一株高效降解木糖的耐酸、嗜热厌氧杆菌的生理特性及产物分析

【目的】分离高效降解木糖的嗜热厌氧杆菌菌株,用于发酵生产生物燃料乙醇,为后继的构建基因工程菌株及联合生物工艺提供材料。【方法】运用亨盖特厌氧操作技术从胜利油田油层采出液两年的富集样中分离到一株嗜热厌氧杆菌xyl-d。采用形态学观察、生理生化指标鉴定及基于16S rRNA的系统发育学分析确定其分类地位。【结果】菌株xyl-d为革兰氏阴性厌氧杆菌,菌体大小为(1.35-5.08)μm×(0.27-0.40)μm,单生、成对或成簇生长,芽胞圆形,端生。温度生长范围30-85℃(最适温度65℃);pH范围3.0-10.0(最适pH 7.5);NaCl浓度范围0%-4%(最适NaCl浓度2.0%)。发酵D-木糖的产物是乙醇、乙酸、CO2及少量的异丁醇、丙酸。菌株xyl-d的(G+C)mol%含量为45.6%,与热厌氧杆菌属模式菌株威吉利热厌氧杆菌(Thermoanaerobacter wiegelii)DSM10319T及嗜热乙醇杆菌(Thermoanaerobacter ethanolicus)DSM2246T的16S rRNA序列相似性均为99.3%。菌株利用D-木糖产乙醇的最佳初始pH为8.5;少量酵母粉能刺激生长并显著提高发酵D-木糖的产醇率,使乙醇成为主要的发酵产物;培养基中乙醇浓度达到7%(V/V)时菌体生长受到抑制,最佳生长条件下D-木糖的降解率可达91.37%,最佳产醇条件下发酵1摩尔D-木糖可产生1.29摩尔的乙醇。【结论】菌株xyl-d是从特殊生境(油藏)中分离到的一株高效降解D-木糖的耐酸、嗜热的厌氧杆菌,其为半纤维素降解产乙醇的联合生物工艺提供了菌源。     

Bacterial conversion of glycerol to beta-hydroxypropionaldehyde

beta-hydroxypropionaldehyde (3-HPA) can be oxidized to acrylic acid, an industrially important chemical used in the manufacture of synthetic plastics and other polymers. Of 19 genera and 55 strains tested, 3 Klebsiella and 2 Enterobacter strains produced 3-HPA. The most efficient strain was Klebsiella pneumoniae NRRL B-4011. Under optimum conditions (28 degrees C; 40 g of semicarbazide hydrochloride per liter, 70 g of glycerol per liter; and pH 6.0), 3.1 g of B-4011 cells per liter accumulated 22 g of 3-HPA per liter at a specific rate of 0.83 g/g per h; however, 14.5 g of cells per liter accumulated 46 g of 3-HPA per liter at a specific rate of 0.41 g/g per h.     

Co-cultivation of the anaerobic fungus Anaeromyces robustus with Methanobacterium bryantii enhances transcription of carbohydrate active enzymes

Journal of Industrial Microbiology & Biotechnology - Anaerobic gut fungi are biomass degraders that form syntrophic associations with other microbes in their native rumen environment. Here,...     

Bacterial conversion of glycerol to beta-hydroxypropionaldehyde.

beta-hydroxypropionaldehyde (3-HPA) can be oxidized to acrylic acid, an industrially important chemical used in the manufacture of synthetic plastics and other polymers. Of 19 genera and 55 strains tested, 3 Klebsiella and 2 Enterobacter strains produced 3-HPA. The most efficient strain was Klebsiella pneumoniae NRRL B-4011. Under optimum conditions (28 degrees C; 40 g of semicarbazide hydrochloride per liter, 70 g of glycerol per liter; and pH 6.0), 3.1 g of B-4011 cells per liter accumulated 22 g of 3-HPA per liter at a specific rate of 0.83 g/g per h; however, 14.5 g of cells per liter accumulated 46 g of 3-HPA per liter at a specific rate of 0.41 g/g per h.     

