter reactor (TBR) packed with a fibrous support matrix. Important parameters investigated included pH, temperature, hydraulic retention time (HRT), and glucose concentration in the feed. The optimal pH and temperature were 5.5 and 60 degrees C, respectively. With decreasing HRT or increasing inlet glucose concentration, volumetric H2 production rate increased but the H2 production yield to glucose decreased gradually. The biogas composition was almost constant at 53 +/- 4% (v/v) of H2 and 47 +/- 4% (v/v) of CO2. No appreciable CH4 was detected when the reactor was under a normal operation. The carbon mass balance showed that, in addition to cell mass, lactate, n-butyrate, CO2, and acetate were major products that comprised more than 85% of the carbon consumed. The maximal volumetric H2 production rate and H2 yield to glucose were 1,050 +/- 63 mmol H2/l.d and 1.11 +/- 0.12 mol H2/mol glucose, respectively. These results indicate that the thermophilic TBR is superior to most suspended or immobilized reactor systems reported thus far. This is the first report on continuous H2 production by a thermophilic TBR system.     

Engineering of unconventional yeast Yarrowia lipolytica for efficient succinic acid production from glycerol at low pH

Yarrowia lipolytica is considered as a potential candidate for succinic acid production because of its innate ability to accumulate citric acid cycle intermediates and its tolerance to acidic pH. Previously, a succinate-production strain was obtained through the deletion of succinate dehydrogenase subunit encoding gene Ylsdh5. However, the accumulation of by-product acetate limited further improvement of succinate production. Meanwhile, additional pH adjustment procedure increased the downstream cost in industrial application. In this study, we identified for the first time that acetic acid overflow is caused by CoA-transfer reaction from acetyl-CoA to succinate in mitochondria rather than pyruvate decarboxylation reaction in SDH negative Y. lipolytica. The deletion of CoA-transferase gene Ylach eliminated acetic acid formation and improved succinic acid production and the cell growth. We then analyzed the effect of overexpressing the key enzymes of oxidative TCA, reductive carboxylation and glyoxylate bypass on succinic acid yield and by-products formation. The best strain with phosphoenolpyruvate carboxykinase (ScPCK) from Saccharomyces cerevisiae and endogenous succinyl-CoA synthase beta subunit (YlSCS2) overexpression improved succinic acid titer by 4.3-fold. In fed-batch fermentation, this strain produced 110.7 g/L succinic acid with a yield of 0.53 g/g glycerol without pH control. This is the highest succinic acid titer achieved at low pH by yeast reported worldwide, to date, using defined media. This study not only revealed the mechanism of acetic acid overflow in SDH negative Y. lipolytica, but it also reported the development of an efficient succinic acid production strain with great industrial prospects.     

Continuous electricity production from artificial wastewater using a mediator-less microbial fuel cell

A microbial fuel cell (MFC) was optimized in terms of MFC design factors and operational parameters for continuous electricity production using artificial wastewater (AW). The performance of MFC was analyzed through the polarization curve method under different conditions using a mediator-less MFC. The highest power density of 0.56 W/m2 was achieved with AW of 300 mg/l fed at the rate of 0.53 ml/min at 35 degrees C. The power per unit cell working volume was 102 mW/l, which was over 60 times higher than those reported in the previous mediator-less MFCs which did not use a cathode or an anode mediator. The power could be stably generated over 2 years.     

Acetone-butanol production by Clostridium acetobutylicum in an ammonium-limited chemostat at low pH values

Clostridium acetobutylicum was grown in continuous culture under ammonium limitation (15.15 mM NH₄ ⁺). At a pH of 6.0 and at various dilution rates only acetate, butyrate and ethanol were formed as non-gaseous products. A decrease of the pH to values between 5.2 and 4.3 resulted in a shift of the fermentation towards acetone-butanol formation.     

Damage to Streptococcus lactis resulting from growth at low pH

Harvey, R. J. (The Dairy Research Institute, Palmerston North, New Zealand). Damage to Streptococcus lactis resulting from growth at low pH. J. Bacteriol. 90:1330-1336. 1965.-Growth of Streptococcus lactis below pH 5.0 results in damage to the cells. A period of growth below pH 5.0 is required before this damage is expressed, and a period of growth above pH 5.0 is required to correct the damage. Part of the damage consists of a reduction in the specific activities of a number of enzymes. At the same time, the differential rate of total protein synthesis is unchanged. During recovery from growth at low pH, the enzymes subject to damage are formed at a differential rate which is higher than normal until the normal specific activities are restored. The growth rate characteristic of the new pH is then resumed. The results are consistent with either of two mechanisms of damage. Growth at low pH could result either in direct inactivation of a number of enzymes, or in loss of control of the differential rates of synthesis of individual enzymes.     

