Bacterial stress enrichment enhances anaerobic hydrogen production in cattle manure sludge

Methodology was evaluated to selectively enrich hydrogen-producing species present in biological sludge produced during organic wastewater treatment. The influence of bacterial stress enrichment on anaerobic hydrogen-producing microorganisms was investigated in batch tests using serum bottles. Enrichment conditions investigated included application of acute physical and chemical stresses: wet heat, dry heat and desiccation, use of a methanogen inhibitor, freezing and thawing, and chemical acidification with and without preacidification of the sludge at pH 3. For each enrichment sample, cultivation pH value was set at an initial value of 7. After application of selective enrichment (by bacterial stress), hydrogen production was significantly higher than that of untreated original sludge. Hydrogen production from the inocula with bacterial stress enrichment was 1.9–9.8 times greater when compared with control sludge. Chemical acidification using perchloric acid showed the best hydrogen production potential, irrespective of preacidification. Enhancement is due to the selective capture of hydrogen-producing sporeformers, which induces altered anaerobic fermentative metabolism.     

Acid–base enrichment enhances anaerobic hydrogen production process

This study offers a novel and quick enrichment technology that can be used as a preliminary method to obtain a hydrogen-producing species from the biological sludge produced by wastewater treatment. The influences of acid-base enrichment (by sludge pH adjustment) on the anaerobic hydrogen-producing micro-organisms were investigated using serum bottle assays. The enrichment pH values were controlled at 3, 4, 5, 7, 10, 11 and 12 with 1 N hydrochloric acid and 1 N sodium hydroxide. For each enrichment pH, the cultivation pH values were controlled at 5, 6 and 7. Based on the experimental results, hydrogen accumulation from sludge with acid or base enrichment is higher than that of the control. The hydrogen-production potential of the sludge with acid or base enrichment is 200 and 333 times enhanced, compared with the control, when the enrichment pH is 10 and 3, respectively. The enhancement is due to a shortening of the micro-organisms' lag-time which occurs at a proper cultivation-pH level.     

Evaluation of methods for preparing hydrogen-producing seed inocula under thermophilic condition by process performance and microbial community analysis

Five methods for preparation of hydrogen-producing seeds (base, acid, 2-bromoethanesulfonic acid (BESA), load-shock and heat shock treatments) as well as an untreated anaerobic digested sludge were compared for their hydrogen production performance and responsible microbial community structures under thermophilic condition (60 degrees C). The results showed that the load-shock treatment method was the best for enriching thermophilic hydrogen-producing seeds from mixed anaerobic cultures as it completely repressed methanogenic activity and gave the a maximum hydrogen production yield of 1.96 mol H(2) mol(-1) hexose with an hydrogen production rate of 11.2 mmol H(2) l(-1)h(-1). Load-shock and heat-shock treatments resulted in a dominance of Thermoanaerobacterium thermosaccharolyticum with acetic acid and butyric acid type of fermentation while base- and acid-treated seeds were dominated by Clostridium sp. and BESA-treated seeds were dominated by Bacillus sp. The comparative experimental results from hydrogen production performance and microbial community analysis showed that the load-shock treatment method was better than the other four methods for enriching thermophilic hydrogen-producing seeds from anaerobic digested sludge. Load-shock treated sludge was implemented in palm oil mill effluent (POME) fermentation and was found to give maximum hydrogen production rates of 13.34 mmol H(2) l(-1)h(-1) and resulted in a dominance of Thermoanaerobacterium spp. Load-shock treatment is an easy and practical method for enriching thermophilic hydrogen-producing bacteria from anaerobic digested sludge.     

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.     