Microbial conversion of glycerol to 1,3-propanediol

Abstract: Glycerol produced by cleavage of natural fats can microbially be converted to 1,3-propanediol (PD) by Citrobacter, Klebsiella and Clostridia strains. The fermentation by C. butyricum , product recovery and purification has been investigated in detail up to the 2 m³ scale. Estimation of product costs for a 10,000 t/a plant indicates that the microbial process is obviously more attractive than the chemical route. Presently, 1,3-propanediol has only a low market volume; however, its use for special polycondensates, in particular polyesters, could reduce glycerol surpluses and make plastics a easily biodegradable part of natural cycles.     

Dominant sugar utilizers in sediment of Lake Constance depend on syntrophic cooperation with methanogenic partner organisms

Six strains of novel bacteria were isolated from profundal sediment of Lake Constance, a deep freshwater lake in Germany, by direct dilution of the sediment in mineral agar medium containing a background lawn of the hydrogen-scavenging Methanospirillum hungatei as a syntrophic partner. The numbers of colony-forming units obtained after incubation for more than 2 months were in the same range as those of total bacterial counts determined by DAPI staining (up to 10(8) cells per millilitre) suggesting that these organisms were dominant members of the community. Identical dilution series in the absence of methanogenic partners yielded numbers that were lower by two to three orders of magnitude. The dominant bacteria were isolated in defined co-culture with M. hungatei, and were further characterized. Growth was slow, with doubling times of 22-28 h at 28 degrees C. Cells were small, 0.5 x 5 microm in size, Gram-positive, and formed terminal oval spores. At 20 degrees C, glucose was fermented by the co-culture strain BoGlc83 nearly stoichiometrically to 2 mol of acetate and 1 mol of methane plus CO(2). At higher temperatures, also lactate and traces of succinate were formed. Anaerobic growth depended strictly on the presence of a hydrogen-scavenging partner organism and was inhibited by bromoethane sulfonate, which together indicate the need for a syntrophic partnership for this process. Strain BoGlc83 grew also aerobically in the absence of a partner organism. All enzymes involved in ATP formation via glycolysis and acetyl CoA were found, most of them at activities equivalent to the physiological substrate turnover rate. This new type of sugar-fermenting bacterium appears be the predominant sugar utilizer in this environment. The results show that syntrophic relationships can play an important role also for the utilization of substrates which otherwise can be degraded in pure culture.     

Optimizing aerobic conversion of glycerol to 3-hydroxypropionaldehyde

When cells of Klebsiella pneumoniae NRRL B-199 (ATCC 8724) were grown aerobically on a rich glycerol medium and then suspended in buffer supplemented with semicarbazide and glycerol, aerobic conversion of glycerol to 3-hydroxypropionaldehyde (3-HPA) ensued. Depending on conditions, 0.38 to 0.67 g of 3-HPA were formed per gram of glycerol consumed. This means that up to 83.8% of the carbon invested as glycerol could potentially be recovered as the target product, 3-HPA. Production of 3-HPA was sensitive to the age of cells harvested for resuspension and was nonexistent if cells were cultivated on glucose instead of glycerol as the sole carbon source. Compared with 24- and 72-h cells, 48-h cells produced 3-HPA at the highest rate and with the greatest yield. The cell biomass concentration present during the fermentation was never particularly critical to the 3-HPA yield, but initial fermentation rates and 3-HPA accumulation displayed a linear dependence on biomass concentration that faded when biomass exceeded 3 g/liter. Fermentation performance was a function of temperature, and an optimum initial specific 3-HPA productivity occurred at 32 degrees C, although the overall 3-HPA yield increased continuously within the 25 to 37 degrees C range studied. The pH optimum based on fermentation rate was different from that based on overall yield; 8 versus 7, respectively. Initial glycerol concentrations in the 20 to 50 g/liter range optimized initial 3-HPA productivity and yield.     

