Characteristics of hydrogen and methane production from cornstalks by an augmented two- or three-stage anaerobic fermentation process

This paper presents the co-production of hydrogen and methane from cornstalks by a two- or three-stage anaerobic fermentation process augmented with effective artificial microbial community. Two-stage fermentation by using the anaerobic sludge and DGGE analysis showed that effective and stable strains should be introduced into the system. We introduced Enterobacter aerogens or Clostridium paraputrificum into the hydrogen stage, and C. paraputrificum was proven to be more effective. In the three-stage process consisting of the improved hydrolysis, hydrogen and methane production stages, the highest soluble sugars (0.482 kg/kg cornstalks) were obtained after the introduction of Clostridium thermocellum in the hydrolysis stage, under the thermophilic (55 °C) and acidic (pH 5.0) conditions. Hydrolysates from 1 kg of cornstalks could produce 2.61 mol (63.7 l) hydrogen by augmentation with C. paraputrificum and 4.69 mol (114.6 l) methane by anaerobic granular sludge, corresponding to 54.1% energy recovery.     

Enhancement of bioenergy production from organic wastes by two-stage anaerobic hydrogen and methane production process

The present study investigated a two-stage anaerobic hydrogen and methane process for increasing bioenergy production from organic wastes. A two-stage process with hydraulic retention time (HRT) 3 d for hydrogen reactor and 12 d for methane reactor, obtained 11% higher energy compared to a single-stage methanogenic process (HRT 15 d) under organic loading rate (OLR) 3 gVS/(L d). The two-stage process was still stable when the OLR was increased to 4.5 gVS/(L d), while the single-stage process failed. The study further revealed that by changing the HRT_hydrogen:HRT_methane ratio of the two-stage process from 3:12 to 1:14, 6.7%, more energy could be obtained. Microbial community analysis indicated that the dominant bacterial species were different in the hydrogen reactors (Thermoanaerobacterium thermosaccharolyticum-like species) and methane reactors (Clostridiumthermocellum-like species). The changes of substrates and HRT did not change the dominant species. The archaeal community structures in methane reactors were similar both in single- and two- stage reactors, with acetoclastic methanogens Methanosarcina acetivorans-like organisms as the dominant species.     

Production of methane and hydrogen by anaerobic ciliates containing symbiotic methanogens

Rates of methane production by three anaerobic ciliates containing symbiotic methanogens (the marine Metopus contortus and Plagiopyla frontata, and the limnic Metopus palaeformis) were quantified. Hydrogen production by normal (containing active symbionts), aposymbiotic and BES-treated cells was also measured in the case of the marine species. Methanogenesis was closely coupled to host metabolism and growth; at maximum ciliate growth rates (20°C) each methanogen produced about 1 fmol CH₄ per hour corresponding to about 7, 4 and 0.35 pmol per ciliate per hour for M. contortus, P. frontata and M. palaeformis, respectively. Normal cells produced traces of H₂. Hydrogen production by BES-treated or aposymbiotic cells accounted for 75 and 45% of the methane production of normal M. contortus and P. frontata cells, respectively. However, it is possible that hydrogen production was partly inhibited in the absence of methanogens. Theoretical considerations suggest that hydrogen transfer is significant to the metabolism of larger anaerobic ciliates. Ciliates with methanogens produced CH₄ under microaerobic conditions due to their ability to maintain an anoxic intracellular environment at low external oxygen tensions. Methanogenesis was still detectable at a pO₂ of 0.63 kPa (3 %atm sat).     

Enhancement of methane production from cassava residues by biological pretreatment using a constructed microbial consortium

In the study, a stable thermophilic microbial consortium with high cellulose-degradation ability was successfully constructed. That several species of microbes coexisted in this consortium was proved by DGGE (denaturing gradient gel electrophoresis) and sequence analysis. The cooperation and symbiosis of these microbes in this consortium enhanced their cellulose-degradation ability. The pretreatment of cassava residues mixing with distillery wastewater prior to anaerobic digestion was investigated by using this microbial consortium as inoculums in batch bioreactors at 55 °C. The experimental results showed that the maximum methane yield (259.46 mL/g-VS) of cassava residues was obtained through 12 h of pretreatment by this microbial consortium, which was 96.63% higher than the control (131.95 mL/g-VS). In addition, it was also found that the maximum methane yield is obtained when the highest filter paper cellulase (FPase), carboxymethyl cellulase (CMCase) and xylanase activity and soluble COD (sCOD) are produced.     

