Limitations in substrate utilization efficiency by Zymomonas mobilis

Summary Optimal growth conditions for Zymomonas mobilis have been established using continuous cultivation methods. Optimal substrate utilization efficiency occurs with 2.5 g l^–1 yeast extract, 2.0 g l^–1 ammonium sulfate and 6.0 g l^–1 magnesium sulfate in the media. Catabolic activity is at its maximum with glucose uptake rates of 16–18 g l^–1 h^–1 and ethanol production rates of 8–9 g l^–1 h^–1, Q_g values of 22–26 and Q_p values between 11 and 13, which results in 40 g l^–1 h^–1 ethanol yields using a 100 g l^–1 substrate feed. Any increase in these parameters goes on cost of substrate utilization efficiency. Calcium pantothenate can not substitute yeast extract.Abbreviations G Glucose (%) - Pant Calcium pantothenate (mg l^–1) - D Dilution rate (h^–1) - NH₄ Ammonium sulfate (%) - M_g Magnesium sulfate (%) - S₁ Residual glucose in the fermenter (g l^–1) - S₀ Glucose feed (g l^–1) - Eth Ethanol concentration (g l^–1) - GUR Glucose uptake rate (g l^–1 h^–1) - Q_g Specific glucose uptake rate (g g^–1 h^–1) - Q_p Specific ethanol production rate (g g^–1 h^–1) - EPR Ethanol production rate (g l^–1 h^–1) - Y_g Yield coefficient for glucose (g g^–1) - Y_p Conversion efficiency (%) - C Biomass concentration (g l^–1) Present address: (Until June 1982) Institut für Mikrobiologie, TH Darmstadt, 6100 Darmstdt, Federal Republic of Germany     

Use of differential dye-ligand chromatography with affinity elution for enzyme purification: 6-phosphogluconate dehydratase from Zymomonas mobilis

Using differential dye-ligand chromatography and affinity elution with a substrate analog, 6-phosphogluconate dehydratase (EC 4.2.1.12) has been isolated from extracts of Zymomonas mobilis in a one-step procedure with 50% recovery. The specific activity of freshly isolated enzyme was 245 units mg-1. The enzyme contains iron, and it is rapidly inactivated in oxidizing conditions. It is inhibited by glycerophosphates, most strongly by the D-alpha-isomer which structurally corresponds to half of the substrate molecule.     

Fermentation pattern of Zymomonas mobilis at high sucrose concentrations

Summary Zymomonas mobilis was grown in batch concentrations between 200 and 400 g/l sucrose. The fermentation pattern revealed that the efficiency of sucrose hydrolysis dropped only from 94 to 78.6% whereas the efficiency with which the hydrolyzed products were converted to ethanol decreased from 94 to 43%. The ethanol yields were relatively constant for final concentrations which lay between 80 and 132 g/l. Fermentation times increased to 72 hours at the higher sucrose concentrations. Sorbitol and fructose were identified as the major by-products. Preliminary evidence suggests that the ratio between the two by-products depends on the pH of the culture medium. Results suggest the possibility of processes producing ethanol plus fructose, ethanol plus fructose and sorbitol, or ethanol plus sorbitol in a single-stage batch fermentation.     

Gluconate kinase from Zymomonas mobilis: isolation and characteristics

The enzyme gluconate kinase EC 2.7.1.12 has been found at high levels in glucose-grown Zymomonas mobilis cells. A simple procedure, based on differential dye-ligand chromatography, has been used to isolate the enzyme, purifying it some 600-fold. The purified enzyme is a monomer of molecular weight 18,000 Da, which is much smaller than other gluconate kinases reported. It has a relatively low affinity for ATP. (Km = 1.5 mM), but high for gluconate (Km = 0.33 mM), and has little activity with any other potential substrates.     

High efficiency ethanol fermentation by entrapment of Zymomonas mobilis into LentiKats

AIMS: To examine the potential of Zymomonas mobilis entrapped into polyvinylalcohol (PVA) lens-shaped immobilizates in batch and continuous ethanol production. METHODS AND RESULTS: Cells, free or immobilized in PVA hydrogel-based lens-shaped immobilizates - LentiKats, were cultivated on glucose medium in a 1 l bioreactor. In comparison with free cell cultivation, volumetric productivity of immobilized batch culture was nine times higher (43.6 g l(-1) h(-1)). The continuously operated system did not improve the efficiency (volumetric productivity of the immobilized cells 30.7 g l(-1) h(-1)). CONCLUSIONS: We demonstrated Z. mobilis capability, entrapped into LentiKats, in the cost-efficient batch system of ethanol production. SIGNIFICANCE AND IMPACT OF THE STUDY: The results reported here emphasize the potential of bacteria in combination with suitable fermentation technology in industrial scale. The innovation compared with traditional systems is characterized by excellent long-term stability, high volumetric productivity and other technological advantages.     

