Effect of aerobically generated inoculum on xylose fermentation by an ethanologenic recombinantE. coli

Summary The anaerobic conversion of xylose to ethanol by a genetically engineredE. coli B (pLOI297) was investigated using anaerobically and aerobically grown cultures as inocula. Using anaerobically grown cells, an increase in the inoculation density from 50 to 340 mg dry wt. cells/L resulted in an increase in the overall volumetric productivity from 0.57 to 0.71 g/L/h. At the higher inoculation density, substitution of the anaerobic inoculum by aerobically grown cells resulted in a 15% reduction in volumetric productivity (0.61 g/L/h) that was caused by the introduction of a lag period during which the aerobic inoculum adapted to the anaerobic environment. In all cases, the ethanol yield from xylose approached the theoretical maximum and seemed unaffected by the physiological history of the inoculum with respect to aeration. It is concluded that aeration should be avoided in the production of high performance starter cultures.     

Loss of ethanologenicity in Escherichia coli B recombinants pLOI297 and KO11 during growth in the absence of antibiotics

Summary The two cultures under investigation were genetically engineered for the purpose of producing fuel ethanol from biomass and wastes. In this study, stability was viewed in pragmatic terms whereby the fermentation performance of the different genetic constructs was assessed solely with respect to their capacity to maintain a high efficiency of sugar-to-ethanol conversion. Two serial transfers of test tube batch cultures accounted for about 12 generations of semi-continuous growth in LB medium containing one of 4 different sugars - glucose, galactose, mannose or xylose. Both the plasmid-bearing recombinant E. coli B (ATCC 11303) pLOI297 and the chromosomally-integrated recombinant KO11 exhibited dramatic loss of ethanologenicity during growth in a selective (antibiotic-supplemented) medium with mannose as fermentation substrate. In the absence of antibiotics, both recombinants exhibited instability, with the exception of KO11 with xylose as substrate. These observations with short term cultures call into question previous claims regarding the stability of these genetic constructs.     

Kinetic modeling of Candida shehatae ATCC 22984 on xylose and glucose for ethanol production

Candida shehatae ATCC 22984, a xylose-fermenting yeast, showed an ability to produce ethanol in both glucose and xylose medium. Maximum ethanol produced by the yeast was 48.8?g/L in xylose and 52.6?g/L in glucose medium with ethanol yields that varied between 0.3 and 0.4?g/g depended on initial sugar concentrations. Xylitol was a coproduct of ethanol production using xylose as substrate, and glycerol was detected in both glucose and xylose media. Kinetic model equations indicated that growth, substrate consumption, and product formation of C. shehatae were governed by substrate limitation and inhibition by ethanol. The model suggested that cell growth was totally inhibited at 40?g/L of ethanol and ethanol production capacity of the yeast was 52?g/L, which were in good agreement with experimental results. The developed model could be used to explain C. shehatae fermentation in glucose and xylose media from 20 to 170?g/L sugar concentrations.     

Single step conversion of cellulose to ethanol by a mesophilic coculture

Summary A coculture consisting of two mesophilic anaerobes, produced about 0.8 mole of ethanol per mole of cellulose from a variety of cellulosic materials. The non-cellulolytic member of this coculture, Clostridium saccharolyticum sp. nov. converted glucose and xylose to ethanol and acetic acid in ratios over 4 to 1.     

Extractive bioconversion in aqueous two-phase systems. A model study on the conversion of cellulose to ethanol

Summary Aqueous two-phase systems composed of dextran and poly (ethylene glycol) have been successfully used for glucose fermentation, cellulose hydrolysis and bioconversion of cellulose to ethanol. The biocatalysts are confined in the bottom phase whereas the products are extracted by the top phase.     

Engineering Escherichia coli for the efficient conversion of glycerol to ethanol and co-products