Effect of fermentation temperature on hydrogen production from cow waste slurry by using anaerobic microflora within the slurry

We examined hydrogen production from a dairy cow waste slurry (13.4 g of volatile solids per liter) by batch cultures in a temperature range from 37 to 85°C, using microflora naturally present within the slurry. Without the addition of seed bacteria, hydrogen was produced by simply incubating the slurry, using the microflora within the slurry. Interestingly, two peaks of fermentation temperatures for hydrogen production from the slurry were observed at 60 and 75°C (392 and 248 ml H₂ per liter of slurry, respectively). After the termination of the hydrogen evolution, the microflora cultured at 60°C displayed hydrogen-consuming activity, but hydrogen-consuming activity of the microflora cultured at 75°C was not detected, at least for 24 days. At both 60 and 75°C, the main by-product was acetate, and the optimum pH of the slurry for hydrogen production was around neutral. Bacteria related to hydrogen-producing moderate and extreme thermophiles, Clostridium thermocellum and Caldanaerobacter subterraneus, were detected in the slurries cultured at 60 and 75°C, respectively, by denaturing gradient gel electrophoresis analyses, using the V3 region of 16S rDNA.     

The anaerobic decomposition of benzoic acid during methane fermentation

Anaerobic rupture of the benzoic acid ring was investigated. Carbon 4 was converted primarily to carbon dioxide. Following ring rupture during methane fermentation, propanoic acid is an intermediate, and carbon 4 of benzoate becomes its carboxyl.Contribution No. 1285-j, Division of Biology, Kansas State University, Manhattan, KS 66506. This work was supported in part by funds from the Kansas Agricultural Experiment Station, Kansas State University, Manhattan, KS 66506. Paper II of this series is Fina and Fiskin (1960)     

Dry anaerobic ammonia–methane production from chicken manure

The effect of temperature on production of ammonia during dry anaerobic fermentation of chicken manure (CM), inoculated with thermophilic methanogenic sludge, was investigated in a batch condition for 8 days. Incubation temperature did not have a significant effect on the production of ammonia. Almost complete inhibition of production of methane occurred at 55 and 65°C while quite low yields of 8.45 and 6.34 ml g⁻¹ VS (volatile solids) were observed at 35 and 45°C due to a higher accumulation of ammonia. In order to improve the production of methane during dry anaerobic digestion of CM, stripping of ammonia was performed firstly on the CM previously fermented at 65°C for 8 days: the stripping for 1 day at 85°C and pH 10 removed 85.5% of ammonia. The first-batch fermentation of methane for 75 days was conducted next, using the ammonia-stripped CM inoculated with methanogenic sludge at different ratios, (CM: thermophilic sludge) of 1:2, 1:1, and 2:1 on volume per volume basis at both 35 and 55°C. Production of methane improved and was higher than that of the control (without stripping of ammonia) but the yield of 20.4 ml g⁻¹ VS was still low, so second stripping of ammonia was conducted, which resulted in 74.7% removal of ammonia. A great improvement in the production of methane of 103.5 ml g⁻¹ VS was achieved during the second batch for 55 days.     

Production of hydrogen and methane from organic solid wastes by phase-separation of anaerobic process

Phase-separated two-stage anaerobic process was examined and evaluated using artificial organic solid waste in laboratory scale. Acidogenic process, which was combined with subsequent methanogenic process using packed-bed reactor, was operated emphasizing on either hydrogen production, or solublizing efficiency of solid materials. In either effluent from hydrogenogenic, or solublizing operation, maximum allowable OLR achieved at methanogenesis was higher than the single methanogenic process. Hydrogenogenic operation was more suitable to combine methanogenic process than solublizing operation, since retention time of hydrogenogenic operation was much shorter than the solublizing operation, obtaining almost the same levels of overall removal efficiency in both COD and VSS. The combination of hydrogenogenic operation in acidogenic process and methanogenic process produced approximately 442mmoll-reactor(1)days(-1) of methane and 199mmoll-reactor(1)days(-1) of hydrogen at 25h of total retention time indicating 82% of COD removal with 96% of VSS decomposition.     