The kinetics of glucose-fructose oxidoreductase from Zymomonas mobilis

Glucose-fructose oxidoreductase operates by a classic ping-pong mechanism with a single site for all substrates: glucose, fructose, gluconolactone and sorbitol. The Km values for these substrates were determined. The values of kcat are 200 s-1 and 0.8 s-1 for the forward and reverse directions respectively. The overall catalytic process consists of two half-reactions with alternate reduction of NADP+ and oxidation of NADPH tightly bound to the enzyme. Reduction of enzyme-NADP+ by glucose and oxidation of enzyme-NADPH by gluconolactone involve single first-order processes. The values of the rate constants at saturating substrate are 2100 s-1 and 8 s-1 respectively; deuterium isotope effects indicate that these are for the hydrogen transfer step. Oxidation of enzyme-NADPH by fructose is first order with a limiting rate constant of at least 430 s-1. The reaction of enzyme-NADP+ with sorbitol is biphasic, with rate constants for both phases less than 1 s-1. This behaviour is explained by a mechanism in which the slow cyclisation of the acyclic form of fructose follows its dissociation from the enzyme. The rate-determining steps for the overall reaction are probably dissociation of gluconolactone in the forward direction and hydrogen transfer from sorbitol to enzyme-bound NADP+ in the reverse direction.     

Use of differential dye-ligand chromatography with affinity elution for enzyme purification: 2-keto-3-deoxy-6-phosphogluconate aldolase from Zymomonas mobilis

2-Keto-3-deoxy-6-phosphogluconate aldolase (EC 4.1.2.14) has been isolated from extracts of Zymomonas mobilis using differential dye-ligand chromatography and affinity elution with product/product analog. The one-step procedure gives an enzyme with specific activity 600 units mg-1. Only 1 out of 47 dyes, Procion Yellow MX-GR, bound the enzyme completely in 20 mM phosphate buffer, pH 6.5. A column of Navy HE-R adsorbent was used first to remove most of the potentially adsorbing proteins.     

Genetic modification of Zymomonas mobilis

The bacterium Zymomonas mobilis is a potentially useful organism for the commercial production of ethanol as it is capable of more than double the rate of alcohol production by yeast. However, industrial application of this bacterium has been restricted in part due to the disadvantages of its limited substrate range (glucose, fructose and sucrose) and by-product formation. Progress in strain improvement and genetic manipulation of this ethanologen is reviewed. Methodologies for gaining reproducible gene transfer in Z. mobilis have recently been developed. Genetic modification has led to its growth on the additional substrates lactose and mannitol. Additionally, a range of by-product negative mutants have also been isolated. Further interest has focused on transfer of Z. mobilis genes to other fermentive organisms in order to gain enhanced product formation. Overall, these genetic approaches should lead to development of novel strains of Z. mobilis and other genera, capable of the use of starch, cellulose and xylan in a manner attractive for industrial ethanol production, besides facilitating over production of products from E. coli strains with enhanced capability to grow at high density.     

Ethanol production from cane juice by Zymomonas mobilis

Summary Zymomonas mobilis Z 7 fermented 100 to 200 g.l^{- 1} sucrose in cane juice to ethanol without addition of cofactors or mineral salts in 1 ltr laboratory and 100 ltr pilot plant fermenters. Ethanol yields (E_yield) were from 60 to 88% with fermentation times of 20 to 29 h at 35 °C.Nomenclature V_s max g.1^-1 .h^-1 maximum sucrose hydrolysis rate - V_g max g.1^-1 .h^-1 maximum glucose uptake rate - V_fmax g.1^-1 .h^-1 maximum fructose uptake rate - V_e max g.1^-1 .h^-1 maximum ethanol production rate - S_h g.1^-1 sucrose hydrolyzed at t_ferm - G_u g.1^-1 glucose utilized at t_ferm - F_u g.1^-1 fructose utilized at t_ferm - E_max g.1^-1 ethanol produced at t_ferm - G_i g.1^-1 initial free glucose (before sucrose hydrolysis) - E_yield g.g^-1 ethanol produced divided by the theoretical ethanol yield from sucrose hydrolyzed - t_ferm h fermentation time to ethanol max     

Glycolytic flux in Zymomonas mobilis: enzyme and metabolite levels during batch fermentation.