Given its availability, low prices, and high degree of reduction, glycerol has become an ideal feedstock for producing reduced compounds via anaerobic fermentation. We recently identified environmental conditions enabling the fermentative metabolism of glycerol in E. coli, along with the pathways and mechanisms mediating this metabolic process. In this work, we used the knowledge base created in previous studies to engineer E. coli for the efficient conversion of crude glycerol to ethanol. Our strategy capitalized on the high degree of reduction of carbon in glycerol, thus enabling the production of not only ethanol but also co-products hydrogen and formate. Two strains were created for the co-production of ethanol-hydrogen and ethanol-formate: SY03 and SY04, respectively. High ethanol yields were achieved in both strains by minimizing the synthesis of by-products succinate and acetate through mutations that inactivated fumarate reductase (DeltafrdA) and phosphate acetyltransferase (Deltapta), respectively. Strain SY04, which produced ethanol-formate, also contained a mutation that inactivated formate-hydrogen lyase (DeltafdhF), thus preventing the conversion of formate to CO(2) and H(2). High rates of glycerol utilization and product synthesis were achieved by simultaneous overexpression of glycerol dehydrogenase (gldA) and dihydroxyacetone kinase (dhaKLM), which are the enzymes responsible for the conversion of glycerol to glycolytic intermediate dihydroxyacetone phosphate. The resulting strains, SY03 (pZSKLMgldA) and SY04 (pZSKLMgldA), produced ethanol-hydrogen and ethanol-formate from unrefined glycerol at yields exceeding 95% of the theoretical maximum and specific rates in the order of 15-30 mmol/gcell/h. These yields and productivities are superior to those reported for the conversion of glycerol to ethanol-H(2) or ethanol-formate by other organisms and equivalent to those achieved in the production of ethanol from sugars using E. coli.     

Efficient ethanol production from glucose, lactose, and xylose by recombinant Escherichia coli.

Lactose and all of the major sugars (glucose, xylose, arabinose, galactose, and mannose) present in cellulose and hemicellulose were converted to ethanol by recombinant Escherichia coli containing plasmid-borne genes encoding the enzymes for the ethanol pathway from Zymomonas mobilis. Environmental tolerances, plasmid stability, expression of Z. mobilis pyruvate decarboxylase, substrate range, and ethanol production (from glucose, lactose, and xylose) were compared among eight American Type Culture Collection strains. E. coli ATCC 9637(pLO1297), ATCC 11303(pLO1297), and ATCC 15224(pLO1297) were selected for further development on the basis of environmental hardiness and ethanol production. Volumetric ethanol productivities per hour in batch culture were 1.4 g/liter for glucose (12%), 1.3 g/liter for lactose (12%), and 0.64 g/liter for xylose (8%). Ethanol productivities per hour ranged from 2.1 g/g of cell dry weight with 12% glucose to 1.3 g/g of cell dry weight with 8% xylose. The ethanol yield per gram of xylose was higher for recombinant E. coli than commonly reported for Saccharomyces cerevisiae with glucose. Glucose (12%), lactose (12%), and xylose (8%) were converted to (by volume) 7.2% ethanol, 6.5% ethanol, and 5.2% ethanol, respectively.     

Application of a compatible xylose isomerase in simultaneous bioconversion of glucose and xylose to ethanol

Simultaneous isomerisation and fermentation (SIF) of xylose and simultaneous isomerisation and cofermentation (SICF) of glucose-xylose mixture was carried out by the yeastSaccharomyces cerevisiae in the presence of a compatible xylose isomerase. The enzyme converted xylose to xylulose andS. cerevisiae fermented xylulose, along with glucose, to ethanol at pH 5.0 and 30°C. This compatible xylose isomerase fromCandida boidinii, having an optimum pH and temperature range of 4.5–5.0 and 30–50°C respectively, was partially purified and immobilized on an inexpensive, inert and easily available support, hen egg shell. An immobilized xylose isomerase loading of 4.5 IU/(g initial xylose) was optimum for SIF of xylose as well as SICF of glucose-xylose mixture to ethanol byS. cerevisiae. The SICF of 30 g/L glucose and 70 g xylose/L gave an ethanol concentration of 22.3 g/L with yield of 0.36 g/(g sugar consumed) and xylose conversion efficiency of 42.8%.     

Thermodynamics of the conversion of aqueous xylose to xylulose

The thermodynamics of the conversion of aqueous xylose to xylulose has been investigated using high-pressure liquid chromatography (HPLC) and microcalorimetry. The reaction was carried out in aqueous phosphate buffer over the pH range 6.8-7.4 using solubilized glucose isomerase with MgSO(4) as a cofactor. The temperature range over which this reaction was investigated was 298.15-342.15 K. A combined analysis of both the HPLC and microcalorimetric data leads to the following results at 298.15 K for the conversion process: DeltaG degrees = 4389 +/- 31 J mol(-1), DeltaH degrees = 16090 +/- 670 J mol(-1), and DeltaC(p) degrees = 40 +/- 23 J mol(-1) K(-1). The temperature dependence of the equilibrium constant for the reaction is expressed as R ln K = -4389/298.15 +16090[(1/298.15)-(1/T)]+40[(298.15/T)-1 + ln(T/298.15)]. Comparisons are made with literature data.     