利用餐厨垃圾循环半连续厌氧发酵产氢研究

利用餐厨垃圾采用半连续厌氧发酵进行产氢的研究。实验结果表明以高温(100℃)预处理15 min的厌氧活性污泥为种泥,在温度37℃,pH 6.0左右,较宽的稀释率(1.0~4.0 d-1)范围内,均能较好的实现厌氧发酵产氢。在稀释率D=2.4 d-1下,流出液中乙醇、乙酸、丙酸、丁酸和戊酸的质量分数分别为5.6%、29.6%、5.4%、58.5%和0.9%,产氢过程属于典型的丁酸型发酵,最终氢气的体积分数可达60%,氢气的产生速率为5.49 m3/(m3.d)。将厌氧发酵液相产物作为稀释液返回到反应器中,反应器的产氢能力大幅度的提高,当回流比R=0.8时,最大产氢速率可达10.9 m3/(m3.d),最终氢气的含量可达65%,厌氧发酵反应器的产氢能力提高了约130%。     

Hydrogen and methane production from desugared molasses using a two‐stage thermophilic anaerobic process

Hydrogen and methane production from desugared molasses by a two‐stage thermophilic anaerobic process was investigated in a series of two up‐flow anaerobic sludge blanket (UASB) reactors. The first reactor that was dominated with hydrogen‐producing bacteria of Thermoanaerobacterium thermosaccharolyticum and Thermoanaerobacterium aciditolerans could generate a high hydrogen production rate of 5600 mL H₂/day/L, corresponding to a yield of 132 mL H₂/g volatile solid (VS). The effluent from the hydrogen reactor was further converted to methane in the second reactor with the optimal production rate of 3380 mL CH₄/day/L, corresponding to a yield of 239 mL CH₄/g VS. Aceticlastic Methanosarcina mazei was the dominant methanogen in the methanogenesis stage. This work demonstrates that biohydrogen production can be very efficiently coupled with a subsequent step of methane production using desugared molasses. Furthermore, the mixed gas with a volumetric content of 16.5% H_2, 38.7% CO₂, and 44.8% CH₄, containing approximately 15% energy by hydrogen is viable to be bio‐hythane.     

Hydrogen and methane production through two-stage mesophilic anaerobic digestion of olive pulp

The present study focused on the anaerobic biohydrogen production from olive pulp (two phase olive mill wastes, TPOMW) and the subsequent anaerobic treatment of the effluent for methane production under mesophilic conditions in a two-stage process. Biohydrogen production from water-diluted (1:4) olive pulp was investigated at hydraulic retention times (HRT) of 30 h, 14.5 h and 7.5 h while methane production from the effluent of hydrogenogenic reactor was studied at 20 d, 15 d, 10 d and 5 d HRT. In comparison with previous studies, it has been shown that the thermophilic hydrogen production process was more efficient than the mesophilic one in both hydrogen production rate and yield. The methanogenic reactor was successfully operated at 20, 15 and 10 days HRT while it failed when an HRT of 5 days was applied. Methane productivity reached the maximum value of 1.13 ± 0.08 L/L/d at 10 days HRT whereas the methane yield increased with the HRT. The Anaerobic Digestion Model no. 1 (ADM1) was applied to the obtained experimental data from the methanogenic reactor to simulate the digester response at all HRT tested. The ability of the model to predict the experimental results was evident even in the case of the process failure, thus implying that the ADM1 could be a valuable tool for process design even in the case of a complex feedstock. In general, the two-stage anaerobic digestion proved to be a stable, reliable and effective process for energy recovery and stabilization treatment of olive pulp.     

Liquefaction and gasification during anaerobic digestion of coffee waste by two-phase methane fermentation with slurry-state liquefaction

In order to improve the gas evolution rate during anaerobic digestion of coffee waste by two-phase methane fermentation with slurry-state liquefaction, the liquefaction and gasification processes were separately investigated. In the liquefaction process (including the acidification process), treatment at a pH above 6 had no major effects on the liquefaction and acidification rates. However, the VFA production rates were 880 and 320 mg/l·d during mesophilic (37°C) and thermophilic (53°C) liquefaction, respectively. Mesophilic conditions were superior to thermophilic conditions in the liquefaction. With respect to the gasification process, a high TOC volumetric loading rate of 21 g/l·d was achieved during thermophilic gasification. However, the mesophilic gasification did not yield stable data, even at a low TOC volumetric loading rate of 2 g/l·d. The gas yield was 1.7 l/g TOC consumed during thermophilic gasification. The thermophilic liquefaction and thermophilic gasification reactors were connected in series and a two-phase experiment was conducted with the reactors at various volumetric ratios. The maximum gas evolution rate of 1.43 l/l·d was achieved with a combination of a gasification reactor with a 0.45l working volume and liquefaction reactor with a 2l working volume. This rate was 1.7 times higher than the rate obtained in a previous study.     

