Fermentation of biomass-generated synthesis gas: effects of nitric oxide

The production of renewable fuels, such as ethanol, has been steadily increasing owing to the need for a reduced dependency on fossil fuels. It was demonstrated previously that biomass-generated synthesis gas (biomass-syngas) can be converted to ethanol and acetic acid using a microbial catalyst. The biomass-syngas (primarily CO, CO(2), H(2), and N(2)) was generated in a fluidized-bed gasifier and used as a substrate for Clostridium carboxidivorans P7(T). Results showed that the cells stopped consuming H(2) when exposed to biomass-syngas, thus indicating that there was an inhibition of the hydrogenase enzyme due to some biomass-syngas contaminant. It was hypothesized that nitric oxide (NO) detected in the biomass-syngas could be the possible cause of this inhibition. The specific activity of hydrogenase was monitored with time under varying concentrations of H(2) and NO. Results indicated that NO (at gas concentrations above 40 ppm) was a non-competitive inhibitor of hydrogenase activity, although the loss of hydrogenase activity was reversible. In addition, NO also affected the cell growth and increased the amount of ethanol produced. A kinetic model of hydrogenase activity with inhibition by NO was demonstrated with results suggesting there are multiple binding sites of NO on the hydrogenase enzyme. Since other syngas-fermenting organisms utilize the same metabolic pathways, this study estimates that NO < 40 ppm can be tolerated by cells in a syngas-fermentation system without compromising the hydrogenase activity, cell growth, and product distribution.     

Influence of switchgrass generated producer gas pre-adaptation on growth and product distribution of Clostridium ragsdalei

Gasification-fermentation is a thermo chemical-biological process for the production of fuels and chemicals. Producer gas cleanup is a major issue that must be addressed for integration of these platforms. Pre-adaptation of producer gas fermenting microbes to gas impurities has improved tolerances to impurities and production of alcohols in certain bacteria. In this research, the effect of switchgrass generated producer gas was studied with adapted and unadapted cultures of C. ragsdalei and compared to fermentations with a control of clean custom producer gas. Results indicated no inhibition to microbial growth with unadapted cells and final cell mass concentrations were 22% higher when cells were exposed to switchgrass-based producer gas compared to control. The ethanol productivity with adapted cells was 1.9 and 2.8 times higher than unadapted and control treatments, respectively. Similarly, the ethanol yield (Y_ETOH/X) of C. ragsdalei adapted to producer gas was 119% more than the control and 35% greater than the unadapted cells used in this study. The presence of switchgrass-based producer gas also induced metabolic shifts resulting in reduction of acetic acid to ethanol that increased ethanol to acetate ratios from 0.7 g/g in control to 4.9 g/g with unadapted cells and 13.7 g/g with adapted cells. Isopropanol was also observed as a product when switchgrass generated producer gas was used. We conclude that cultural adaptation of C. ragsdalei to biomass generated producer gas during preculture stages could be used as an important strategy to enhance ethanol yields for integrating gasification and fermentation platforms using C. ragsdalei.     

Ethanol and acetate production by <Emphasis Type="Italic">Clostridium ljungdahlii</Emphasis> and <Emphasis Type="Italic">Clostridium autoethanogenum</Emphasis> using resting cells

Combined gasification and fermentation technologies can potentially produce biofuels from renewable biomass. Gasification generates synthesis gas consisting primarily of CO, CO₂, H₂, N₂, with smaller amounts of CH₄, NO_x, O₂, C₂ compounds, ash and tars. Several anaerobic bacteria species can ferment bottled mixtures of pure synthesis gas constituents. However, there are challenges to maintaining culture viability of synthesis gas exposed cells. This study was designed to enhance culture stability and improve ethanol-to-acetate ratios using resting (non-growing) cells in synthesis gas fermentation. Resting cell states were induced in autotrophic Clostridium ljungdahlii cultures with minimal ethanol and acetate production due to low metabolic activity compared to growing cell production levels of 5.2 and 40.1 mM of ethanol and acetate. Clostridium autoethanogenum cultures were not induced into true resting states but did show improvement in total ethanol production (from 5.1 mM in growing cultures to 9.4 in one nitrogen-limited medium) as well as increased shifts in ethanol-to-acetate production ratios.     