Production of bio-hydrogen by mesophilic anaerobic fermentation in an acid-phase sequencing batch reactor

The pH and hydraulic retention time (HRT) of an anaerobic sequencing batch reactor (ASBR) were varied to optimize the conversion of carbohydrate-rich synthetic wastewater into bio-hydrogen. A full factorial design using evolutionary operation (EVOP) was used to determine the effect of the factors and to find the optimum condition of each factor required for high hydrogen production rate. Experimental results from 20 runs indicate that a maximum hydrogen production rate of 4,460-5,540 mL/L/day under the volumetric organic loading rate (VOLR) of 75 g-COD/L/day obtained at an observed design point of HRT = 8 h and pH = 5.7. The hydrogen production rate was strongly dependent on the HRT, and the effect was statistically significant (P < 0.05). However, no significant effect (P > 0.05) was found for the pH on the hydrogen production rate. When the ASBR conditions were set for a maximum hydrogen production rate, the hydrogen production yield and specific hydrogen production rate were 60-74 mL/g-COD and 330-360 mL/g-VSS/day, respectively. The hydrogen composition was 43-51%, and no methanogenesis was observed. Acetate, propionate, butyrate, valerate, caproate, and ethanol were major liquid intermediate metabolites during runs of this ASBR. The dominant fermentative types were butyrate-acetate or ethanol-acetate, representing the typical anaerobic pathway of Clostridium species. This hydrogen-producing ASBR had a higher hydrogen production rate, compared with that produced using continuous-flow stirred tank reactors (CSTRs). This study suggests that the hydrogen-producing ASBR is a promising bio-system for prolonged and stable hydrogen production.     

Hydrogen production of a salt tolerant strain Bacillus sp. B2 from marine intertidal sludge

To isolate a salt tolerant hydrogen-producing bacterium, we used the sludge from the intertidal zone of a bathing beach in Tianjin as inoculum to enrich hydrogen-producing bacteria. The sludge was treated by heat-shock pretreatment with three different temperature (80, 100 and 121°C) respectively. A hydrogen-producing bacterium was isolated from the sludge pretreated at 80°C by sandwich plate technique and identified using microscopic examination and 16S rDNA gene sequence analysis. The isolated bacterium was named as Bacillus sp. B2. The present study examined the hydrogen-producing ability of Bacillus sp. B2. The strain was able to produce hydrogen over a wide range of initial pH from 5.0 to 10.0, with an optimum at pH 7.0. The level of hydrogen production was also affected by the salt concentration. Strain B2 has unique capability to adapt high salt concentration. It could produce hydrogen at the salt concentration from 4 to 60‰. The maximum of hydrogen-producing yield of strain B2 was 1.65 ± 0.04 mol H₂/mol glucose (mean ± SE) at an initial pH value of 7.0 in marine culture conditions. Hydrogen production under fresh culture conditions reached a higher level than that in marine ones. As a result, it is likely that Bacillus sp. B2 could be applied to biohydrogen production using both marine and fresh organic waste.     

Microbial Consortia for Hydrogen Production Enhancement

Ten efficient hydrogen-producing strains affiliated to the Clostridium genus were used to develop consortia for hydrogen production. In order to determine their saccharolytic and proteolytic activities, glucose and meat extract were tested as fermentation substrates, and the best hydrogen-producing strains were selected. The C. roseum H5 (glucose-consuming) and C. butyricum R4 (protein-degrading) co-culture was the best hydrogen-producing co-culture. The end-fermentation products for the axenic cultures and co-cultures were analyzed. In all cases, organic acids, mainly butyrate and acetate, were produced lowering the pH and thus inhibiting further hydrogen production. In order to replace the need for reducing agents for the anaerobic growth of clostridia, a microbial consortium including Clostridium spp. and an oxygen-consuming microorganism able to form dense granules (Streptomyces sp.) was created. Increased yields of hydrogen were achieved. The effect of adding a butyrate-degrading bacteria and an acetate-consuming archaea to the consortia was also studied.     