Submersed macrophyte growth at low pH

Summary Vallisneria americana was grown for six weeks in a greenhouse on relatively fertile sediment to test for factors other than nutrient limitation which may slow growth of this submersed macrophyte at pH 5. On the basis of dry mass accumulated, (1) low pH significantly depressed Vallisneria growth at constant free CO₂ levels; (2) free CO₂ enrichment, however, greatly stimulated Vallisneria growth at pH 5, by 2.8-fold and 10-fold at 3.2 times and 10 times air-equilibrated CO₂ levels, respectively; and (3) growth was greater by far at pH 5 than at higher pH with constant total dissolved inorganic carbon (DIC). Free CO₂ availability was thus an important controller of growth at low pH by Vallisneria americana on fertile sediment, and low pH was not directly deleterious. Field surveys of acidic lakes in the Adirondack Mountains of New York state revealed that DIC levels in low pH lakes were often well above equilibrium values and could potentially support vigorous macrophyte growth. Aluminum and/or iron toxicity did not appear to impair growth at low pH, and aluminum concentrations in Vallisneria shoots significantly decreased with increasing free CO₂ concentrations at pH 5.0, perhaps due to growth dilution. Rosette production (a measure of asexual reproduction), maximum leaf length, and extent of flowering within treatments were positively correlated with plant biomass, rather than with pH or free CO₂ levels per se.     

Buffer-anion-dependent Ca2+ leaching from horseradish peroxidase at low pH

Despite highly conserved active-site structures, members of the plant peroxidase superfamily exhibit a wide range of pH optima. Horseradish peroxidase isozyme C (HRPC) is an ideal peroxidase to investigate the structural determinants of pH stability and activity in superfamily members. Conflicting reports exist on the low-pH stability of HRPC and consequently the pKa of the catalytic distal histidine, which is neutral in active peroxidases. Towards resolving such discrepancies, acid-induced changes in HRPC from two popular commercial suppliers were systematically analyzed. Specifically, FTIR v(CO) and Soret-CD spectra of HRPC-CO and Soret absorption of ferric HRPC were recorded to probe time-dependent heme-pocket changes at pH 3.0 in phosphate, citrate and formate buffers, while the FTIR amide I' and far-UV CD spectra were examined to probe changes in secondary structure. Both HRPC-CO samples exhibited identical pH 7.0 v(CO) bands at 1934 and 1905 cm-1. In the pH 3.0 spectrum of sample A, the 1934 cm-1 band was dominant while a broad 1969 cm-1 band appeared in sample B. The intensity of this band, which is assigned to solvent-exposed heme, was greater in citrate than phosphate buffer, but in formate the 1934 cm-1 band remained dominant. Other spectral changes mirrored the v(CO) trends. No time- or buffer-anion-dependent conformation changes were detected in 1 mM CaCl2, revealing that buffer-anion-dependent leaching of stabilizing Ca2+ from HRPC occurs at pH 3.0. Since the N-glycans present in HRPC are of the flexible protein-surface-shielding type, the variation in low-pH conformational stability of the HRPC samples could be attributed to heterogeneous glycosylation, which was detected by SDS-PAGE. It is further proposed that glycosylation patterns may affect the low-pH stability of class II and III plant peroxidases.     

Bioenergy production from waste: examples of biomethane and biohydrogen

This new century addresses several environmental challenges among which distribution of drinking water, global warming and availability of novel renewable energy sources to substitute for fossil fuels are of utmost importance. The last two concerns are closely related because the major part of carbon dioxide (CO(2)), considered as the main cause of the greenhouse effect, is widely produced from fossil fuel combustion. Renewable energy sources fully balanced in CO(2) are therefore of special interest, especially the issue of biological production from organic wastes. Among the possibilities of bioenergy production from wastes, two approaches are particularly interesting: The first one is relatively old and related to the production of biomethane by anaerobic digestion while the second one, more recent and innovative, relies on biohydrogen production by microbial ecosystems.     

Comparison of various pretreatment methods for biohydrogen production from cornstalk

To establish high-efficiency pretreatments of cornstalk (CS) for hydrogen fermentative production, various pretreatment strategies have been investigated and contrasted in this work. Five pretreatment methods, including acid-soaking pretreatment, base-soaking pretreatment, high-temperature-assisted acid pretreatment, high-temperature-assisted base pretreatment and ultrasonic-assisted acid pretreatment (UAP), were performed on CS. The results showed that UAP significantly promoted the hydrogen production by CS compared with other pretreatments. The optimum UAP process, pretreating substrate with ultrasonication in 2.0% sulfuric acid solution for 1.5 h at the liquid-solid ratio of 20:1, obtained the maximum specific hydrogen accumulation of 142.59 mL g(-1)-CS and an average hydrogen production rate of 17.03 mL g(-1)-CS h(-1). Furthermore, the scanning electron microscope analysis of CS samples supports the hydrogen production results as well. The present work demonstrates that UAP is an efficient and practical CS pretreatment for hydrogen production from agricultural waste straws.     