Swine manure fermentation for hydrogen production

Biohydrogen fermentation using liquid swine manure as substrate supplemented with glucose was investigated in this project. Experiments were conducted using a semi-continuously-fed fermenter (8 L in total volume and 4 L in working volume) with varying pHs from 4.7 through 5.9 under controlled temperature (35 ± 1 °C). The hydraulic retention time (HRT) tested include 16, 20, and 24 h; however, in two pH conditions (5.0 and 5.3), an additional HRT of 12 h was also tried. The experimental design combining HRT and pH provided insight on the fermenter performance in terms of hydrogen generation. The results indicated that both HRT and pH had profound influences on fermentative hydrogen productivity. A rising HRT would lead to greater variation in hydrogen concentration in the offgas and the best HRT was found to be 16 h for the fermenter in this study. The best pH value in correspondence to the highest hydrogen generation was revealed to be 5.0 among all the pHs studied. There was no obvious inhibition on hydrogen production by methanogenesis when methane content in the offgas was lower than 2%. Otherwise, an inverse linear relationship between hydrogen and methane content was observed with a correlation coefficient of 0.9699. Therefore, to increase hydrogen content in the offgas, methane production has to be limited to below 2%.     

Effect of iron concentration on hydrogen fermentation

The effect of the iron concentration in the external environment on hydrogen production was studied using sucrose solution and the mixed microorganisms from a soybean-meal silo. The iron concentration ranged from 0 to 4000 mgFeCl₂ l⁻¹. The temperature was maintained at 37°C. The maximum specific hydrogen production rate was found to be 24.0 mlg⁻¹ VSSh⁻¹ at 4000 mgFeCl₂ l⁻¹. The specific production rate of butyrate increased with increasing iron concentration from 0 to 20 mgFeCl₂ l⁻¹, and decreased with increasing iron concentration from 20 to 4000 mgFeCl₂ l⁻¹. The maximum specific production rates of ethanol (682 mgg⁻¹ VSSh⁻¹) and butanol (47.0 mgg⁻¹ VSSh⁻¹) were obtained at iron concentrations of 5 and 3 mgFeCl₂ l⁻¹, respectively. The maximum hydrogen production yield of 131.9 mlg⁻¹ sucrose was obtained at the iron concentration of 800 mgFeCl₂ l⁻¹. The maximum yields of acetate (389.3 mgg⁻¹ sucrose), propionate (37.8 mgg⁻¹ sucrose), and butyrate (196.5 mg g⁻¹ sucros) were obtained at iron concentrations of 3, 200 and 200 mgFeCl₂ l⁻¹, respectively. The sucrose degradation efficiencies were close to 1.0 when iron concentrations were between 200 and 800 mgFeCl₂ l⁻¹. The maximum biomass production yield was 0.283 gVSSg⁻¹ sucrose at an iron concentration of 3000 mgFeCl₂ l⁻¹.     

Response surface methodological analysis on biohydrogen production by enriched anaerobic cultures

The individual and interactive effects of pH, temperature and substrate concentration on the biohydrogen production from sucrose by mixed anaerobic cultures were investigated in this study. A central composite design and response surface methodology (RSM) were employed in planning the experiments, in order to determine the optimum conditions for biohydrogen production. Experimental results show that pH, temperature and substrate concentration all had a significant influence on specific hydrogen production potential (P_s) and the maximum hydrogen production rate (R_max) individually. Temperature and sucrose concentration, pH and temperature were interdependent or there was a significant interaction on P_s and R_max. Substrate concentration and pH were slightly interdependent, or their interactive effect on P_s and R_max was not significant. A maximum P_s of 252 mL H₂/g sucrose was estimated under the optimum conditions of pH 5.5, temperature 34.8 °C and sucrose concentration of 24.8 g/L, while a maximum R_max of 1511 mL H₂/h was calculated under the optimum conditions of pH 5.5, temperature 35.5 °C and sucrose concentration of 25.4 g/L. The experiment results show that the RSM with the central composite design was useful for optimizing the biohydrogen-producing process.     

啤酒废水的厌氧发酵产氢

对经热处理后的厌氧污泥利用啤酒废水厌氧产氢的影响因素（温度、初始pH值和有机物浓度）进行了研究。结果表明,温度与初始pH值对厌氧产氢过程均有显著影响。最佳温度为35℃,此时,比产氢速率、氢气产率、VFA含量与总糖降解率均达到最大,分别为10.16mL/g-VSS.h、0.1673mL/mg.COD、4640.0mg/L和95.20%。最适初始pH值为6.0～7.0,在此范围内氢气产率、VFA含量、总糖降解率均可获得最大值。一个半经验模型适用于描述初始pH值与氢气产率之间的相互关系。在35℃、初始pH值6.5的条件下,有机物浓度COD1000mg/L～2000mg/L时,总糖降解率与VFA产率均获得最大值。底物抑制模型分析结果显示COD1587mg/L时,氢气产率（0.1935mL/mg.COD）达到最大。     