Hydrogen cycling in a three-tiered food web growing on the methanogenic conversion of 3-chlorobenzoate

Abstract A defined 3-chlorobenzoate-degrading methanogenic consortium was constructed by recombining key organisms isolated from a 3-chlorobenzoate-degrading methanogenic sludge enrichment. The organisms comprise a three-tiered food chain which includes: (1) reductive dechlorination of 3-chlorobenzoate; (2) oxidation of benzoate to acetate, H₂ and CO₂; (3) removal of H₂ plus CO₂ by conversion into methane. The defined consortium, consisting of a dechlorinating organism (DCB-1), a benzoate degrader (BZ-1) and a lithotrophic methanogen ( Methanospirillum strain PM-1) grew well in a basal salts medium supplemented with 3-chlorobenzoate (3.2 mM) as the sole energy source. The chlorine released from the aromatic ringe was recovered in stoichiometric amounts as the chloride ion. The reducing power required for reductive dechlorination was obtained from the hydrogen produced in the acetogenic oxidation of benzoate. One-third of the benzoate-derived hydrogen was recycled via the reductive dechlorination of 3-chlorobenzoate, indicating that the consortium operated as a food web rather than a food chain.     

Metabolism of biodiesel-derived glycerol in probiotic Lactobacillus strains

Three probiotic Lactobacillus strains, Lactobacillus acidophilus, Lactobacillus plantarum, and Lactobacillus delbrueckii, were tested for their ability to assimilate and metabolize glycerol. Biodiesel-derived glycerol was used as the main carbon and energy source in batch microaerobic growth. Here, we show that the tested strains were able to assimilate glycerol, consuming between 38 and 48 % in approximately 24 h. L. acidophilus and L. delbrueckii showed a similar growth, higher than L. plantarum. The highest biomass reached was 2.11 g?L^?1 for L. acidophilus, with a cell mass yield (Y _X/S) of 0.37 g?g^?1. L. delbrueckii and L. plantarum reached a biomass of 2.06 and 1.36 g?L^?1. All strains catabolize glycerol mainly through glycerol kinase (EC 2.7.1.30). For these lactobacillus species, kinetic parameters for glycerol kinase showed Michaelis–Menten constant (K _m) ranging from 1.2 to 3.8 mM. The specific activities for glycerol kinase in these strains were in the range of 0.18 to 0.58 U?mg?protein^?1, with L. acidophilus ATCC 4356 showing the maximum specific activity after 24 h of cultivation. Glycerol dehydrogenase activity was also detected in all strains studied but only for the reduction of glyceraldehyde with NADPH (K _m for DL-glyceraldehyde ranging from 12.8 to 32.3 mM). This enzyme shows a very low oxidative activity with glycerol and NADP⁺ and, most likely, under physiological conditions, the oxidative reaction does not occur, supporting the assumption that the main metabolic flux concerning glycerol metabolism is through the glycerol kinase pathway.     

Optimizing aerobic conversion of glycerol to 3-hydroxypropionaldehyde.

When cells of Klebsiella pneumoniae NRRL B-199 (ATCC 8724) were grown aerobically on a rich glycerol medium and then suspended in buffer supplemented with semicarbazide and glycerol, aerobic conversion of glycerol to 3-hydroxypropionaldehyde (3-HPA) ensued. Depending on conditions, 0.38 to 0.67 g of 3-HPA were formed per gram of glycerol consumed. This means that up to 83.8% of the carbon invested as glycerol could potentially be recovered as the target product, 3-HPA. Production of 3-HPA was sensitive to the age of cells harvested for resuspension and was nonexistent if cells were cultivated on glucose instead of glycerol as the sole carbon source. Compared with 24- and 72-h cells, 48-h cells produced 3-HPA at the highest rate and with the greatest yield. The cell biomass concentration present during the fermentation was never particularly critical to the 3-HPA yield, but initial fermentation rates and 3-HPA accumulation displayed a linear dependence on biomass concentration that faded when biomass exceeded 3 g/liter. Fermentation performance was a function of temperature, and an optimum initial specific 3-HPA productivity occurred at 32 degrees C, although the overall 3-HPA yield increased continuously within the 25 to 37 degrees C range studied. The pH optimum based on fermentation rate was different from that based on overall yield; 8 versus 7, respectively. Initial glycerol concentrations in the 20 to 50 g/liter range optimized initial 3-HPA productivity and yield.     

