Effects of high product and substrate inhibitions on the kinetics and biomass and product yields during ethanol batch fermentation

In ethanol fermentation, instantaneous biomass yield of the yeast Saccharmoyces cerevisiae was found to decrease (from 0.156 to 0.026) with increase in ethanol concentration (from 0 to 107 g/L), indicating a definite relationship between biomass yield and product inhibition. A suitable model was proposed to describe this decrease which incorporates the kinetic parameters of product inhibition rather than pure empirical constants. Substrate inhibition was found to occur when substrate concentration is above 150 g/L. A similar definite relationship was observed between substrate inhibition and instantaneous biomass yield. A simple empirical model is proposed to describe the declines in specfic growth rate and biomass yield due to substrate inhibition. It is observed that product inhibition does not have any effect on product yield whereas substrate inhibition significantly affects the product yield, reflecting a drop in overall product yield from 0.45 to 0.30 as the initial substrate concentration increases from 150 to 280 g/L. These results are expected to have a significant influence in formulating optimum fermentor design variables and in developing an effective control strategy for optimizing ethanol producitivity.     

Effect of substrate loading on hydrogen production during anaerobic fermentation by Clostridium thermocellum 27405

We have investigated hydrogen (H₂) production by the cellulose-degrading anaerobic bacterium, Clostridium thermocellum. In the following experiments, batch-fermentations were carried out with cellobiose at three different substrate concentrations to observe the effects of carbon-limited or carbon-excess conditions on the carbon flow, H₂-production, and synthesis of other fermentation end products, such as ethanol and organic acids. Rates of cell growth were unaffected by different substrate concentrations. H₂, carbon dioxide (CO₂), acetate, and ethanol were the main products of fermentation. Other significant end products detected were formate and lactate. In cultures where cell growth was severely limited due to low initial substrate concentrations, hydrogen yields of 1 mol H₂/mol of glucose were obtained. In the cultures where growth ceased due to carbon depletion, lactate and formate represented a small fraction of the total end products produced, which consisted mainly of H₂, CO₂, acetate, and ethanol throughout growth. In cultures with high initial substrate concentrations, cellobiose consumption was incomplete and cell growth was limited by factors other than carbon availability. H₂-production continued even in stationary phase and H₂/CO₂ ratios were consistently greater than 1 with a maximum of 1.2 at the stationary phase. A maximum specific H₂ production rate of 14.6 mmol g dry cell⁻¹ h⁻¹ was observed. As cells entered stationary phase, extracellular pyruvate production was observed in high substrate concentration cultures and lactate became a major end product.     

Mevalonate production by engineered acetogen biocatalyst during continuous fermentation of syngas or CO2/H2 blend

Naturally mevalonate-resistant acetogen Clostridium sp. MT1243 produced only 425 mM acetate during syngas fermentation. Using Clostridium sp. MT1243 we engineered biocatalyst selectively producing mevalonate from synthesis gas or CO₂/H₂ blend. Acetate production and spore formation were eliminated from Clostridium sp. MT1243 using Cre-lox66/lox71-system. Cell energy released via elimination of phosphotransacetylase, acetate kinase and early stage sporulation genes powered mevalonate accumulation in fermentation broth due to expression of synthetic thiolase, HMG-synthase, and HMG-reductase, three copies of each, integrated using Tn7-approach. Recombinants produced 145 mM mevalonate in five independent single-step fermentation runs 25 days each in five repeats using syngas blend 60 % CO and 40 % H₂ (v/v) (p < 0.005). Mevalonate production was 97 mM if only CO₂/H₂ blend was fed instead of syngas (p < 0.005). Mevalonate from CO₂/H₂ blend might serve as a commercial route to mitigate global warming in proportion to CO₂ fermentation scale worldwide.     

