Optimization of 2,3-butanediol production by Klebsiella oxytoca through oxygen transfer rate control

Production of 2,3-butanediol by Klebsiella oxytoca is influenced by the degree of oxygen limitation. During batch culture studies, two phases of growth are observed: energy-coupled growth, during which cell growth and oxygen supply are coupled; and, energy-uncoupled growth, which arises when the degree of oxygen limitation reaches a critical value. Optimal 2,3-butanediol productivity occurs during the energy-coupled growth phase. In this article, a control system which maintains the batch culture at a constant level of oxygen limitation in the energy-coupled growth regime has been designed. Control, which involves feedback control on the oxygen transfer coefficient, is achieved by continually increasing the partial pressure of oxygen in the feed gas, which in turn continually increases the oxygen transfer rate. Control has resulted in a balanced state of growth, a repression of ethanol formation, and an increase in 2,3-butanediol productivity of 18%. (c) 1993 John Wiley & Sons, Inc.     

一种简单的高产2,3-丁二醇发酵生产方法

利用一株克雷伯氏菌(Klebsiellasp.LN145)在以葡萄糖和磷酸氢二铵为主要成分的培养基中发酵生产2,3-丁二醇。在补料发酵培养过程中,通过补糖,2,3-丁二醇和3-羟基丁酮的最大产量分别达到了84.0 g/L和10.5 g/L,二醇的摩尔转化率达到理论水平的91%,转化速率达到1.8 g/(L.h)。     

2，3-丁二醇的发酵及盐析分离工艺

采用克雷伯氏菌（Klebsiella pneumoniae CICC 10011）发酵生产2,3-丁二醇,并对2,3-丁二醇的盐析分离工艺进行了考察。通过实验确定了以葡萄糖为底物微氧批式流加发酵的条件,发酵液中2,3-丁二醇和3-羟基丁酮的质量浓度分别为90．98g/L和12．40g/L,2,3-丁二醇的摩尔转化率为82．7％,生产强度达到2．1g/（L·h）。对发酵液中2,3-丁二醇的盐析分离研究表明,K2HPO4和K3PO4对2,3-丁二醇的盐析效果优于K2CO3。当发酵液浓缩70％后,加入质量分数为45％的K,HPO4,2,3-丁二醇的分配系数达到9．10,回收率为79．37％;上相中2,3-丁二醇的质量浓度达到420g／L;此时3-羟基丁酮的分配系数和回收率分别为11．9和83．48％。     

Optimization of operating parameters for sludge process reduction under alternating aerobic/oxygen-limited conditions by response surface methodology

Batch tests were employed to estimate the optimal conditions for excess sludge reduction under an alternating aerobic/oxygen-limited environment using response surface methodology. Three key operating parameters, initial mixed liquor suspended solids (initial MLSS), HRT (hydraulic retention time) and reaction temperature (T), were selected, and their interrelationships studied by the Box–Behnken design. The experimental data and ANOVA analysis showed that the coefficient of determination (R²) was 0.9956 and the adjR² was 0.9912, which demonstrates that the modified model was significant. The optimum conditions were predicted to give a maximal ΔMLSS yield of 226 mg/L at an initial MLSS of 10,021 ± 50 mg/L, an HRT of 9.1 h and a reaction temperature of 29 °C. The prediction was tested by triplicate experiments, where a ΔMLSS yield of 233 mg/L was achieved under the chosen optimal conditions. This excellent correlation between the predicted and measured values provides confidence in the model.     

Production of L-2,3-butanediol by a new pathway constructed in Escherichia coli

AIMS: A metabolic pathway for L-2,3-butanediol (BD) as the main product has not yet been found. To rectify this situation, we attempted to produce L-BD from diacetyl (DA) by producing simultaneous expression of diacetyl reductase (DAR) and L-2,3-butanediol dehydrogenase (BDH) using transgenic bacteria, Escherichia coli JM109/pBUD-comb. METHODS AND RESULTS: The meso-BDH of Klebsiella pneumoniae was used for its DAR activity to convert DA to L-acetoin (AC) and the L-BDH of Brevibacterium saccharolyticum was used to reduce L-AC to L-BD. The respective gene coding each enzyme was connected in tandem to the MCS of pFLAG-CTC (pBUD-comb). The divided addition of DA as a source, addition of 2% glucose, and the combination of static and shaking culture was effective for the production. CONCLUSIONS: L-BD (2200 mg l(-1)) was generated from 3000 mg l(-1) added of DA, which corresponded to a 73% conversion rate. Meso-BD as a by-product was mixed by 2% at most. SIGNIFICANCE AND IMPACT OF THE STUDY: An enzyme system for converting DA to L-BD was constructed with a view to using DA-producing bacteria in the future.     