Enzymatic conversion of D-galactose to D-tagatose: heterologous expression and characterisation of a thermostable L-arabinose isomerase from Thermoanaerobacter mathranii

The ability to convert d-galactose into d-tagatose was compared among a number of bacterial l-arabinose isomerases (araA). One of the most efficient enzymes, from the anaerobic thermophilic bacterium Thermoanaerobacter mathranii, was produced heterologously in Escherichia coli and characterised. Amino acid sequence comparisons indicated that this enzyme is only distantly related to the group of previously known araA sequences in which the sequence similarity is evident. The substrate specificity and the Michaelis–Menten constants of the enzyme determined with l-arabinose, d-galactose and d-fucose also indicated that this enzyme is an unusual, versatile l-arabinose isomerase which is able to isomerise structurally related sugars. The enzyme was immobilised and used for production of d-tagatose at 65 °C. Starting from a 30% solution of d-galactose, the yield of d-tagatose was 42% and no sugars other than d-tagatose and d-galactose were detected. Direct conversion of lactose to d-tagatose in a single reactor was demonstrated using a thermostable -galactosidase together with the thermostable l-arabinose isomerase. The two enzymes were also successfully combined with a commercially available glucose isomerase for conversion of lactose into a sweetening mixture comprising lactose, glucose, galactose, fructose and tagatose.     

Immobilization of glycerol dehydrogenase on magnetic silica nanoparticles for conversion of glycerol to value-added 1,3-dihydroxyacetone

Abstract

Glycerol dehydrogenase (GlyDH) which oxidizes glycerol to the value-added chemical, 1,3-dihydroxyacetone, is of interest due to the oversupply of glycerol as a by-product of the biodiesel industry. To exploit the enzymatic oxidation of glycerol industrially, silica coated magnetic Fe₃O₄ nanoparticles were prepared and then activated with an amino-silane reagent for covalent immobilization of GlyDH via a glutaraldehyde linkage. At the optimal glutaraldehyde concentration of 0.05% (v/v), an enzyme loading of up to 57.5 mg/g-nanoparticles was achieved with 81.1% of the original activity retained. Reaction kinetic analysis indicated that the immobilized GlyDH had almost the same Michaelis-Menten constants for both NAD⁺ and glycerol as the free GlyDH did. However, after immobilization the turnover number k_cat of the GlyDH decreased from 164 s^?1 to 113 s^?1, and the reaction was 1.3-fold less sensitive to inhibition by DHA, which could compensate the decrease in k_cat. The immobilized GlyDH was also less sensitive to changes in pH and temperature, and showed a 5.3-fold improvement in thermal stability at 50^°C. Furthermore, excellent reusability was observed such that 10 cycles of re-use only led to 9% loss of enzyme activity.     

Uptake and dissimilation of glycerol by wild type and glycerol nonutilizing strains of Neurospora crassa

Summary Seven mutant strains defective for utilization of glycerol, glyceraldehyde or dihydroxyacetone were isolated. One strain was deficient for NAD-linked glycerol-3-phosphate dehydrogenase, two for glycerol kinase, and four had no detected enzymatic deficiency, although one of the latter strains was deficient in glycerol uptake. Glycerol uptake was increased by incubation in glycerol, glycerol-3-phosphate, erythritol, and propanediol, and was protein-mediated below 0.14 mM glycerol, but at higher concentrations free diffusion predominated. Glycerol uptake was decreased by cycloheximide and was more sensitive to sodium azide than to iodoacetate.     