Biomethanation: Anaerobic fermentation of CO2, H2 and CO to methane

Studies to examine the microbial fermentation of coal gasification products (CO₂, H₂ and CO) to methane have been done with a mixed culture of anaerobic bacteria selected from an anaerobic sewage digestor. The specific rate of methane production at 37°C reached 25 mmol/g cell hr. The stoichiometry for methane production was 4 mmol H₂/mol CO₂. Cell recycle was used to increase the cell concentration from 2.5 to 8.3 g/liter; the volumetric rate of methane production ran from 1.3 to 4 liter/liter hr. The biogasification was also examined at elevated pressure (450 psi) and temperature to facilitate interfacing with a coal gasifier. At 60°C, the specific rate of methane production reached 50 mmol/g cell hr. Carbon monoxide utilization by the mixed culture of anaerobes and by a Rhodopseudomonas species was examined. Both cultures are able to carry out the shift conversion of CO and water to CO₂ and hydrogen.     

Bacterial community dynamics and product distribution during pH-adjusted fermentation of vegetable wastes

AIMS: To estimate the effect of pH on the structures of bacterial community during fermentation of vegetable wastes and to investigate the relationship between bacterial community dynamics and product distribution. METHODS AND RESULTS: The bacterial communities in five batch tests controlled at different pH values [uncontrolled (about pH 4), 5, 6, 7 and 8] were monitored by denaturing gradient gel electrophoresis (DGGE) and single-strand conformation polymorphism (SSCP). The two fingerprinting methods provided consistent results and principal component analysis indicated a close similarity of bacterial community at pH 7 and 8 in addition to those at pH 4-6. This clustering also corresponded to dominant metabolic pathway. Thus, pH 7-8 shifted from alcohol-forming to acid-forming, especially butyric acid, whereas both alcohol-forming and acid-forming dominated at pH 5-6, and at pH 4, fermentation was inhibited. Shannon-weaver index was calculated to analyse the DGGE profiles, which revealed that the bacterial diversities at pH 7 and 8 were the highest while those at pH 5 and 4 (uncontrolled) were the lowest. According to sequencing results of the bands excised from DGGE gels, lactic acid bacteria and Clostridium sp. were predominant at all pH values, but varieties in species were observed as pH changed and time prolonged. CONCLUSIONS: The bacterial community during fermentation was materially influenced by pH and the diverse product distribution was related to the shift of different bacterial population. SIGNIFICANCE AND IMPACT OF THE STUDY: The study reveals that the impact of pH on fermentation product distribution is implemented primarily by changes of bacterial community. It also provides information about the comparison of two fingerprinting methods, DGGE and SSCP.     

豆粕营养成分对蝙蝠蛾拟青霉发酵产物的影响

为探索培养基中的豆粕以及制备豆粕的原材料大豆对蝙蝠蛾拟青霉发酵产物的影响,我们比较了不同品种大豆和用其制成的豆粕的主要营养成分含量,包括粗蛋白、粗脂肪、6种微量元素（钙、镁、铜、锌、铁、锰）和总异黄酮（大豆苷、黄豆黄苷、染料木苷、大豆苷元、黄豆黄素、染料木素）,以及豆粕作为培养基对蝙蝠蛾拟青霉发酵产物的生物量和有效成分含量包括腺苷、腺嘌呤、虫草素和麦角甾醇的影响,结果表明大豆中钙和大豆苷与发酵产物中腺苷含量正相关。豆粕中钙、大豆苷、大豆苷元、染料木素与发酵产物中腺苷含量正相关;豆粕中钙、镁、大豆苷、大豆苷元、染料木素、总异黄酮与发酵产物中腺嘌呤含量负相关;豆粕中铁与菌丝体干重值正相关。结果表明,培养基中的豆粕和原料大豆主要营养成分含量对蝙蝠蛾拟青霉发酵产物品质有显著影响。     

Electron availability in CO2, CO and H2 mixtures constrains flux distribution,energy management and product formation in Clostridium ljungdahlii