Dynamics of hydrogen-producing bacteria in a repeated batch fermentation process using lake sediment as inoculum

In this study, we evaluated the effectiveness of lake sediment as inoculum for hydrogen production through dark fermentation in a repeated batch process. In addition, we investigated the effect of heat treatment, applied to enrich hydrogen-producing bacteria, on the bacterial composition and metabolism. Denaturing gradient gel electrophoresis and molecular cloning, both performed using the 16S rDNA gene as target gene, were used to monitor the structure of the bacterial community. Hydrogen production and bacterial metabolism were analysed via gas chromatography and high-performance liquid chromatography. Both treated and non-treated inocula were able to produce high amounts of hydrogen. However, statistical analysis showed a clear difference in their bacterial composition and metabolism. The heat treatment favoured the growth of different Clostridia sp., in particular of Clostridium bifermentans, allowing the production of a constant amount of hydrogen over prolonged time. These cultures showed both butyrate and ethanol fermentation types. Absence of heat treatment allowed species belonging to the genera Bacillus, Sporolactobacillus and Massilia to outgrow Clostridia sp. with a reduction in hydrogen production and a significant metabolic change. Our data indicate that lake sediment harbours bacteria that can efficiently produce hydrogen over prolonged fermentation time. Moreover, we could show that the heat treatment stabilizes the bacterial community composition and the hydrogen production.     

光合菌生物制氢技术

简要分析了光合细菌产氢的主要影响因素,介绍了国内外光合细菌生物制氢技术的研究和应用现状,并对光合制氢技术的发展趋势和应用前景进行了评述。     

Characterization of a hydrogen-producing granular sludge

This study demonstrated that hydrogen-producing acidogenic sludge could agglutinate into granules in a well-mixed reactor treating a synthetic sucrose-containing wastewater at 26 degrees C, pH 5.5, with 6 h of hydraulic retention. A typical matured granule is 1.6 mm in diameter, 1.038 g/mL in density, 11% in ash content, and over 50 m/h in settling velocity. Treating a solution containing 12.15 g/L of sucrose at a volumetric loading rate of 48.6 g/(L x d), the reactor containing 20 g/L of granular sludge degraded 97% of sucrose. Effluent comprised 46% acetate and 49% butyrate and the methane-free biogas comprised 63% hydrogen, 35% carbon dioxide, and 2% nitrogen. Hydrogen production rate was 13.0 L/(L x d), and the yield was 0.28 L/g-sucrose. The granule had multiple cracks on the surface and comprised two morphological types of bacteria: fusiform bacilli and a spore-forming bacterium. Phylogenetic analysis showed that 69.1% of the clones were affiliated with four Clostridium species in the family Clostridiaceae, and 13.5% with Sporolactobacillus racemicus in the Bacillus/Staphylococcus group.     

Metabolic pathways of hydrogen production in fermentative acidogenic microflora

Biohydrogen production from organic wastewater by anaerobically activated sludge fermentation has already been extensively investigated, and it is known that hydrogen can be produced by glucose fermentation through three metabolic pathways, including the oxidative decarboxylation of pyruvic acid to acetyl-CoA, oxidation of NADH to NAD+, and acetogenesis by hydrogen-producing acetogens. However, the exact or dominant pathways of hydrogen production in the anaerobically activated sludge fermentation process have not yet been identified. Thus, a continuous stirred-tank reactor (CSTR) was introduced and a specifically acclimated acidogenic fermentative microflora obtained under certain operation conditions. The hydrogen production activity and potential hydrogen-producing pathways in the acidogenic fermentative microflora were then investigated using batch cultures in Erlenmeyer flasks with a working volume of 500 ml. Based on an initial glucose concentration of 10 g/l, pH 6.0, and a biomass of 1.01 g/l of a mixed liquid volatile suspended solid (MLVSS), 247.7 ml of hydrogen was obtained after a 68 h cultivation period at 35 +/- 1 degrees C. Further tests indicated that 69% of the hydrogen was produced from the oxidative decarboxylation of pyruvic acid, whereas the remaining 31% was from the oxidation of NADH to NAD+. There were no hydrogen-producing acetogens or they were unable to work effectively in the anaerobically activated sludge with a hydraulic retention time (HRT) of less than 8 h.     