Hydrolysis of Lipid-Extracted Chlorella vulgaris by Simultaneous Use of Solid and Liquid Acids

Microalgal biomass was hydrolyzed using a solid acid catalyst with the aid of liquid acid. The use of solid acid as the main catalyst instead of liquid acid was to omit subsequent neutralization and/or desalination steps, which are commonly required in using the resulting hydrolysates for microbial fermentation. The hydrolysis of 10 g/L of lipid-extracted Chlorella vulgaris containing 12.2% carbohydrates using 7.6 g/L Amberlyst 36 and 0.0075 N nitric acid at 150°C resulted in 1.08 g/L of mono-sugars with a yield of 88.5%. For hydrolysis of higher concentrations of the biomass over 10 g/L, the amount of Amberlyst 36 needed to be increased in proportion to the biomass concentration to maintain similar levels of hydrolysis performance. Increasing the solid acid concentration protected the surface of the solid acid from being severely covered by cell debris during the reaction. A hydrolysate of lipid-extracted C. vulgaris 50 g/L was used, with no post-treatment of desalination, for the cultivation of Klebsiella oxytoca producing 2,3-butanediol. Cell growth in the hydrolysate was found to be almost the same as in the conventional medium with the same monosaccharide composition, confirming its fermentation compatibility. It was noticeable that the yield of 2,3-butanediol with the hydrolysate was observed to be 2.6 times higher than that with the conventional medium. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 35: e2729, 2019     

Physiological and energetic aspects of bacterial metabolite overproduction

This review attempts to provide a rational explanation for microbial metabolite over-production, a phenomenon manifest with many wild-type and mutant organisms. After analysing the relationships between catabolic and anabolic processes within the growing cell (which point to the presence of sufficient kinetic control elements to ensure a stringent coupling between the two), consideration is given to mechanisms that might allow the rate of catabolism to be varied independently of the rate of anabolism. It is in this latter context that an excretion of specific metabolites appears to play a key role.     

Selection of an endogenous 2,3-butanediol pathway in Escherichia coli by fermentative redox balance

Fermentative redox balance has long been utilized as a metabolic evolution platform to improve efficiency of NADH-dependent pathways. However, such system relies on the complete recycling of NADH and may become limited when the target pathway results in excess NADH stoichiometrically. In this study, endogenous capability of Escherichia coli for 2,3-butanediol (2,3-BD) synthesis was explored using the anaerobic selection platform based on redox balance. To address the issue of NADH excess associated with the 2,3-BD pathway, we devised a substrate-decoupled system where a pathway intermediate is externally supplied in addition to the carbon source to decouple NADH recycling ratio from the intrinsic pathway stoichiometry. In this case, feeding of the 2,3-BD precursor acetoin effectively restored anaerobic growth of the mixed-acid fermentation mutant that remained otherwise inhibited even in the presence of a functional 2,3-BD pathway. Using established 2,3-BD dehydrogenases as model enzyme, we verified that the redox-based selection system is responsive to NADPH-dependent reactions but with lower sensitivity. Based on this substrate-decoupled selection scheme, we successfully identified the glycerol/1,2-propanediol dehydrogenase (Ec-GldA) as the major enzyme responsible for the acetoin reducing activity (k_cat/K_m≈0.4 mM⁻¹ s⁻¹) observed in E. coli. Significant shift of 2,3-BD configuration upon withdrawal of the heterologous acetolactate decarboxylase revealed that the endogenous synthesis of acetoin occurs via diacetyl. Among the predicted diacetyl reductase in E. coli, Ec-UcpA displayed the most significant activity towards diacetyl reduction into acetoin (V_max≈6 U/mg). The final strain demonstrated a meso-2,3-BD production titer of 3 g/L without introduction of foreign genes. The substrate-decoupled selection system allows redox balance regardless of the pathway stoichiometry thus enables segmented optimization of different reductive pathways through enzyme bioprospecting and metabolic evolution.     

High-yield production of (R)-acetoin in Saccharomyces cerevisiae by deleting genes for NAD(P)H-dependent ketone reductases producing meso-2,3-butanediol and 2,3-dimethylglycerate

Acetoin is widely used in food and cosmetics industries as a taste and fragrance enhancer. To produce (R)-acetoin in Saccharomyces cerevisiae, acetoin biosynthetic genes encoding α-acetolactate synthase (AlsS) and α-acetolactate decarboxylase (AlsD) from Bacillus subtilis and water-forming NADH oxidase (NoxE) from Lactococcus lactis were integrated into delta-sequences in JHY605 strain, where the production of ethanol, glycerol, and (R,R)-2,3-butanediol (BDO) was largely eliminated. We further improved acetoin production by increasing acetoin tolerance by adaptive laboratory evolution, and eliminating other byproducts including meso-2,3-BDO and 2,3-dimethylglycerate, a newly identified byproduct. Ara1, Ypr1, and Ymr226c (named Ora1) were identified as (S)-alcohol-forming reductases, which can reduce (R)-acetoin to meso-2,3-BDO in vitro. However, only Ara1 and Ypr1 contributed to meso-2,3-BDO production in vivo. We elucidate that Ora1, having a substrate preference for (S)-acetoin, reduces (S)-α-acetolactate to 2,3-dimethylglycerate, thus competing with AlsD-mediated (R)-acetoin production. By deleting ARA1, YPR1, and ORA1, 101.3 g/L of (R)-acetoin was produced with a high yield (96% of the maximum theoretical yield) and high stereospecificity (98.2%).     