Acetogens such as Clostridium ljungdahlii can play a crucial role reducing the human CO₂ footprint by converting industrial emissions containing CO₂, CO and H₂ into valuable products such as organic acids or alcohols. The quantitative understanding of cellular metabolism is a prerequisite to exploit the bacterial endowments and to fine-tune the cells by applying metabolic engineering tools. Studying the three gas mixtures CO₂ + H₂, CO and CO + CO₂ + H₂ (syngas) by continuously gassed batch cultivation experiments and applying flux balance analysis, we identified CO as the preferred carbon and electron source for growth and producing alcohols. However, the total yield of moles of carbon (mol-C) per electrons consumed was almost identical in all setups which underlines electron availability as the main factor influencing product formation. The Wood–Ljungdahl pathway (WLP) showed high flexibility by serving as the key NAD⁺ provider for CO₂ + H_2, whereas this function was strongly compensated by the transhydrogenase-like Nfn complex when CO was metabolized. Availability of reduced ferredoxin (Fd_red) can be considered as a key determinant of metabolic control. Oxidation of CO via carbon monoxide dehydrogenase (CODH) is the main route of Fd_red formation when CO is used as substrate, whereas Fd_red is mainly regenerated via the methyl branch of WLP and the Nfn complex utilizing CO₂ + H₂. Consequently, doubled growth rates, highest ATP formation rates and highest amounts of reduced products (ethanol, 2,3-butanediol) were observed when CO was the sole carbon and electron source.     

Alcoholic fermentation: modelling based on sole substrate and product measurement

Optimal automatic bioreactor control requires a mathematical model adapted to the potency of reliable sensors. A new relationship describing the kinetic behavior of alcoholic fermentation is discussed. By analogy with chemical kinetics, the biological rate of substrate consumption is related to substrate and product concentration by the following equation: \documentclass{article}\pagestyle{empty}\begin{document}$$r_s = kS;\alpha P;\beta$$\end{document} Using the well known yield relation between product and substrate, it is possible to describe in both batch and continuous cultures the ethanol and sugar concentrations versus time. This pattern has been successfully tested on several fermentations performed by yeasts (S. cerevisiae, S. bayanus, and S. cerevisiae sake) and a bacterium (Z. mobilis). This simple relationship is proposed as a tool for process control alcoholic fermentation.     

The influence of substrate transport limitation on porosity and methanogenic activity of anaerobic sludge granules

The relationship between porosity, diameter and methanogenic activity of anaerobic granules has been investigated. Experiments with different granular sludges revealed that substrate transport limitations increase with the diameter of the granules. As a consequence, autolysis can occur in the core of the granule, producing hallow granules. The porosity measurements revealed that the hollow centre is not available for substrate transport. Possibly as an effect of bacterial lysis, the porosity decreases in the more interior layers of the granules. This results in a inactive inner part of the large granules, which is not involved in the treatment process; the specific methanogenic activity decreases with granule size. No marked difference in substrate affinity is observed between granules of different sizes, which probably indicates that for large granules only the exterior is biological active. Correspondence to: G. Lettinga     

Glucose fermentation to acetate,CO2 and H2 in the anaerobic hyperthermophilic eubacterium Thermotoga maritima: involvement of the Embden-Meyerhof pathway

The hyperthermophilic anaerobic eubacterium Thermotoga maritima was grown on glucose as carbon and energy source. During growth 1 mol glucose was fermented to 2 mol acetate, 2 mol CO₂ and 4 mol H₂. The molar growth yicld on glucose (Y_glucose) was about 45 g cell dry mass/mol glucose. In the presence of elemental sulfur growing cultures of T. maritima converted 1 mol glucose to 2 mol acetate, 2 mol CO₂ about 0.5 mol H₂ and about 3.5 mol H₂S. Y_glucose was about 45 g/mol. Cell extracts contained all enzymes of the Embden-Meyerhof pathway: hexokinase (0.29 U/mg, 50°C), glucose-6-phosphate isomerase (0.56 U/mg, 50°C), phosphofructokinase (0.19 U/mg, 50° C), fructose-1,6-bisphosphate aldolase (0.033 U/mg, 50°C), triosephosphate isomerase (6.3 U/mg, 50°C), glyceraldehyde-3-phosphate dehydrogenase (NAD⁺ reducing: 0.63 U/mg, 50°C), phosphoglycerate kinase (3.7 U/mg, 50°C), phosphoglycerate mutase (0.4 U/mg, 50°C); enolase (4 U/mg, 80°C), pyruvate kinase (0.05 U/mg, 50°C). Furthermore, cell extracts contained pyruvate: ferredoxin oxidoreductasee (0.43 U/mg, 60°C); NADH: ferredoxin oxidoreductase (benzylviologen reduction: 0.46 U/mg, 80°C); hydrogenase (benzylviologen reduction: 15 U/mg, 80°C), phosphate acetyltransferase (0.13 U/mg, 80°C), acetate kinase (1.2 U/mg, 55°C), lactate dehydrogenase (0.16 U/mg, 80°C) and pyruvate carboxylase (0.02 U/mg, 50°C). The findings indicate that the hyperthermophilic eubacterium T. maritima ferments sugars (glucose) to acetate, CO₂ and H₂ involving the Embden-Meyerhof pathway, phosphate acetyltransferase and acetate kinase. Thus, the organism differs from the hyperthermophilic archaeon Pyrococcus furiosus which ferments sugars to acetate, CO₂ and H₂ involving a modified non-phosphorylated Entner-Doudoroff pathway and acetyl-CoA synthetase (ADP forming).     