Pyrolysis of glycerol for the production of hydrogen or syn gas

Biodiesel has high potential as alternative liquid transportation fuel because it is renewable and CO(2) neutral, and has similar properties as diesel fuel. Glycerol is a by-product obtained during the production of biodiesel. Canadian government has planned to produce 500 million litres of biodiesel by 2010. An increase in biodiesel production would decrease the market price of glycerol. The objective of this study is to pyrolyse glycerol for the production of clean fuels such as H(2) or a feedstock such as syn gas for additional transportation fuel via Fisher-Tropsch synthesis. The pyrolysis of glycerol was carried out at various flow rates of N(2) (30-70 mL/min), temperatures (650-800 degrees C) and types and sizes of packing material in a tubular reactor at atmospheric pressure. The products were mostly gas, essentially consisting of CO, H(2), CO(2), CH(4) and C(2)H(4). It was observed that temperature, carrier flow rates and particle diameter of packing material had profound effects on the conversion of glycerol as well as product distribution. Composition of product gas ranged between syn gas 70-93 mol%, CH(4) 3-15 mol% and C(2)H(4) 2-12 mol% and heating value ranged from 13 to 22 MJ/m(3). This study indicates that the bio-glycerol has potential in making syn gas and medium heating value gases.     

多年冻土退化地区湿地土壤温室气体排放及其影响因子

采用野外原位实验静态箱-气相色谱法,研究了兴安岭多年冻土不同程度退化地区生长季湿地土壤温室气体CH4、CO2和N2O的排放通量特征,同时分析了环境因子对土壤温室气体排放的影响。结果表明:1)3种类型冻土区(季节性冻土区、岛状多年冻土区、连续多年冻土区,分别用D1、D2、D3表示)土壤在生长季时期表现为CO2和N2O的源;D1和D3为CH4的源,D2为CH4的汇。D1、D2、D3土壤在生长季中平均CH4排放通量分别为(0.127±0.021)、(-0.020±0.006)、(0.082±0.019)mg·m^-2·h^-1;CO2排放通量分别为(371.50±66.73)、(318.43±55.67)、(213.19±37.05)mg·m^-2·h^-1;N2O排放通量分别为(24.05±2.62)、(8.07±2.42)、(2.17±0.25)μg·m-2·h-1。土壤CO2和N2O排放通量随多年冻土退化程度的加剧呈现出升高的趋势。2)细根生物量、凋落物生物量、全碳、全氮、可溶性有机碳、总可溶性氮、土壤容重、土壤温度、土壤含水量等均影响温室气体排放,3种不同类型冻土区土壤CH4、CO2和N2O的排放差异是诸多影响因子综合作用的结果。     

合成气厌氧发酵生产有机酸和醇的研究进展

合成气来自于煤、石油、生物质和有机废物的气化,其主要成份为CO、H2和CO2。研究发现某些厌氧菌能利用合成气生成乙醇、乙酸、丁醇和丁酸等燃料和化学品。由于生物转化所具有的优势,合成气厌氧发酵被认为是一项极具潜力和竞争力的技术,在生物质及有机废物的利用方面将发挥重要作用。对厌氧发酵合成气生产有机酸和醇的研究进展,包括利用合成气产有机酸和醇的微生物,合成气发酵的代谢途径和关键酶（一氧化碳脱氢酶/乙酰辅酶A合成酶）及用于合成气发酵的反应器等进行了综述,并对该项技术的发展提出了一些建议。     

Greenhouse gas emission during storage of pig manure on a pilot scale

The greenhouse gas emissions (CO2, CH4, N2O) from a 2 ton (4.4 m3) deep litter pig manure pile (storage time 113 days during winter season) were quantified by using a tent, which covered the whole pile during the measuring periods only. The emissions were calculated in CO2 equivalents per kilogram dry matter by. Additionally the retention time (use of tracer gas SF6) and the concentrations of the gases in different parts of the pile were determined. The average retention time of the gases in the pile was less than 2 h. CH4 is assumed to have been generated only in the centre of the pile, whereas CO2 was assumed to have been generated in a wider zone. The emissions of CH4, CO2 and N2O were at the highest in the beginning when nearly the whole pile had temperatures in the range of thermophilic microorganisms. This leads to the assumption that mainly thermophilic microorganisms formed the gases. The most important gas for global warming was found to be nitrous oxide.     