芽胞杆菌发酵产2,3-丁二醇的研究进展及展望

综述了近年来利用芽胞杆菌生产2,3-丁二醇(2,3-BD)的研究进展,包括生产菌株的筛选、影响芽胞杆菌发酵2,3-丁二醇的因素、芽胞杆菌2,3-丁二醇代谢途径及调控等方面,并对其研究方向进行了展望。     

Purification and Characterization of L-2,3-Butanediol Dehydrogenase of Brevibacterium saccharolyticum C-1012 Expressed in Escherichia coli

The L-2,3-butanediol dehydrogenase produced in E. coli JM109/pLBD2-CTC was purified by 5 steps. The molecular mass of this enzyme was estimated at 110 kDa and the subunit was mesured to be 30 kDa. The L-BDH had some differences from the BDHs from other sources in substrate specificity, pI value, pH stability, effects of divalent cations, and organic acids.     

氧供应量对Klebsiella pneumoniae利用混合糖生物合成2,3-丁二醇过程的影响分析

以筛选的肺炎克雷伯氏茵（Klebsiella pneumoniaeUV-86）为对象,考察供氧条件分别对茵体生长、葡萄糖和木糖双底物利用和产物合成的影响。研究发现生物量随氧供应量增加而增加。不同供氧条件对茵体消耗葡萄糖过程的影响较小,而代谢木糖的能力随氧供应量的增大而增强。微氧条件下2,3-丁二醇的生物合成能力最强,2,3-丁二醇产量在1．5wm下达到最高为30．1g／L,是好氧时的2．5倍,最大体积产率为0．485g／（L·h）。不同条件下两底物产物分布有所区别,木糖代谢中乙酸生产增强。因此根据不同阶段代谢特点选择适合的供氧策略可以提高过程产量和产率。     

Biotechnological production of 2,3-butanediol—Current state and prospects

Biotechnological production of 2,3-butanediol (hereafter referred to as 2,3-BD) from wastes and excessive biomass is a promising and attractive alternative for traditional chemical synthesis. In the face of scarcity of fossil fuel supplies the bio-based process is receiving a significant interest, since 2,3-BD may have multiple practical applications (e.g. production of synthetic rubber, plasticizers, fumigants, as an antifreeze agent, fuel additive, octane booster, and many others). Although the 2,3-BD pathway is well known, microorganisms able to ferment biomass to 2,3-BD have been isolated and described, and attempts of pilot scale production of this compound were made, still much has to be done in order to achieve desired profitability. This review summarizes hitherto gained knowledge and experience in biotechnological production of 2,3-BD, sources of biomass used, employed microorganisms both wild type and genetically improved strains, as well as operating conditions applied.     

An energetic model of muscle contraction

Initial energy utilization in the twitch is visualized as the result of the activity of two distinct processes. The first is the calcium-pumping activity of the sarcoplasmic reticulum, which has a constant energy requirement under normal conditions. The second is the chemomechanical transduction process consisting of a variable number of quantal contractile events, each with a fixed enthalpy equal to the molecular enthalpy of adenosine triphosphate (ATP) hydrolysis in vivo. This enthalpy appears either as heat or as contractile element work. Total enthalpy varies according to the number of quantal contractile events that occur in the twitch cycle. The basis of the variation is suggested to be velocity-dependent activity of the actomyosin ATPase, allowing more quantal events to occur in a contraction cycle when shortening occurs. The classical designation “activation heat” is held to be appropriate for the first process. The partition of the enthalpy of the second process that is currently in vogue is held to be misleading and a new formulation is suggested in which the properties of the quantal contractile event are reflected in general terms. The formulation of the proposed transduction model represents a conceptual return to the viscoelastic theory, but at a quantal level. The model can explain the results of the preceding paper and is adaptable to different muscles without having to postulate fundamental differences in energy utilization.     