The rate at which Z. mobilis (Entner-Doudoroff pathway) converts high concentrations of glucose (20%) into ethanol plus CO2 changes as ethanol accumulates in the surrounding broth. This decline in glycolytic activity (per milligram of cell protein) does not result from inhibitory effects of ethanol, which can be reversed immediately by ethanol removal. The peak of fermentative activity (58 mumol of CO2 evolved per mg of cell protein per h) occurred after the accumulation of 1.1% ethanol (18 h) and declined to one-half this rate after 30 h (6.2% accumulated ethanol), although the cell number continued to increase. These times corresponded to the end of exponential growth and to the onset of the stationary phase (on the basis of measurement of cell protein), respectively. An examination of many of the requirements for fermentation (nucleotides, magnesium, enzyme levels, intracellular pH, delta pH) revealed three possible reasons for this early decline in activity: decreased abundance of nucleotides, a decrease in internal pH from 6.3 to 5.3, and a decrease in the specific activities of two glycolytic enzymes (pyruvate kinase and glyceraldehyde-3-phosphate dehydrogenase). 31P nuclear magnetic resonance spectra of perchlorate extracts from cells fermenting in broth revealed very low levels of glycolytic intermediates (Entner-Doudoroff pathway) in cells examined at the peak of fermentative activity (18-h cells) in comparison with cells examined at a later stage (30-h cells), consistent with limitation of the fermentation rate by glycolytic enzymes near the end of the pathway. It is likely that cell death (loss of colony-forming ability) and the collapse of delta pH also contribute to the further decline in fermentative activity after 30 h.     

Ethanol production from wheat flour by Zymomonas mobilis

Starch from wheat flour was enzymatically hydrolyzed and used for ethanol production by Zymmonas mobilis. The addition of a nitrogen source like ammonium sulfate was sufficient to obtain a complete fermentation of the hdyrolyzed strach. In batch culture a glucose concentration as high as 223 g/l could be fermented (conversion 99.5%) to 105 g/l of ethanol in 70 h with an ethanol yield of 0.47 g/g (92% of theoretical). In continuous culture the use of a flocculent strain and a fermentor with an internal settler resulted (D=1,4 h⁻¹) in a high ethanol productivity of 70.7 g/l·h with: ethanol concentration 49.5 g/l, ethanol yield 0.50 g/g (98% of theoretical and substrate conversion 99%.     

NADP+-dependent acetaldehyde dehydrogenase from Zymomonas mobilis

An NADP⁺-linked acetaldehyde dehydrogenase (EC 1.2.1.4) from the ethanol producing bacterium Zymomonas mobilis was purified 180-fold to homogeneity. The enzyme is a cytosolic protein with an isoelectric point of 8.0 and has an apparent molecular weight of 210000. It showed a single band in sodium dodecylsulfate gel electrophoresis with a molecular weight of 55000, which indicates that it consists of four probably identical subunits. The apparent K _m values for the substrate acetaldehyde were 57 M and for the cosubstrate NADP⁺ 579 M. The enzyme was almost inactive with NAD⁺ as cofactor. Several other aldehydes besides acetaldehyde were accepted as a substrate but not formaldehyde or trichloroacetaldehyde. In anaerobically grown cells of Zymomonas mobilis the enzyme showed a specific activity of 0.035 U/mg protein but its specific activity could be increased up to 0.132 U/mg protein by adding acetaldehyde to the medium during the exponential growth phase or up to 0.284 U/mg protein when cells were grown under aeration. The physiological role of the enzyme is discussed.Abbreviations ALD-DH acetaldehyde dehydrogenases from Z. mobilis - DTT dithiothreitol - MES 2-(N-morpholino)ethanesulfonic acid - MOPS 3-(N-morpholino)propanesulfonic acid - SDS sodium dodecylsulfate Dedicated to Prof. Dr. H.-G. Schlegel, Universität Göttingen, on the occasion of his 65th birthday     

An improved synthetic medium for continuous cultivation of Zymomonas mobilis

Summary A synthetic medium for continuous cultivation of Zymomonas mobilis was developed using the chemostat pulse technique in appropriate experimental designs. Yeast extract could be replaced by a mixture of six mineral salts, Ca-pantothenate, l-as-partate, and l-serine. Kinetic data from continuous cultivations of strains ATCC 10988 and ZM4 are presented and compared with published data.     

