Feasibility of hydrogen production in thermophilic mixed fermentation by natural anaerobes

The biological sludge from an animal wastewater treatment plant was treated to enrich hydrogen-producing mixed bacteria, and effects on hydrogen yield were investigated during anaerobic fermentation at 55 degrees C. Enrichment of hydrogen-producing bacteria was conducted at pH adjustment of inocula to 3 and 5 with and without additional heat treatment (NHT and HT). The enriched mixed bacteria were cultivated at initial pHs of 5, 6, and 7 with synthetic organic wastewater containing different levels of nitrogen (2.0 and 0.8 g/l as total nitrogen) under static batch conditions. The main effects of heat treatment and enrichment pH were significant on hydrogen production. There was no significant effect of different nitrogen concentrations on hydrogen production. The methane-free biogas contained hydrogen levels of up to 64% for a fermentative condition that showed maximum hydrogen evolution (at culture pH 5 after enrichment at pH 5 with HT). The dominating intermediate metabolites were acetate, n-butyrate, and ethanol. Yields of produced hydrogen were significantly dependent upon levels of n-butyrate.     

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.     

Changes in bacterial community during fermentative hydrogen and acid production from organic waste by thermophilic anaerobic microflora

AIMS: Changes in fermentation pattern during the treatment of organic wastes containing solid materials by thermophilic anaerobic microflora were investigated with respect to product formation and bacterial community structure during hydrogen production. METHODS AND RESULTS: Anaerobic microflora enriched from sludge compost was cultivated using artificial garbage slurry in a continuous flow-stirred tank reactor. Product formation varied depending on pH and hydraulic retention time (HRT) applied. Community analysis by terminal restriction fragment length polymorphism and clone library analysis of polymerase chain reaction-amplified bacterial 16S rDNA indicated that difference in the fermentative product distribution could be caused by different populations of micro-organisms in the microflora. CONCLUSION: Hydrogen fermentation with acetate/butyrate formation was optimized at <1.0 d HRT at pH 5.0 and 6.0. Thermoanaerobacterium thermosaccharolyticum was the dominant hydrogen-producing micro-organism. Conversely, unidentified organisms became dominant after 4.0 d HRT at pH 7.0 and 8.0, where relatively high-solubilization efficiency of solid materials was observed with no production of hydrogen. SIGNIFICANCE AND IMPACT OF THE STUDY: This is the first report describing product formation in the fermentation of solid organic wastes by a mixed population of micro-organisms. Various fermentation patterns including hydrogen fermentation were characterized and evaluated from engineering and microbial aspects.     

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.     

Modeling and optimization of anaerobic digested sludge converting starch to hydrogen

The pH and hydraulic retention time (HRT) of a chemostat reactor were varied according to a central composite design methodology with the aim of modeling and optimizing the conversion of starch into hydrogen by microorganisms in an anaerobic digested sludge. Experimental results from 23 runs indicate that a maximum hydrogen production rate of 1600 L/m(3)/d under the organic loading rate of 6 kg starch m(3)/d obtained at pH = 5.2 and HRT = 17 h. Throughout this study, the hydrogen percentage in the biogas was approximately 60% and no methanogenesis was observed. while the reactor was operated with HRT of 17 h, hydrogen was produced within a pH range between 4.7 and 5.7. Alcohol production rate was greater than hydrogen production rate if the pH was lower than 4.3 or higher than 6.1. Supplementary experiments confirm that the optimum conditions evaluated in this study were highly reliable; while a hydrogen production yield of 1.29 l H(2)/g starch-COD was obtained. An examination of the response surfaces, including hydrogen, volatile fatty acids (VFA) and alcohols production, led us to the belief that clostridium sp. predominated in the anaerobic hydrogen-producing microorganisms in this study. Experiment results obtained emphasize that the response of metabolites was a more useful indicator than hydrogenic activity for obtaining efficient hydrogen production. Furthermore, expressions of contour plots indicate that Response-Surface Methodology may provide easily interpretable advice on the operation of a hydrogen-producing bioprocess.     

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.     