Effects of acid pre-treatment on bio-hydrogen production and microbial communities during dark fermentation

Optimal conditions for acid pre-treatment were investigated for the enrichment of hydrogen-producing bacteria (HPB) in a mixed culture using three strong acids: HCl, HNO(3), and H2SO4 x HCl was selected as a suitable acid for the enrichment of HPB in the fermentation process. The volume of bio-hydrogen produced when the mixed culture was pre-treated using HCl at pH 2 was 3.2 times higher than that obtained without acid pre-treatment. Changes in the microbial community during acid pre-treatment were monitored using images obtained by the fluorescent in situ hybridization (FISH) method and the Live/Dead cell viability test. The tests clearly indicated that the Clostridium species of cluster I were the predominant strains involved in bio-H(2) fermentation, and could be selectively enriched by HCl pre-treatment.     

光合细菌与产气肠杆菌协同产氢特性分析

对光合细菌(Rhodopseudomonas sp. DT)与产气肠杆菌(Enterobacter aerogenes)进行了发酵产氢试验, 考察了不同起始接种比例、培养温度及碳源条件下混合菌协同产氢特性。结果表明: 光合细菌与产气肠杆菌初始接种比例对协同产氢影响较大, 初始接种比例为1:1最有利于协同产氢, 产氢效率和产氢周期达到了3.1 mol H2/mol葡萄糖及81 h。进一步培养液pH动力学变化研究发现初始接种比例为1:1的混合菌培养液pH变化较小, 为pH 6~7, 利于混合菌协同产氢。28°     

A dual-substrate steady-state model for biological hydrogen production in an anaerobic hydrogen fermentation process

Biological hydrogen production from anaerobic waste fermentation possesses potential benefits in simultaneously reducing organic wastes and generating sustainable energy sources. Three kinetic-based steady-state models for anaerobic fermentation of multiple substrates, including glucose and peptone, were evaluated. Experimental results obtained from a continuous stirred tank reactor (CSTR) were primarily used for model evaluation. The dual-substrate steady-state model developed and the associated kinetic parameters estimated in this study successfully described the anaerobic growth of hydrogen-producing bacteria. The model was able to capture the general trends of consumption of substrates and accumulation of products, including formate, acetate, butyrate, and hydrogen, at dilution rates (D) between 0.06 and 0.69/h. According to the model, the adverse effects of endogeneous and peptone metabolism on net hydrogen production can be minimized by increasing D. For the operational conditions of D > 0.69/h, however, substantial washout of hydrogen-producing bacteria from the CSTR was observed, and it resulted in a rapid drop in hydrogen production rate as well.     

高效产氢细菌新种--Ethanologenbacterium sp.X-1的分离鉴定及其产氢效能

为获得高效产氢发酵细菌 ,采用改进的厌氧Hungate培养技术 ,从生物制氢反应器CSTR中分离一株产氢细菌X 1。对该株细菌进行了形态学特征、生理生化指标、16SrDNA和 16S 2 3SrDNA间隔区序列分析等研究。结果表明与最相近的种属Clostridiumcellulosi和Acetanaerobacteriumelongatum等的 16SrRNA基因序列同源性为 94 %以下。16S 2 3SrRNA间隔区基因序列比对分析显示保守区域仅为tRNAAla和tRNAIle序列 ,其它可变部位没有同源性区域 ,鉴定为新属Ethanologenbacteriumsp .。该株细菌为专性厌氧杆菌 ,代谢特征为乙醇发酵 ,葡萄糖发酵产物主要为乙醇、乙酸、H2 和CO2 。在pH4 0和 36℃条件下最大产氢速率是 2 8 3mmolH2 (gdrycell·h)。经鉴定和产氢效能分析表明该菌株是一新属的高效产氢细菌     

正交实验优选光合细菌混合菌群产氢的最佳条件

对光合细菌混合菌群产氢影响因子进行了实验研究。通过单因素实验和正交实验, 系统考察了碳源、氮源、碳源浓度、氮源浓度、初始pH值、光照方式、接种量等因素对产氢量的影响, 实验得出最佳工艺条件为: 采用3号菌群, 碳源为葡萄糖, 碳源浓度为3 g/L, 氮源为尿素, 氮源浓度为9 g/L, 接种量为10%, pH值为8.5, 光照方式为12 h光照-12 h黑暗交替光照, 培养温度为30°C。菌种、碳源、碳源浓度、氮源是影响产氢量的重要因素。     