An evolved xylose transporter from Zymomonas mobilis enhances sugar transport in Escherichia coli

Background  

Xylose is a second most abundant sugar component of lignocellulose besides glucose. Efficient fermentation of xylose is important for the economics of biomass-based biorefineries. However, sugar mixtures are sequentially consumed in xylose co-fermentation with glucose due to carbon catabolite repression (CCR) in microorganisms. As xylose transmembrance transport is one of the steps repressed by CCR, it is therefore of interest to develop a transporter that is less sensitive to the glucose inhibition or CCR.     

Regulation of glucose 6-phosphate dehydrogenase in Zymomonas mobilis CP4

Abstract Glucose 6-phosphate dehydrogenase was purified 29-fold from Zymomonas mobilis . The enzyme was active with both NAD and NADP. Phosphoenolpyruvate was found to be a negative allosteric effector and ATP inhibited the enzyme non-allosterically, at physiological concentrations.     

Glucose-6-phosphate dehydrogenase in cell free extracts of Zymomonas mobilis

Summary Glucose-6-phosphate dehydrogenase activity in cell free extracts o Zymomonas mobilis showed marked differences when compared with the corresponding enzyme of Escherichia coli. It exhibited 3 times higher activity and the reaction rate over 10 min gave linearity only up to a cell free protein concentration of 0.15 mg protein. This different behaviour was not a function of environmental growth conditions of the culture nor of the nine different assay methods employed. A constant relationship existed between the specific G-6-P dehydrogenase protein and the total protein concentration in the cell free extract. The enzyme was stable for at least 5 h at 4°C in Tris-NaCl-MgCl₂-buffer.An investigation of the properties of G-6-P dehydrogenase from Z. mobilis revealed a pH optimum of 8.7 with a rapid decline towards the acidic and a small decrease towards the alkaline side. The K _m values were 5×10^-4 m for glucose-6-phosphate and 3.6×10^-5 m NADP⁺. The addition of 1×10^-2 m MgCl₂ produced optimal activity but higher concentrations inhibited the enzyme reaction.These results were discussed with those from other sources and found to be unique for Zymomonas mobilis.Meinem hochverehrten Lehrer Herrn Professor A. Rippel zum 80. Geburtstage.     

d-Glucose Transport System of Zymomonas mobilis

The properties of the d-glucose transport system of Zymomonas mobilis were determined by measuring the uptake of nonmetabolizable analogs (2-deoxy-d-glucose and d-xylose) by wild-type cells and the uptake of d-glucose itself by a mutant lacking glucokinase. d-Glucose was transported by a constitutive, stereospecific, carrier-mediated facilitated diffusion system, whereby its intracellular concentration quickly reached a plateau close to but not above the external concentration. d-Xylose was transported by the d-glucose system, as evidenced by inhibition of its uptake by d-glucose. d-Fructose was not an efficient competitive inhibitor of d-glucose uptake, indicating that it has a low affinity for the d-glucose transport system. The apparent K(m) of d-glucose transport was in the range of 5 to 15 mM, with a V(max) of 200 to 300 nmol min mg of protein. The K(m) of Z. mobilis glucokinase (0.25 to 0.4 mM) was 1 order of magnitude lower than the K(m) for d-glucose transport, although the V(max) values for transport and phosphorylation were similar. Thus, glucose transport cannot be expected to be rate limiting at concentrations of extracellular glucose normally used in fermentation processes, which greatly exceed the K(m) for the transport system. The low-affinity, high-velocity, nonconcentrative system for d-glucose transport described here is consistent with the natural occurrence of Z. mobilis in high-sugar environments and with the capacity of Z. mobilis for rapid conversion of glucose to metabolic products with low energetic yield.     

产乙醇运动发酵单胞菌的研究进展

运动发酵单胞菌作为天然生产乙醇的主要微生物之一,具有特殊的Entner Doudoroff途径和其他一些特殊的糖代谢和能量代谢方式,因此具有乙醇产率高和乙醇耐受力强的显著特点。通过简述运动发酵单胞菌的糖代谢和能量代谢、乙醇和高渗透压等耐性及其遗传改造三方面的研究进展,阐明其应用于燃料乙醇生产的巨大潜力