Maltose fermentation to acetate,CO2 and H2 in the anaerobic hyperthermophilic archaeon Pyrococcus furiosus: evidence for the operation of a novel sugar fermentation pathway

The hyperthermophilic anaerobe Pyrococcus furiosus was grown on maltose as energy and carbon source. During growth 1 mol maltose was fermented to 3–4 mol acetate, 6–7 mol H₂ and 3–4 mol CO₂. The presence of the following enzyme activities in cell extracts of maltose-grown P. furiosus indicate that the sugar is degraded to pyruvate and H₂ by a modified non-phosphorylated Entner-Doudoroff-pathway (the values given in brackets are specific enzyme activities at 100 °C): Glucose: methyl viologen oxidoreductase (0.03 U/mg); 2-keto-3-deoxy-gluconate aldolase (0.03 U/mg); glyceraldehyde: benzyl viologen oxidoreductase (2.6 U/mg), glycerate kinase (2-phosphoglycerate forming) (0.48 U/mg), enolase (10.4 U/mg), pyruvate kinase (1.4 U/mg). Hexokinase, glucose-6-phosphate dehydrogenase, 2-keto-3-deoxy-6-phosphogluconate aldolase and phosphofructokinase could not be detected. Further conversion of pyruvate to acetate, CO₂ and H₂ involves pyruvate: ferredoxin oxidoreductase (0.4 U/mg; T=60°C with Clostridium pasteurianum ferredoxin as electron acceptor), hydrogen: methyl viologen ixodoreductase (3.4 U/mg) and ADP-dependent acetyl-CoA synthetase (1.9 U/mg). Phosphate acetyl transferase and acetate kinase could not be detected. The ADP-dependent acetyl-CoA synthetase catalyzes ATP synthesis via the mechanism of substrate level phosphorylation and apparently constitutes the only ATP conserving site during maltose catabolism in P. furiosus.This novel pathway of maltose fermentation to acetate, CO₂ and H₂ in the anaerobic archaeon P. furiosus may represent a phylogenetically ancient pathway of sugar fermentation.Non-standard abbreviations DTE dithioerythritol - MV methyl viologen - BV benzyl viologen - CHES cyclohexylamino-ethane sulfonic acid - ABTS 2,2-Azino-di-(3-ethylbenzthiazoliumsulfonate)     

Organic acid production from CO2/H2 and CO/H2 by mixed-culture anaerobes

The gases CO, CO₂, and H₂ were used as substrates in anaerobic fermentations producing organic acids. Various mixed bacterial sources were used, including sewage sludge digester effluent, rabbit feces, and soil. Nonsterile microorganism selection was carried out using CO₂/H₂ and CO/H₂ as the primary carbon and energy sources. Cultures were grown in specially designed, high-pressure (to 70 psig) flasks. Methanogenic bacteria were eliminated from the cultures. Liquid products of the fermentations were acetic through caproic acids, with the even-numbered acids predominating. Carbon balances showed conclusively that acetic acid was formed from carbon contained in the CO or CO₂ feed gas. Measurements made included rates of acid product formation, cell density, and degree of gas utilization. Limited characterization of the microorganisms was also performed. Production of organic acids by mixed culture inocula from CO₂/H₂ or CO/H₂ had not been reported previously. Application of this work is to the production of organic chemicals from synthesis gas (SNG), produced by the gasification of fossil fuels (peat, lignite, and various ranks of coals), biomass (agricultural and forest residues, and various biomass crops grown expressly for energy recovery), and municipal solid waste.     