Fast conversion of glycerol to 1,3-propanediol by a new strain of Klebsiella pneumoniae

Five bacterial strains screened from a batch of 39 samples could convert glycerol anaerobically to 1,3-propanediol (1,3-PD). One of the strains, XJ-Li, which could synthesize 1,3-PD with a higher concentration, was identified and characterized. Phylogenetic analysis of the strain XJ-Li included the study of morphology, physiological and biochemical characteristics. In addition, 16SrDNA sequences were created. The results indicated that this strain is a member of Klebsiella pneumoniae. The optimal cultivation parameters for pH and temperature were determined as 8.0 and 40 °C, respectively. The optimized nitrogen source and carbon source were 6.0 g/L of (NH₄)₂SO₄ and 20 g/L of glycerol, respectively. After 8 h in batch fermentation, both the 1,3-PD concentration and glycerol consumption reached the maximum, with 12.2 g/L of 1,3-PD and 1.53 g/L h of productivity, and a molar yield of 1,3-PD to glycerol of 0.75. Fed-batch fermentation also indicated a higher molar yield of 0.70, and the concentration of 1,3-PD reached 38.1 g/L after 66.4 g/L of glycerol consumption. The results of batch and fed-batch fermentations demonstrated that K. pneumoniae XJ-Li would be an excellent 1,3-PD producer.     

Microbial conversion of glycerol: present status and future prospects

Biodiesel has emerged as a potential alternate renewable liquid fuel in the past two decades. Total annual production of biodiesel stands at 6.96 million tons and 11.2 million tons in USA and Europe, respectively. In other countries, Asia and Latin America, biodiesel production has increased at unprecedented rate. Despite this, the economy of biodiesel is not attractive. An obvious solution for boosting the economy of the biodiesel industry is to look for markets for side products of the transesterification process of biodiesel synthesis. The main by-product is glycerol. However, this glycerol is contaminated with alkali/acid catalyst and alcohol, and thus, is not useful for conventional applications such as in toothpaste, drugs, paints and cosmetics. Conversion of this glycerol to value-added product is a viable solution for effective and economic utilization, which would also generate additional revenue for the biodiesel industry. Intensive research has taken place in area of conversion of glycerol to numerous products. The conventional catalytic route of glycerol transformation employs prohibitively harsh conditions of temperature and pressure, and thus, has slim potential for large-scale implementation. In addition, the selectivity of the process is rather small with formation of many undesired side products. The bioconversion processes, on the other hand, are highly selective although with slower kinetics. In this review, we have given an assessment and overview of the literature on bioconversion of glycerol. We have assessed as many as 23 products from glycerol bioconversion, and have reviewed the literature in terms of microorganism used, mode of fermentation, type of fermentor, yield and productivity of the process and recovery/purification of the products. The metabolic pathway of conversion of glycerol to various products has been discussed. We have also pondered over economic and engineering issues of large-scale implementation of process and have outlined the constraints and limitations of the process. We hope that this review will be a useful source of information for biochemists, biotechnologists, microbiologists and chemical engineers working in the area of glycerol bioconversion.     

Spotlight on biodiversity of microbial cell factories for glycerol conversion

Plant oil based industrial oleochemistry leads to a large side stream of crude glycerol, which offers itself as a low price carbon source for microbial chemical production. Compared to sugar, glycerol is more reduced and less microorganisms are able to use it as carbon source. An interesting feature of glycerol conversion is that many organisms cannot use it as carbon source at all, but they readily use it as electron sink under anaerobic conditions. In any case the number of pathways by which glycerol enters the microbial metabolism is quite limited. Having said this, an interesting variety of products of industrial relevance is accumulated by naturally occurring microorganisms which can use glycerol. These chemicals range from fuels and solvents to polymer precursors up to food additives. The limited number of metabolic pathways and the manageable amount of products allow to highlight the importance of tapping the outstanding resource of biodiversity for industrial purposes. The interplay of microbial biodiversity, metabolic engineering and bioprocess engineering is key for economic success in industrial microbiology. In this article we shed light on the biodiversity of naturally glycerol consuming microorganisms and their impact and importance on microbial chemical production.     