Evaluation of pretreatment methods on mixed inoculum for both batch and continuous thermophilic biohydrogen production from cassava stillage

Anaerobic sludges, pretreated by chloroform, base, acid, heat and loading-shock, as well as untreated sludge were evaluated for their thermophilic fermentative hydrogen-producing characters from cassava stillage in both batch and continuous experiments. Results showed that the highest hydrogen production was obtained by untreated sludge and there were significant differences (p < 0.05) in hydrogen yields (varied from 32.9 to 65.3 mlH₂/gVS) among the tested pretreatment methods in batch experiments. However, the differences in hydrogen yields disappeared in continuous experiments, which indicated the pretreatment methods had only short-term effects on the hydrogen production. Further study showed that alkalinity was a crucial parameter influencing the fermentation process. When the influent was adjusted to pH 6 by NaHCO₃ instead of NaOH, the hydrogen yield increased from about 40 to 52 mlH₂/gVS in all the experiments. Therefore, pretreatment of anaerobic sludge is unnecessary for practical thermophilic fermentative hydrogen production from cassava stillage.     

Rapid formation of hydrogen-producing granules in an anaerobic continuous stirred tank reactor induced by acid incubation

A novel approach to rapidly initiate granulation of hydrogen-producing sludge was developed in an anaerobic continuous stirred tank reactor at 37 degrees C. To induce microbial granulation, the acclimated culture was subject to an acid incubation for 24 h by shifting the culture pH from 5.5 to 2.0. The culture was resumed to pH 5.5 after the incubation and the reactor was operated at hydraulic retention times (HRTs) of 12, 6, 2, 1, and 0.5 h in sequence. Microbial aggregation took place immediately with the initiation of acid incubation and granules were developed at 114 h. No granule was observed in the absence of acid incubation in the control test. Changing the culture pH resulted in improvement in surface physicochemical properties of the culture favoring microbial granulation. The zeta potential increased from -11.6 to -3.5 mV, hydrophobicity in terms of contact angle improved from 31 degrees to 43 degrees and extracellular proteins/polysaccharides ratio increased from 0.2 to 0.5-0.8. Formation of granular sludge facilitated biomass retention of up to 32.2 g-VSS/L and enhanced hydrogen production. The hydrogen production rate and hydrogen yield increased with the reduction in HRT at an influent glucose concentration of 10 g/L once steady granular sludge layer was formed, achieving the respective peaks of 3.20 L/L x h and 1.81 mol-H(2)/mol-glucose at 0.5 h HRT. The experimental results suggested that acid incubation was able to initiate the rapid formation of hydrogen-producing granules by regulating the surface characteristics of microbial aggregates in a well-mixed reactor, which enhanced the hydrogen production.     

高效产氢菌株Enterococcus sp. LG1的分离及产氢特性

采用Hungate厌氧培养技术分别从厌氧污泥、好氧污泥及河底泥中分离出12株厌氧产氢细菌,并对其中的Enterococcus sp.LG1(注册号:EU258743)进行了研究.结果表明,该株细菌为专性厌氧菌,经革兰氏染色结果为阴性.通过16S rDNA碱基测序和比对证实,该菌株是目前尚未报道过的1个新菌种,初步确定其细菌学上的分类地位.同时,以灭菌预处理的污泥为底物培养基,对该菌的产氢能力及污泥发酵过程中底物性质变化(SCOD、可溶性蛋白质、总糖和pH值等)进行了探讨.实验结果显示,产氢茵Enterococcus sp.LG1的发酵过程中只有H2和CO2产生,无CH4产生.产气量最高为36.48 mL/g TCOD,氢气含量高达73.5%,为已报道文献中以污泥为底物发酵制氢中之最高.根据污泥发酵产物分析得知,该菌的发酵类行为典型的丁酸型发酵.     

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.     

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     

Start‐up of Anaerobic Hydrogen Producing Reactors Seeded with Sewage Sludge

The procedure for starting‐up continuously stirred tank reactors (CSTR) for acclimating anaerobic hydrogen‐producing microorganisms with sewage sludge was investigated. Initially, feeding with glucose and sucrose as well as mixing were carried out in semicontinuous mode; hydraulic retention time (HRT) was in an order of 20, 15, 10, 5, 2.5 and 2 days. When the pH declined to its lowest value (pH 5.18), it was adjusted to 6.7 using sodium hydroxide (1 N). At the same time, the semi‐continuous operation was changed to a continuous one. Finally, the pH was continuously regulated at approximately 6.7. The results indicate that this procedure can be used to cultivate seed sludge for hydrogen production from sewage sludge resulting in a large hydrogen production in less than 60 days. When the substrate was glucose, a hydrogen yield of 1.63 mol H₂/mol glucose and a specific hydrogen production rate of 321 mmol H₂/g VSS day at an HRT of 13.3 h was achieved. When the substrate was sucrose with the same HTR, a hydrogen yield of 4.45 mol H2/mol sucrose and a specific hydrogen production rate of 707 mmol H₂/g VSS day was obtained.     