1,3-丙二醇发酵中甘油代谢及产物抑制作用

对微生物法甘油转化成1,3-丙二醇过程中代谢规律及代谢控制的相关酶作以简述,并着重分析了丁酸梭菌发酵生产中乙酸、丁酸等副产物对细胞的抑制作用,对未来的研究发展方向进行了展望。     

Enumeration of bacteria forming acetate from H2 and CO2 in anaerobic habitats

A method has been worked out that allows the detection and isolation of bacteria fermenting molecular hydrogen and carbon dioxide to acetic acid.The ratio of methanogenic to acetogenic bacteria in sludge and lake sediment samples has been found to be approximately 100 to 1. Acetogenic bacteria could not be detected in rumen samples.     

DHA system mediating aerobic and anaerobic dissimilation of glycerol in Klebsiella pneumoniae NCIB 418.

In Klebsiella pneumoniae NCIB 418, the pathways normally responsible for aerobic growth on glycerol and sn-glycerol 3-phosphate (the glp system) are superrepressed. However, aerobic growth on glycerol can take place by the intervention of the NAD-linked glycerol dehydrogenase and the ATP-dependent dihydroxyacetone kinase of the dha system normally inducible only anaerobically by glycerol or dihydroxyacetone. Conclusive evidence that the dha system is responsible for both aerobic and anaerobic dissimilation of glycerol was provided by a Tn5 insertion mutant lacking dihydroxyacetone kinase. An enzymatically coupled assay specific for this enzyme was devised. Spontaneous reactivation of the glp system was achieved by selection for aerobic growth on sn-glycerol 3-phosphate or on limiting glycerol as the sole carbon and energy source. However, the expression of this system became constitutive. Aerobic operation of the glp system highly represses synthesis of the dha system enzymes by catabolite repression.     

The influence of H2, CO2 and dilution rate on the continuous fermentation of acetone-butanol

Summary The effect of product gases, H₂ and CO₂, on solvent production was studied using a continuous culture of alginate-immobilized Clostridium acetobutylicum. Initially, in order to find the optimum dilution rate for aceton--butanol production in this system, fermentations were carried out at various dilution rates. With 10% H₂ and 10% CO₂ in the sparging gas, a dilution rate of 0.07 h^–1 was found to maximize volumetric productivity (0.58 g·l^–1·h^–1), while the maximum specific productivity of 0.27 g^–·h^–1 occured at 0.12 h^–1. Continuous cultures with vigorous sparging of N₂ produced only acids. It was concluded that in the case of continuous fermentation H₂ is essential for good solvent production, although good solvent production is possible in an H₂-absent environment in the case of batch fermentations. When the fermentation was carried out at atmospheric pressure under H₂-enriched conditions, the presence of CO₂ in the sparging gas did not slow down glucose metabolism; rather it changed the direction of the phosphoroclastic reaction and as a result increased the butanol/acetone ratio.     

Effects of glycerol on alcohol fermentation. Inhibition mechanism and diffusion limitations

Batch alcohol fermentations have been carried out varying the starting level of glycerol in the broth and keeping constant all the other fermentation parameters, in order to study the effect of the accumulation of this metabolite on the fermentation kinetics. A linear slow decrease of the maximum specific ethanol productivity with increasing glycerol level has been followed by a sharp fall of this parameter over a glycerol concentration threshold. A kinetic study through unstructured integrated models demonstrates that, at low concentrations, glycerol behaves as a non competitive inhibitor of fermentation, while, over a concentration threshold (105 kg/m³), an additional effect takes place, likely ascribable to diffusion limitations provoked by excess viscosity of the broth.