Rapid Method for the Radioisotopic Analysis of Gaseous End Products of Anaerobic Metabolism

A gas chromatographic procedure for the simultaneous analysis of (14)C-labeled and unlabeled metabolic gases from microbial methanogenic systems is described. H(2), CH(4), and CO(2) were separated within 2.5 min on a Carbosieve B column and were detected by thermal conductivity. Detector effluents were channeled into a gas proportional counter for measurement of radioactivity. This method was more rapid, sensitive, and convenient than gas chromatography-liquid scintillation techniques. The gas chromatography-gas proportional counting procedure was used to characterize the microbial decomposition of organic matter in anaerobic lake sediments and to monitor (14)CH(4) formation from H(2) and (14)CO(2) by Methanosarcina barkeri.     

Pyrolytic behavior of waste corn cob

The powder of the agricultural waste corn cob was pyrolyzed in a tube-typed stainless steel reactor of 200 ml volume under N2 atmosphere. The compositions of the gases and liquid obtained at different pyrolytic temperatures below 600 degrees C at the heating rate of 30 K/min were analyzed. With the increment of the pyrolytic temperature, the yields of the solid and the liquid products were decreased, but the yield of gas products was increased. The liquid products were approximately 34-40.96% (wt%), the gas products were 27-40.96% (wt%) and the solid products 23.6-31.6% (wt%). There were less changes for the yields of these products above 600 degrees C. The gas products were analyzed by gas chromatography (GC) as CO2, CO, H2, CH4, C2H4, C3H6, C3H8, etc. When the temperature was 350-400 degrees C, the gases had CO2 and CO 80-95% (v/v). When the temperature increased continuously, yields of H2, CH4, C2H4, C3H6 and C3H8 gradually increased. The liquid products were identified by GC-MS as phenols, 2-furanmethanol, 2-cyclopentanedione, etc. The Fourier transform infra-red spectrophotometer (FT-IR) analysis of the liquid product showed a strong -OH group absorption peak. Differential thermogravimetric analysis (DTG) showed that thermal decomposition process involves two steps. The heating rate affects not only the activation energy of the decomposition reaction, but also the path of the reaction. With the increment of the heating rate, the maximum rate temperature of the decomposition reaction was shifted to a higher temperature, and the order and activation energy of the total decomposition reaction were decreasing.     

玉渡山水库生长季温室气体排放特征及其影响因素

为了探讨温带水库温室气体排放规律,采用静态箱-色谱分析法,研究了温带地区库龄10年内的北京玉渡山水库生长季3种温室气体CO2、CH4及N2O排放特征,及其影响因子。结果表明:样地类型、测定月份与样地类型交互作用对3种温室气体通量影响极显著,5月消落带CO2通量(664.31mg·m-2·h-1)达到最大,显著高于入库口和浅水区;8月消落带CH4通量(0.87mg·m-2·h-1)及N2O通量(3.05mg·m-2·h-1)最大;8月,切除消落带样地地上植物后,3种温室气体通量均有所降低。CO2通量与地下5cm地温、氧化还原电位和水体总氮显著正相关,与地上生物量和水体pH显著负相关;CH4通量与地表温度、地上生物量、水体pH呈显著相关,与水体总氮和水体铵态氮显著负相关;N2O通量与水体总氮含量显著相关,与水体pH显著负相关。采取平均估值法初步推测,在生长季,水库消落带、入库口及浅水区CO2排放量依次为15960、2160、-70kg·hm-2;CH4排放量依次20.04、-7.05、14.8kg·hm-2;N2O排放量依次83.42、3.79、-1.54kg·hm-2;表明消落带3种温室气体的排放量均较高,为玉渡山水库3种温室气体排放的重点区域。     