Biohydrogen production in granular up-flow anaerobic sludge blanket (UASB) reactors with mixed cultures under hyper-thermophilic temperature (70 degrees C)

Hyper-thermophilic hydrogen production without methane was demonstrated for the first time in granular up-flow anaerobic sludge blanket (UASB) system fed with glucose using mixed cultures. The maximum hydrogen yield in this study was 2.47 +/- 0.15 mol H2/mol glucose. This high yield has never been previously reported in mixed culture systems and it was likely due to more favorable thermodynamic conditions at hyper-thermophilic temperatures. Different start-up strategies (bromoethanosulfonate (BES) addition and flow recycle) were evaluated. BES addition during start-up prevented the establishment of methanogenic cultures in granules. Flow recycle was important to achieve higher hydrogen yield through enriching better hydrogen-producing organisms and reduced the start-up period as well. This study indicated UASB system was a promising system for hydrogen production.     

厌氧产氢颗粒污泥蛋白质组分析样品的高效制备方法

【背景】厌氧产氢颗粒污泥比絮状产氢污泥具有更高的生物量、沉降性与反应效率,对颗粒污泥进行蛋白质组学研究,有助于揭示其代谢调控的分子机制,从而对厌氧代谢过程进行优化调控。目前关于产氢颗粒污泥蛋白质组分析样品制备方法的研究尚未见文献报道。革兰氏阳性菌Ethanoligenens harbinense YUAN-3是自凝集产氢发酵细菌,在间歇和连续流培养中可形成自聚集的厌氧颗粒,由于其全基因组信息清楚,可作为模式研究材料对制备方法进行评估。【目的】针对厌氧产氢颗粒污泥的蛋白质组学研究,比较不同蛋白质提取方法进行优化。【方法】分别利用液氮研磨、超声破碎、匀浆破碎对产氢颗粒污泥破碎,比较这3种方法对总蛋白提取量的影响;通过双向电泳比较三氯乙酸(Trichloroacetic acid,TCA)-丙酮沉淀法与苯酚抽提法对总蛋白提取效果的影响;对总蛋白样品分别进行同位素标记相对和绝对定量标记(Isobarictagsforrelativeandabsolutequantification,i TRAQ)、串联质谱标签(Tandemmasstag,TMT)标记以及质谱鉴定。【结果】液氮研磨、超声破碎、匀浆破碎3种破碎方法下总蛋白的提取量分别是对照样品的2.0、3.9与5.2倍。与TCA-丙酮沉淀法相比,苯酚抽提法总蛋白样品在双向电泳图谱上的蛋白质点明显增多,分布均匀,同时其在碱性蛋白端与小分子量蛋白端的蛋白质点也明显增多。质谱分析发现,iTRAQ标记样品与TMT标记样品中分别鉴定到1797个与1644个蛋白,在分子量、等电点、亚细胞定位的各个分布范围内,这些蛋白良好地覆盖了E.harbinenseYUAN-3中各个类型的蛋白。【结论】匀浆破碎与苯酚抽提法联用的总蛋白制备方法更适用于厌氧产氢颗粒污泥,该方法有利于后续的蛋白质双向电泳和定量蛋白质组质谱分析,可作为产氢颗粒污泥以及革兰氏阳性菌总蛋白制备的方法参考。     

产氢产乙酸菌ZR-1 的分离鉴定及产酸特性

采用改良的亨盖特厌氧操作技术, 从有机废水污泥中分离到一株耐低温高效产氢产乙酸菌ZR-1。经过对其形态学观察、生理生化特征研究及16S rRNA 序列比对, 初步鉴定为梭状芽胞杆菌属的乙二醇梭菌(Clostridium glycolicum)。通过单因子实验, 在厌氧条件下对该菌株的培养温度、pH、最适底物、金属离子的影响等产酸条件进行了优化。结果表明该菌株最适生长温度37 °C,最佳培养基初始pH 值8.5, 最适发酵底物丁酸盐, Mn²⁺对其产酸有一定的激活作用。最适培养条件下丁酸盐降解率达到12.7%, H₂ 含量达到了28.73%。     