Biomethanation of low pH petrochemical wastewater using up-flow fixed-film anaerobic bioreactors

Anaerobic digestion of wastewater from a petrochemical plant, manufacturing Nylon-6 was studied in continuously fed up-flow fixed-film column reactors using different biomass support materials such as bonechar, charcoal, bricks, plastic beads and polyurethane foam under varying hydraulic and organic loading rates. Experimental results showed bonechar as the best support material with high biomass-retaining capacity because of its high specific surface area (53.35m²g^–1 of bedding material) and pore specific volume (0.244cm³g^–1 of bedding material). This system could treat waste water at hydraulic retention times (HRT) as low as 2.5 days with organic loading rates as high as 21.76kg COD m^–3 day^–1 using acidic feed of pH 2.5 resulting in a 95% COD reduction with biogas production of 11.76m³ m^–3 of reactor volume day^–1. Total alkalinity of 1700mg CaCO₃ l^–1 and pH of 7.5 of the treated wastewater were observed at 2.5 days HRT, indicating that methanogenesis appear to be alkalizing step and wastewater with pH as low as 2.5 can be treated as such without neutralization with retention of methanogenic biomass on bonechar.     

Reduction of dehydroascorbic acid at low pH

Ascorbic acid and dehydroascorbic acid are unstable in aqueous solution in the presence of copper and iron ions, causing problems in the routine analysis of vitamin C. Their stability can be improved by lowering the pH below 2, preferably with metaphosphoric acid. Dehydroascorbic acid, an oxidised form of vitamin C, gives a relatively low response on the majority of chromatographic detectors, and is therefore routinely determined as the increase of ascorbic acid formed after reduction. The reduction step is routinely performed at a pH that is suboptimal for the stability of both forms. In this paper, the reduction of dehydroascorbic acid with tris-[2-carboxyethyl] phosphine (TCEP) at pH below 2 is evaluated. Dehydroascorbic acid is fully reduced with TCEP in metaphosphoric acid in less than 20 min, and yields of ascorbic acid are the same as at higher pH. TCEP and ascorbic acid formed by reduction, are more stable in metaphosphoric acid than in acetate or citrate buffers at pH 5, in the presence of redox active copper ions. The simple experimental procedure and low probability of artefacts are major benefits of this method, over those currently applied in a routine assay of vitamin C, performed on large number of samples.     

Microbial sulphate reduction at a low pH

It is now well established that microbial sulphate-reduction can proceed in environments with a pH<5. This review summarizes existing reports on sulphate reduction at low pH and discusses possible pH effects on sulphate-reducing bacteria. Microbial sulphate reduction has been observed in acidic lakes, wetlands, mesocosms, acidic sulphate soils and bioreactors. Possible inhibitory factors include the metabolites H(2)S and organic acids, which can be toxic depending on pH. Metal sulphide precipitation and competition with other bacteria, namely iron-reducing bacteria, can inhibit sulphate reduction. Theoretical considerations show that normal sulphate reduction rates are too low to maintain a neutral micro niche in an acidic environment. The first acidotolerant sulphate-reducing bacteria have been isolated recently.     

Reduction of dehydroascorbic acid at low pH

Ascorbic acid and dehydroascorbic acid are unstable in aqueous solution in the presence of copper and iron ions, causing problems in the routine analysis of vitamin C. Their stability can be improved by lowering the pH below 2, preferably with metaphosphoric acid. Dehydroascorbic acid, an oxidised form of vitamin C, gives a relatively low response on the majority of chromatographic detectors, and is therefore routinely determined as the increase of ascorbic acid formed after reduction. The reduction step is routinely performed at a pH that is suboptimal for the stability of both forms. In this paper, the reduction of dehydroascorbic acid with tris-[2-carboxyethyl] phosphine (TCEP) at pH below 2 is evaluated. Dehydroascorbic acid is fully reduced with TCEP in metaphosphoric acid in less than 20 min, and yields of ascorbic acid are the same as at higher pH. TCEP and ascorbic acid formed by reduction, are more stable in metaphosphoric acid than in acetate or citrate buffers at pH 5, in the presence of redox active copper ions. The simple experimental procedure and low probability of artefacts are major benefits of this method, over those currently applied in a routine assay of vitamin C, performed on large number of samples.