Steps in the conversion of alpha-ketosuberate to 7-mercaptoheptanoic acid in methanogenic bacteria

The biosynthetic steps involved in the conversion of alpha-ketosuberate to 7-mercaptoheptanoic acid were studied in cell-free extracts of methanogenic bacteria. The pathway was established by measuring the incorporation of stable isotopically labeled precursors into the S-methyl ether methyl ester derivative of the enzymatically generated 7-mercaptoheptanoic acid by using gas chromatography-mass spectrometry (GC-MS). Quantitation of the 7-mercaptoheptanoic acid produced in the incubations with the substrates was accomplished by using an internal standard of 6-mercaptohexanoic acid. [4,4,6,6-2H4]-2-Oxosuberic acid, [7-2H]-7-oxoheptanoic acid, [2-2H]-2(RS)-(5-carboxypentyl)thiazolidine-4(R)-carboxylic acid, and S-(6-carboxyhexyl)cysteine were each shown to be converted to 7-mercaptoheptanoic acid. Incubation of cell extracts with a mixture of 2(RS)-(5-carboxypentyl)thiazolidine-4(R)-carboxylic acid and [2-2H]-2-(RS)-(5-carboxypentyl)-[34S]thiazolidine-4(R)-carboxylic acid showed that both 34S and 2H are incorporated into the 7-mercaptoheptanoic acid but only after separation of the cysteine from the [7-2H]-7-oxyheptanoic acid portion of the molecule. Furthermore, the sulfur from the cysteine was incorporated into the thiol only after its elimination from the cysteine and subsequent mixing with an unlabeled sulfur source which had a molecular weight of sufficient size that it was excluded from Sephadex G-25. Hydrogen sulfide was found to supply the sulfur for the production of the 7-mercaptoheptanoic acid in a reaction that was shown to obtain its reducing equivalents from hydrogen via an F420-dependent hydrogenase.     

Microbial conversion of glycerol: present status and future prospects

Biodiesel has emerged as a potential alternate renewable liquid fuel in the past two decades. Total annual production of biodiesel stands at 6.96 million tons and 11.2 million tons in USA and Europe, respectively. In other countries, Asia and Latin America, biodiesel production has increased at unprecedented rate. Despite this, the economy of biodiesel is not attractive. An obvious solution for boosting the economy of the biodiesel industry is to look for markets for side products of the transesterification process of biodiesel synthesis. The main by-product is glycerol. However, this glycerol is contaminated with alkali/acid catalyst and alcohol, and thus, is not useful for conventional applications such as in toothpaste, drugs, paints and cosmetics. Conversion of this glycerol to value-added product is a viable solution for effective and economic utilization, which would also generate additional revenue for the biodiesel industry. Intensive research has taken place in area of conversion of glycerol to numerous products. The conventional catalytic route of glycerol transformation employs prohibitively harsh conditions of temperature and pressure, and thus, has slim potential for large-scale implementation. In addition, the selectivity of the process is rather small with formation of many undesired side products. The bioconversion processes, on the other hand, are highly selective although with slower kinetics. In this review, we have given an assessment and overview of the literature on bioconversion of glycerol. We have assessed as many as 23 products from glycerol bioconversion, and have reviewed the literature in terms of microorganism used, mode of fermentation, type of fermentor, yield and productivity of the process and recovery/purification of the products. The metabolic pathway of conversion of glycerol to various products has been discussed. We have also pondered over economic and engineering issues of large-scale implementation of process and have outlined the constraints and limitations of the process. We hope that this review will be a useful source of information for biochemists, biotechnologists, microbiologists and chemical engineers working in the area of glycerol bioconversion.     

High yield conversion of a crude glycerol fraction from biodiesel production to hydrogen by photofermentation

Present biodiesel manufacturing processes inevitably produce a crude glycerol side fraction. Projected future volumes of biodiesel will generate enormous quantities of glycerol of a magnitude suggesting that conversion to a fuel is the only viable route. Here we have shown that the photosynthetic bacterium Rhodopseudomonas palustris is capable of the photofermentative conversion of glycerol, both pure and a crude glycerol fraction, to hydrogen, a proposed future fuel. Relatively high yields, up to 6 moles H₂/mole glycerol (75% of theoretical, 8 moles of H₂/mole glycerol) were obtained. Even the crude glycerol fraction, at the concentrations used here, was readily converted to hydrogen with no apparent evidence of inhibition or toxicity. We show that the concentration of added nitrogen can be used to modify both rates and yields of hydrogen production with an apparent trade-off between the two. Finally, some factors are identified that might be examined in future studies in attempts to increase rates and/or yields.