Producing hydrogen from wastewater sludge by Clostridium bifermentans

Excess wastewater sludge collected from the recycling stream of an activated sludge process is biomass that contains large quantities of polysaccharides and proteins. However, relevant literature indicates that the bio-conversion of wastewater sludge to hydrogen is limited and therefore not economically feasible. This work examined the anaerobic digestion of wastewater sludge using a clostridium strain isolated from the sludge as inoculum. A much higher hydrogen yield than presented in the literature was obtained. Also, the effects of five pre-treatments-ultrasonication, acidification, sterilization, freezing/thawing and adding methanogenic inhibitor-on the production of hydrogen were examined. Freezing and thawing and sterilization increased the specific hydrogen yield by 1.5-2.5 times to that of untreated sludge, while adding an inhibitor and ultrasonication reduced the hydrogen yield.     

初始pH值对产氢产乙酸/耗氢产乙酸两段耦合工艺定向生产乙酸的影响

以葡萄糖为底物,以经加热预处理并活化过的厌氧污泥为种泥,研究了初始pH值对产氢产乙酸/耗氢产乙酸两段耦合工艺厌氧发酵定向生产乙酸的影响。实验考察了7个初始pH值(5、6、7、8、9、10、11)条件下的底物降解、产物产生和发酵过程pH值的变化。结果表明:产氢产乙酸段初始pH值的变化不仅影响本阶段产酸,而且影响耗氢产乙酸段产酸。初始pH=5时主要进行乙醇型发酵;pH=6和7时主要进行丁酸型发酵;pH=8时混合酸型发酵类型逐渐占优势,pH=8~11时均以乙酸为主要产物,耦合系统生产乙酸最优初始pH值为10。在初始pH=8~11范围内,产氢产乙酸段初期的乙醇浓度一般较高,但到后期因乙醇被微生物进一步代谢转化成乙酸而使其含量下降。     

Biological hydrogen production by anaerobic digestion of food waste and sewage sludge treated using various pretreatment technologies

The purpose of this study was to enhance the efficiency of anaerobic co-digestion with sewage sludge using pretreatment technologies and food waste. We studied the effects of various pretreatment methods (thermal, chemical, ultrasonic, and their combination) on hydrogen production and the characteristics of volatile fatty acids (VFAs) using sewage sludge alone and a mixture of sewage sludge and food waste. The pretreatment combination of alkalization and ultrasonication performed best, effecting a high solubilization rate and high hydrogen production (13.8 mL H₂/g VSS_consumed). At a food waste:pretreated sewage sludge ratio of 2:1 in the mixture, the peak hydrogen production value was 5.0 L H₂/L/d. As the production of hydrogen increased, propionate levels fell but butyrate concentrations rose gradually.     

Quantitative analysis of a high-rate hydrogen-producing microbial community in anaerobic agitated granular sludge bed bioreactors using glucose as substrate

Fermentative H₂ production microbial structure in an agitated granular sludge bed bioreactor was analyzed using fluorescence in situ hybridization (FISH) and polymerase chain reaction-denatured gradient gel electrophoresis (PCR-DGGE). This hydrogen-producing system was operated at four different hydraulic retention times (HRTs) of 4, 2, 1, and 0.5 h and with an influent glucose concentration of 20 g chemical oxygen demand/l. According to the PCR-DGGE analysis, bacterial community structures were mainly composed of Clostridium sp. (possibly Clostridium pasteurianum), Klebsiella oxytoca, and Streptococcus sp. Significant increase of Clostridium/total cell ratio (68%) was observed when the reactor was operated under higher influent flow rate. The existence of Streptococcus sp. in the reactor became more important when operated under a short HRT as indicated by the ratio of Streptococcus probe-positive cells to Clostridium probe-positive cells changing from 21% (HRT 4 h) to 38% (HRT 0.5 h). FISH images suggested that Streptococcus cells probably acted as seeds for self-flocculated granule formation. Furthermore, combining the inspections with hydrogen production under different HRTs and their corresponding FISH analysis indicated that K. oxytoca did not directly contribute to H₂ production but possibly played a role in consuming O₂ to create an anaerobic environment for the hydrogen-producing Clostridium.