Tracing carbon monoxide uptake by Clostridium ljungdahlii during ethanol fermentation using 13C-enrichment technique

Conversion of synthesis gas (CO and H₂) to ethanol can be an alternative, promising technology to produce biofuels from renewable biomass. To distinguish microbial utilization of carbon source between fructose and synthesis gas CO and to evaluate biological production of ethanol from CO, we adopted the ¹³C-enrichment of the CO substrate and hypothesized that the residual increase in δ¹³C of the cell biomass would reflect the increased contribution of ¹³C-enriched CO. Addition of synthesis gas to live culture medium for ethanol fermentation by Clostridum ljungdahlii increased the microbial growth and ethanol production. Despite the high ¹³C-enrichment in CO (99 atom % ¹³C), however, microbial δ¹³C increased relatively small compared to the microbial growth. The uptake efficiency of CO estimated using the isotope mass balance equation was also very low: 0.0014 % for the low CO and 0.0016 % for the high CO treatment. Furthermore, the fast production of ethanol in the early stage indicated that the presence of sugar in fermentation medium would limit the utilization of CO as a carbon source by C. ljungdahlii.     

Soil microorganisms as controllers of atmospheric trace gases (H2, CO, CH4, OCS, N2O, and NO).

Production and consumption processes in soils contribute to the global cycles of many trace gases (CH4, CO, OCS, H2, N2O, and NO) that are relevant for atmospheric chemistry and climate. Soil microbial processes contribute substantially to the budgets of atmospheric trace gases. The flux of trace gases between soil and atmosphere is usually the result of simultaneously operating production and consumption processes in soil: The relevant processes are not yet proven with absolute certainty, but the following are likely for trace gas consumption: H2 oxidation by abiontic soil enzymes; CO cooxidation by the ammonium monooxygenase of nitrifying bacteria; CH4 oxidation by unknown methanotrophic bacteria that utilize CH4 for growth; OCS hydrolysis by bacteria containing carbonic anhydrase; N2O reduction to N2 by denitrifying bacteria; NO consumption by either reduction to N2O in denitrifiers or oxidation to nitrate in heterotrophic bacteria. Wetland soils, in contrast to upland soils are generally anoxic and thus support the production of trace gases (H2, CO, CH4, N2O, and NO) by anaerobic bacteria such as fermenters, methanogens, acetogens, sulfate reducers, and denitrifiers. Methane is the dominant gaseous product of anaerobic degradation of organic matter and is released into the atmosphere, whereas the other trace gases are only intermediates, which are mostly cycled within the anoxic habitat. A significant percentage of the produced methane is oxidized by methanotrophic bacteria at anoxic-oxic interfaces such as the soil surface and the root surface of aquatic plants that serve as conduits for O2 transport into and CH4 transport out of the wetland soils. The dominant production processes in upland soils are different from those in wetland soils and include H2 production by biological N2 fixation, CO production by chemical decomposition of soil organic matter, and NO and N2O production by nitrification and denitrification. The processes responsible for CH4 production in upland soils are completely unclear, as are the OCS production processes in general. A problem for future research is the attribution of trace gas metabolic processes not only to functional groups of microorganisms but also to particular taxa. Thus, it is completely unclear how important microbial diversity is for the control of trace gas flux at the ecosystem level. However, different microbial communities may be part of the reason for differences in trace gas metabolism, e.g., effects of nitrogen fertilizers on CH4 uptake by soil; decrease of CH4 production with decreasing temperature; or different rates and modes of NO and N2O production in different soils and under different conditions.     