Monitoring the biochemical hydrogen and methane potential of the two-stage dark-fermentative process

A two-step process has been recently proposed whereby the products of biological hydrogen production processes are used as substrates for biological methane production. The aim of the present study is to evaluate a simple bench-scale batch procedure for measuring the biochemical hydrogen and methane potential of organic substances as a two-step simulated process. Glucose fermentation showed an hydrogen and methane recovery (measured as the ratio of electron equivalents recovered as hydrogen and methane and electron equivalents of the initial substrate added) from the initial substrate of 13.3% and 75.5%, respectively, that approximates mass balance closure. On the contrary, gas recoveries ranging from 61% to 75% were measured from wastes originating from the food-industry. Moreover, the results demonstrate that the substrate origins significantly influence the ratio of H₂ and CH₄ recovery.     

Abundance and distribution of anaerobic protozoa and their contribution to methane production in Lake Cadagno (Switzerland)

Abstract In the uupermost layers of the anoxic sediment in Lake Cadagno, 9 different species of anaerobic protozoa were identified. The total number of these organisms was about 580 cells·ml⁻¹ sediment. Most pf these protozoa contained endosymbiotic methanogenic bacteria which in total amounted to 10⁶ methanogens·ml⁻¹ sediment. In addition to the methanogenic endosymbionts, cells of Metopus setosus and Caenomorpha lata also contained a non-fluorescent bacterial rod inside the cytoplasm. In some individual cells of C. lata this second type of endosymbiotic bacterium was sometimes the only endosymbiont observed. Contrary to earlier suggestions, anaerobic protozoa do not seem to play a major role in methane production at least in Lake Cadagno. No significant methane production due to the anaerobic protozoa and their methanogenic endosymbionts was found in situ. Isolated ciliates and amoebae produced methane at 12°C, but not at 6°C, probably as a result of temperature limitation. In the sediment of Lake Cadagno sulfate reduction seemed to be the dominant terminal degradation process.     

Methane recovery from the anaerobic codigestion of municipal sludge and FOG

The anaerobic biodegradability of a mix of municipal primary sludge (PS), thickened waste activated sludge (TWAS) and fat, oil, and grease (FOG) was assessed using semi-continuous feed, laboratory-scale anaerobic digesters operated at mesophilic (35 °C) and thermophilic (52 °C) temperature. Addition of a large FOG fraction (48% of the total VS load) to a PS + TWAS mix, resulted in 2.95 times larger methane yield, 152 vs. 449 mL methane @ STP/g VS added at 35 °C and 2.6 times larger methane yield, 197 vs. 512 mL methane @ STP/g VS added at 52 °C. The high FOG organic load fraction was not inhibitory to the process. The results of this study demonstrate the benefit of sludge and FOG codigestion.     

Isolation and characterization of an anaerobic syntrophic benzoate-degrading bacterium from sewage sludge

An anaerobic, motile, gram-negative, rod-shaped bacterium is described which degrades benzoate in coculture with an H₂-utilizing organism and in the absence of exogenous electron acceptors such as O₂, SO ₄ ⁼ or NO ₃ ^- . The bacterium was isolated from a municipal primary, anaerobic sewage digestor using anaerobic roll-tube medium with benzoate as the main energy source and in syntrophic association with an H₂-utilizing sulfate-reducing Desulfovibrio sp. which cannot utilize benzoate or fatty acids apart from formate as energy source. The benzoate utilizer produced acetate (3 mol/mol of substrate degraded) and presumably CO₂ and H₂, or formate from benzoate. In media without sulfate and with Methanospirillum hungatei (a methanogen that utilizes only H₂–CO₂ or formate as the energy source) added, 3 mol of acetate and 0.7 mol of methane were produced per mol of benzoate and CO₂ was probably formed. Low numbers of Desulfovibrio sp. were present in the methanogenic coculture and a pure coculture of the benzoate utilizer with M. hungatei was not obtained. The generation times for growth of the sulfate-reducing and methanogenic cocultures were 132 and 166h, respectively. The benzoate utilizer did not utilize other common aromatic compounds, C ₃ ^- –C₇ monocarboxylic acids, or C₄-C₆ dicarboxylic acids for growth, nor did it appear to use SO ₄ ⁼ , NO ₃ ^- or fumarate as alternative electron acceptors. Addition of H₂ inhibited growth and benzoate degradation.