Simultaneous bioconversion of glucose and xylose to ethanol by Saccharomyces cerevisiae in the presence of xylose isomerase

Simultaneous isomerisation and fermentation (SIF) of xylose and simultaneous isomerisation and cofermentation (SICF) of a glucose/xylose mixture was carried out by Saccharomyces cerevisiae in the presence of xylose isomerase. The SIF of 50 g l⁻¹ xylose gave an ethanol concentration and metabolic yield of 7.5 g l⁻¹ and 0.36 g (g xylose consumed)⁻¹. These parameters improved to 13.4 g l⁻¹ and 0.40 respectively, when borate was added to the medium. The SICF of a mixture of 50 g l⁻¹ glucose and 50 g l⁻¹ xylose gave an ethanol concentration and metabolic yield of 29.8 g l⁻¹ and 0.42 respectively, in the presence of borate. Temperature modulation from 30 °C to 35 °C during fermentation further enhanced the above parameters to 39 g l⁻¹ and 0.45 respectively. The approach was extended to the bioconversion of sugars present in a real lignocellulose hydrolysate (peanut-shell hydrolysate) to ethanol, with a fairly good yield. Received: 14 May 1999 / Received revision: 27 September 1999 / Accepted: 2 October 1999     

A one step process for the conversion of cellulose to ethanol using anaerobic microorganisms in mono- and co-culture

Summary The reducing sugars, glucose, and ethanol produced during growth of the anaerobes Clostridium thermocellum and Acetivibrio cellulolyticus on cellulose were assayed. Zymomonas mobilis was grown under similar conditions and could ferment glucose to ethanol. The ethanol production by the cellulolytic bacteria alone and in co-culture with Zymomonas is described. Approximately 27% of a 1% cellulose substrate could be converted to ethanol by this co-culture.     

Hydrolysis of xylan and fermentation of xylose to ethanol

The focus in the development of pulping processes has usually been exclusively on cellulose. However, hemicellulose could serve as a valuable source of hexose and pentose sugars. Consequently, it should not be destroyed in a process designed for very high cellulose fibre yields. Novel procedures developed for production of ethanol by the fermentation of pentoses as well as hexoses provide new possibilities of hemicellulose utilization.

Many fungi produce extracellular hemicellulases. In the present work the production of xylanase and β-xylosidase with strains of Aspergillus and Trichoderma was studied. The enzymes were used for the hydrolysis of xylan. Xylose was fermented to ethanol by the mold Fusarium oxysporum.     

Characterization of the steam-exploded spent Shiitake mushroom medium and its efficient conversion to ethanol

Spent Shiitake mushroom medium was subjected to steam explosion followed by simultaneous saccharification and fermentation (SSF) using Meicelase and Saccahromyces cerevisiae AM12. Water extraction of the medium exposed to steam at 20 atm for 5 min enhanced the saccharification rate by about 20% compared to steam-exploded medium before water extraction and resulted in the production of 23.8 g/l ethanol from a substrate concentration of 100 g/l. This corresponded to 87.6% of the theoretical ethanol yield, i.e., 15.9 g ethanol was obtained from 100 g of spent Shiitake mushroom medium. Spent Shiitake mushroom medium subjected to steam explosion and then water extraction appears to be a candidate for efficient bioconversion to ethanol.     

Characterization of the binding of Actinomyces naeslundii (ATCC 12104) and Actinomyces viscosus (ATCC 19246) to glycosphingolipids, using a solid-phase overlay approach

Actinomyces naeslundii (ATCC 12104) and Actinomyces viscosus (ATCC 19246) were radiolabeled externally (125I) or metabolically (35S) and analyzed for their ability to bind glycosphingolipids separated on thin layer chromatograms or coated in microtiter wells. Two binding properties were found and characterized in detail. (i) Both bacteria showed binding to lactosylceramide (LacCer) in a fashion similar to bacteria characterized earlier. The activity of free LacCer was dependent on the ceramide structure; species with 2-hydroxy fatty acid and/or a trihydroxy base were positive, while species with nonhydroxy fatty acid and a dihydroxy base were negative binders. Several glycolipids with internal lactose were active but only gangliotriaosylceramide and gangliotetraosylceramide were as active as free LacCer. The binding to these three species was half-maximal at about 200 ng of glycolipid and was not blocked by preincubation of bacteria with free lactose or lactose-bovine serum albumin. (ii) A. naeslundii, unlike A. viscosus, showed a superimposed binding concluded to be to terminal or internal GalNAc beta and equivalent to a lactose-inhibitable specificity previously analyzed by other workers. Terminal Gal beta was not recognized in several glycolipids, although free Gal and lactose were active as soluble inhibitors. The binding was half-maximal at about 10 ng of glycolipid. A glycolipid mixture prepared from a scraping of human buccal epithelium contained an active glycolipid with sites for both binding specificities.     