Importance of agitation in acetone-butanol fermentation

The specific rates of anaerobic solvent production by Clostridium acetobutylicum increased with increasing fermentor impeller speed from 190 to 340 rpm (N(Re) = 3.93 x 10(4)). The maximum values were 5.54, 3.85, and 0.8 mmol/h . g cell for butanol, acetone, and ethanol, respectively. Corresponding rates for respective gases produced were 11.60 and 15.88 mmol/h . g cell for H(2) and CO(2). Further increases in agitation speed resulted in generally decreasing specific production rates to the point of inactive fermentation at 560 rpm. A competition observed between the cellular subsystems for butanol + butyric acid and biomass biosynthesis was evaluated through expressing the energetic yield coefficients. An imbalance between the production and outflux of the former metabolites is apparently further enhanced by a mechanical damage of the cells at high shear rates. A correlation was developed between the production of gases and solvents pointing at both H(2)-to-solvent as well as CO(2)-to-solvent ratios following the same pattern, peaking at 410 rpm.     

Fermentation of cellulose by Ruminococcus flavefaciens in the presence and absence of Methanobacterium ruminantium

The anaerobic cellulolytic rumen bacterium Ruminococcus flavefaciens normally produces succinic acid as a major fermentation product together with acetic and formic acids, H2, and CO2. When grown on cellulose and in the presence of the methanogenic rumen bacterium Methanobacterium ruminantium, acetate was the major fermentation product; succinate was formed in small amounts; little formate was detected; H2 did not accumulate; and large amounts of CH4 were formed. M. ruminantium depends for growth on the reduction of CO2 to CH4 by H2, which it can obtain directly or by producing H2 and CO2 from formate. In mixed culture, the methanobacterium utilized the H2 and possibly the formate produced by the ruminococcus and in so doing stimulated the flow of electrons generated during glycolysis by the ruminococcus toward H2 formation and away from formation of succinate. This type of interaction may be of significance in determining the flow of cellulose carbon to the normal rumen fermentation products.     

Fermentation of cellulose by Ruminococcus flavefaciens in the presence and absence of Methanobacterium ruminantium.

The anaerobic cellulolytic rumen bacterium Ruminococcus flavefaciens normally produces succinic acid as a major fermentation product together with acetic and formic acids, H2, and CO2. When grown on cellulose and in the presence of the methanogenic rumen bacterium Methanobacterium ruminantium, acetate was the major fermentation product; succinate was formed in small amounts; little formate was detected; H2 did not accumulate; and large amounts of CH4 were formed. M. ruminantium depends for growth on the reduction of CO2 to CH4 by H2, which it can obtain directly or by producing H2 and CO2 from formate. In mixed culture, the methanobacterium utilized the H2 and possibly the formate produced by the ruminococcus and in so doing stimulated the flow of electrons generated during glycolysis by the ruminococcus toward H2 formation and away from formation of succinate. This type of interaction may be of significance in determining the flow of cellulose carbon to the normal rumen fermentation products.     

The relationship between hydrogen gas and butanol production by Clostridium saccharoperbutylacetonicum

Two simultaneous fermentations were performed at 26 degrees C with simultaneous inocula using Clostridium saccharoperbutylacetonicum. Fermentation 1 prevented the gas formed by the biomass from escaping the fermentor while 2 allowed the gas formed to escape. Fermentor 1 provided for the production of butanol, acetone, and ethanol, while when the H(2) formed was allowed to escape with fermentor 2, neither butanol nor acetone were produced. Ethanol was also formed in both fermentors and began along with the initial growth of biomass and continued until the fermentations were complete. Butanol and acetone production began after biomass growth had reached a maximum and began to subside. The butanol-acetone-ethanol millimolar yields and ratios were 38:1:14 respectively. The fermentor 2 results show that a yield of 2.1 L H(2), 93 or 370 mmol H(2)/mol glucose, was formed only during the growing stage of growth; neither butanol nor acetone were produced; ethanol was formed throughout the fermentation, reaching a yield of 15.2 mmolar. It appears that hydrogen gas is required for butanol production during the resting stage of growth.     