Ethanol utilization by sulfate-reducing bacteria: an experimental and modeling study

A mixed culture of sulfate-reducing bacteria containing the species Desulfovibrio desulfuricans was used to study sulfate-reduction stoichiometry and kinetics using ethanol as the carbon source. Growth yield was lower, and kinetics were slower, for ethanol compared to lactate. Ethanol was converted into acetate and no significant carbon dioxide production was observed. A mathematical model for growth of sulfate-reducing bacteria on ethanol was developed, and simulations of the growth experiments on ethanol were carried out using the model. The pH variation due to sulfate reduction, and hydrogen sulfide production and removal by nitrogen sparging, were examined. The modeling study is distinct from earlier models for systems using sulfate-reducing bacteria in that it considers growth on ethanol, and analyzes pH variations due to the product-formation reactions.     

Influence of Sulfate-Reducing Bacteria on Outdoor Hydrogen Production by Photosynthetic Bacterium with Seawater

The application of seawater for bacterial fermentative production is a cost-effective technology. Hydrogen production by marine photosynthetic bacterium with seawater failed to continue after more than 10 days, and was accompanied by the formation of hydrogen sulfide and a change in culture color from red to black. However, substrate consumption in the blackish culture was comparable to that in a hydrogen-producing culture. A decrease in hydrogen production occurred upon the addition of sodium sulfide at concentrations of 1.5 mM or higher. PCR analysis targeted at the 16S rDNA sequence selective for sulfate-reducing bacteria revealed the existence of sulfate-reducing bacteria in inoculation cultures of the phototrophic bacterium and medium for hydrogen production. Hence, the high sulfate concentration of seawater, the low oxidation-reduction potential under hydrogen-producing conditions, and the presence of electron donors such as acetate might promote the metabolic activities of sulfate-reducing bacteria, resulting in the deterioration of hydrogen production with seawater. Received: 15 September 1999 / Accepted: 14 October 1999     

发酵生物制氢研究进展

综述了近年来发酵生物制氢领域的研究进展?在菌种方面,除了对现有产氢菌种的深入研究外,还采用生物学,分子生物学及生物信息学手段建立产氢菌种库;在氢酶的研究方面,已逐步从基因确定、功能研究拓展到基因工程构建高效产氢菌研究：而在与废弃生物质处理相结合的反应过程方面,研究主要集中在利用不同种类的废弃物的产氢和高效产氢反应器上。此外,还初步总结了目前对发酵制氢可行性和经济性的评价,并对其发展方向提出了新的看法。     

沼泽红假单胞菌乙酸光合放氢研究

依据光合细菌生长代谢特性和有机废水降解主要产物类型,11种有机物被用于沼泽红假单胞菌（Rhodopseudomonas palustris）Z菌株的光合产氢研究,其中,乙酸反应体系产氢活性最高。在此基础上,研究了该菌株的生长与产氢动力学行为,探求了影响该菌株光合放氢的主要限制性影响因素。结果表明,该菌株产氢与生长部分相关。种子培养基和菌龄对产氢活性有明显影响。细胞最适产氢和生长所需要的光照强度和温度基本一致。当种子来源于硫酸铵高菌龄预培养物或谷氨酸钠对数期预培养物时,该菌株产氢活性显著增加,产氢延滞期明显缩短。氧浓度和接种量对产氢活性也有显著影响。供氢体和氮源浓度直接决定细胞的生长与光放氢活性。在低于70 mmol/L乙酸钠和15 mmol/L谷氨酸钠时,产氢活性随底物浓度的增加而增强。谷氨酸钠浓度高于15mmol/L时,由于游离NH₄⁺的出现,产氢活性受到抑制,但却明显刺激细胞的生长。在标准状况下,该菌株的最大产氢速率可达19.4 mL·L^-1·h^-1。