Characterization of enzymatic reduction of hexavalent chromium by Escherichia coli ATCC 33456.

Chromium reduction by Escherichia coli ATCC 33456 quantitatively transferred hexavalent chromium, Cr(VI), to trivalent chromium, Cr(III). The reduced chromium was predominantly present in the external medium. Supernatant fluids of cell extract, obtained by centrifugation at 12,000 and 150,000 x g, showed almost the same Cr(VI) reduction activity, indicating that Cr(VI) reduction by E. coli ATCC 33456 was a largely soluble reductase activity. In studies with respiratory inhibitors, no inhibitory effects on aerobic and anaerobic Cr(VI) reduction were demonstrated by addition of cyanide, azide, and rotenone into both intact cell cultures and supernatant fluids of E. coli ATCC 33456. Although cytochromes b and d were identified in the membrane fraction of cell extracts, Cr(VI) was not reduced by the membrane fraction alone. The cytochrome difference spectra analysis also indicated that these cytochromes of the respiratory chain require the presence of the soluble Cr(VI) reductase to mediate electron transport to Cr(VI). Stimulation of Cr(VI) reduction by an uncoupler, 2,4-dinitrophenol, indicated that the respiratory-chain-linked electron transport to Cr(VI) was limited by the rate of dissipation of the proton motive force.     

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。     

Characterization of total deoxyribonucleic acid of Mycobacterium paratuberculosis (ATCC 19698) and of M. avium complex (ATCC 25291) using restriction enzymes

Total DNA was extracted from M. paratuberculosis (ATCC 19698) and from M. avium complex (ATCC 25291) cultivated on RVB-10 enriched liquid media. Restriction endonuclease analysis was conducted of Total DNA using 34 enzymes and DNA digestion profiles were compared. Fifteen enzymes revealed important differences between the two species. Two pairs of enzymes (EcoRII, BstNI) and (MboI, Sau3AI) provide evidence for the presence of dcmI and dam methylation in DNA of M. avium complex and M. paratuberculosis. The differences in DNA fragments of these two species could be of potential value in differentiating these clinically significant mycobacteria.     

Engineering of ethanolic E. coli with the Vitreoscilla hemoglobin gene enhances ethanol production from both glucose and xylose

Escherichia coli strain FBR5, which has been engineered to direct fermentation of sugars to ethanol, was further engineered, using three different constructs, to contain and express the Vitreoscilla hemoglobin gene (vgb). The three resulting strains expressed Vitreoscilla hemoglobin (VHb) at various levels, and the production of ethanol was inversely proportional to the VHb level. High levels of VHb were correlated with an inhibition of ethanol production; however, the strain (TS3) with the lowest VHb expression (approximately the normal induced level in Vitreoscilla) produced, under microaerobic conditions in shake flasks, more ethanol than the parental strain (FBR5) with glucose, xylose, or corn stover hydrolysate as the predominant carbon source. Ethanol production was dependent on growth conditions, but increases were as high as 30%, 119%, and 59% for glucose, xylose, and corn stover hydrolysate, respectively. Only in the case of glucose, however, was the theoretical yield of ethanol by TS3 greater than that achieved by others with FBR5 grown under more closely controlled conditions. TS3 had no advantage over FBR5 regarding ethanol production from arabinose. In 2 L fermentors, TS3 produced about 10% and 15% more ethanol than FBR5 for growth on glucose and xylose, respectively. The results suggest that engineering of microorganisms with vgb/VHb could be of significant use in enhancing biological production of ethanol.     

Parametric studies of ethanol production form xylose and other sugars by recombinant Escherichia coli

The conversion of xylose to ethanol by recombinant Escherichia coli has been investigated in pH-controlled batch fermentations. Chemical and environmental parameters were varied to determine tolerance and to define optimal conditions. Relatively high concentrations of ethanol (56 g/L) were produced from xylose with excellent efficiencies. Volumetric productivities of up to 1.4 g ethanol/L h were obtained. Productivities, yields, and final ethanol concentrations achieved from xylose with recombinant E. coli exceeded the reported values with other organisms. In addition to xylose, all other sugar constituents of biomass (glucose, mannose, arabinose, and galactose) were efficiently converted to ethanol by recombinant E. coli. Unusually low inocula equivalent to 0.033 mg of dry cell weight/L were adequate for batch fermentations. The addition of small amounts of calcium, magnesium, and ferrous ions stimulated fermentation. The inhibitory effects of toxic compounds (salts, furfural, and acetate) which are present in hemicellulose hydrolysates were also examined.