Acidogenic fermentation of lactose

Cheese whey is the main component of waste streams from cheese manufacturing plants. Whey is a high biochemical oxygen demand (BOD) effluent that must be reduced before the streams are sent to the sewer. It is proposed in this article that the production of methane by anaerobic fermentation would be the best use of this stream, especially for small plants. Single-stage fermentation of lactose, the main component of whey, results in a very low pH and a stalled process. Two-phase fermentation will eliminate this problem. The acidogenic stage of fermentation has been studied at pH of between 4 and 6.5. The nature of the main products of the reaction have been found to be pH dependent. Below a pH of 4.5 a gas (CO(2) and H(2)) is produced along with ethanol, acetate, and butyrate. Above a pH of 4.5 no gas was produced, and the liquid products included less ethanol and butyrate and more acetate. A separate study on the conditions for gas formation showed that if the pH dropped for a short time below 4.5 gases were formed at all subsequent pH. This would indicate a change in population distribution due to the period at a low pH. By assuming that the desired products from the acidogenic stage were butyrate, acetate, and no gases, the optimum pH range was found to be between 6.0 and 6.5.     

Methane fermentation of rubber (Hevea brasiliensis) latex effluent.

Four species of bacteria capable of CH4 fermentation of rubber latex effluent were isolated and identified as a Methanococcus, a strain of M. vannielii, a Methanobacterium and a strain of M. omelianskii. Auxanographic tests using the four strains showed growth and CH4 formation on a basal medium containing mineral salts or added H2 and Co2. Varied response was obtained when the basal medium was added to formate, acetate, butyrate, methanol, ethanol, and glucose. Previous work has established acid fermentation of Hevea latex arising from bacterial contamination and decomposition of the non-rubber constituents which consist of N-compounds, 2% quebrachitol, and smaller concentration of carbohydrates. This suggests that reduction of CO2 and fermentation of acids formed during metabolism of Hevea latex are possible pathways of CH4 production.     

Study of gaseous substrate fermentations: carbon monoxide conversion to acetate. 1. Batch culture

Biological processes may be used to convert gas phase substrates, such as H(2)S, CH(4), CO, H(2), and CO(2), to useful products. Utilization of these substrates is often a mass transfer limited process, first requiring absorption across the gas-liquid interface and diffusion through the culture medium to the cell surface, prior to reaction. This article presents a method for determining fermentation parameters of a gaseous substrate in convenient batch vessels using a modified Monod model. The procedure is illustrated with experimental data for the conversion of carbon monoxide to acetate by the strict anaerobe Peptostreptococcus productus.     

Reduction of acetone to isopropanol using producer gas fermenting microbes

Gasification‐fermentation is an emerging technology for the conversion of lignocellulosic materials into biofuels and specialty chemicals. For effective utilization of producer gas by fermenting bacteria, tar compounds produced in the gasification process are often removed by wet scrubbing techniques using acetone. In a preliminary study using biomass generated producer gas scrubbed with acetone, an accumulation of acetone and subsequent isopropanol production was observed. The effect of 2 g/L acetone concentrations in the fermentation media on growth and product distributions was studied with “Clostridium ragsdalei,” also known as Clostridium strain P11 or P11, and Clostridium carboxidivorans P7 or P7. The reduction of acetone to isopropanol was possible with “C. ragsdalei,” but not with P7. In P11 this reaction occurred rapidly when acetone was added in the acidogenic phase, but was 2.5 times slower when added in the solventogenic phase. Acetone at concentrations of 2 g/L did not affect the growth of P7, but ethanol increased by 41% and acetic acid concentrations decreased by 79%. In the fermentations using P11, growth was unaffected and ethanol concentrations increased by 55% when acetone was added in the acidogenic phase. Acetic acid concentrations increased by 19% in both the treatments where acetone was added. Our observations indicate that P11 has a secondary alcohol dehydrogenase that enables it to reduce acetone to isopropanol, while P7 lacks this enzyme. P11 offers an opportunity for biological production of isopropanol from acetone reduction in the presence of gaseous substrates (CO, CO₂, and H₂). Biotechnol. Bioeng. 2011;108: 2330–2338. © 2011 Wiley Periodicals, Inc.