巴氏醋杆菌高酸度醋发酵过程的能量代谢分析

【目的】初步分析了Acetobacter pasteurianus CICIM B7003-02在醋酸发酵过程中的能量代谢状况, 通过强化细胞能量代谢水平以提升菌株高酸发酵的产酸强度。【方法】探明A. pasteurianus CICIM B7003-02在高酸度醋发酵的不同阶段中三羧酸循环底物含量、乙醇呼吸链酶活及能量代谢酶基因的转录水平等代谢特点, 分析用于醋酸发酵的产能代谢途径及其作用。【结果】发现A. pasteurianus CICIM B7003-02在醋酸发酵初期, 主要通过苹果酸/琥珀酸回补偶联有氧呼吸途径产能。进入醋酸快速积累阶段, 乙醇呼吸链为主要供能代谢途径。发酵后期苹果酸/琥珀酸回补途径配合乙醇呼吸链供能。基于上述研究, 采取添加琥珀酸和苹果酸强化细胞产能, 促进高酸度醋发酵强度。【结论】能量供给影响醋杆菌耐酸能力和醋酸生产能力。确定乙醇呼吸链为醋酸发酵的主要供能系统。强化细胞产能手段可达到提高醋酸发酵强度的目的。     

Road avoidance and its energetic consequences for reptiles

Roads are one of the most widespread human‐caused habitat modifications that can increase wildlife mortality rates and alter behavior. Roads can act as barriers with variable permeability to movement and can increase distances wildlife travel to access habitats. Movement is energetically costly, and avoidance of roads could therefore impact an animal's energy budget. We tested whether reptiles avoid roads or road crossings and explored whether the energetic consequences of road avoidance decreased individual fitness. Using telemetry data from Blanding's turtles (Emydoidea blandingii; 11,658 locations of 286 turtles from 15 sites) and eastern massasaugas (Sistrurus catenatus; 1,868 locations of 49 snakes from 3 sites), we compared frequency of observed road crossings and use of road‐adjacent habitat by reptiles to expected frequencies based on simulated correlated random walks. Turtles and snakes did not avoid habitats near roads, but both species avoided road crossings. Compared with simulations, turtles made fewer crossings of paved roads with low speed limits and more crossings of paved roads with high speed limits. Snakes made fewer crossings of all road types than expected based on simulated paths. Turtles traveled longer daily distances when their home range contained roads, but the predicted energetic cost was negligible: substantially less than the cost of producing one egg. Snakes with roads in their home range did not travel further per day than snakes without roads in their home range. We found that turtles and snakes avoided crossing roads, but road avoidance is unlikely to impact fitness through energetic expenditures. Therefore, mortality from vehicle strikes remains the most significant impact of roads on reptile populations.     

产酸克雷伯氏杆菌发酵产2，3-丁二醇的培养基优化

采用不同设计方法相结合的策略对耐高糖产酸克雷伯氏杆菌（Klebsiella oxytoca）ME—UD-3-4发酵产2,3-丁二醇的培养基进行优化。首先在单因素实验的基础上采用Plackett—Burrnan设计法对影响ME—UD-3-4发酵产2,3-丁二醇的相关因素进行研究,筛选到3种有显著效应的因素（P〈0．05）：葡萄糖、玉米浆和MgSO4·7H2O。然后利用响应曲面法（Response Surface Methodology,RSM）对这3种因素的最佳水平范围进一步探讨;对得到的回归模型进行分析,得最佳条件（g／L）：葡萄糖220、玉米浆19和MgSO4·7H2O 0．4;在最佳条件下,发酵80h,2,3-丁二醇产量从原来的57．3 g／L提高到86．1 g／L,生产强度由0．72g／（L·h）提高到1．08g/（L·h）。     

Spontaneous activity rates and resting metabolism: Support for the allocation model of energy management at the among-individual level

Despite continuing interest in the proximate energetic constraints on individual variation in behavior, there is presently equivocal evidence for correlations between metabolism and behavior at the among-individual level. Possible reasons for this include imprecise estimates of individual mean behavior and metabolism due to no repeated measures on one or more of the traits, analyses that do not take into account the labile nature of these traits and the uncertainty in individual estimates, and changing environmental conditions not accounted for. In this empirical study, we repeatedly measured activity rates and resting metabolic rates (RMR) of individual male mosquitofish over an extended period, lasting several months under constant laboratory conditions. Repeatability of each trait was significant (RMR: R = .41; activity: R = .72), indicating consistent variation among individuals, making covariance between them possible. Contrary to expectations, bivariate mixed model analysis revealed that more active individuals had lower RMR (r = −.58) after accounting for mass effects and other covariates. This result suggests that high activity rates require individuals to allocate less energy toward maintenance, and thus provides evidence for the “allocation” model of energy management. We suggest that it would be valuable to study whether and how behavior-RMR correlations change over individual lifetime, a topic that has yet to be addressed.     

An algebraic spline model of molecular surfaces for energetic computations

In this paper, we describe a new method to generate a smooth algebraic spline (AS) approximation of the molecular surface (MS) based on an initial coarse triangulation derived from the atomic coordinate information of the biomolecule, resident in the Protein data bank (PDB). Our method first constructs a triangular prism scaffold covering the PDB structure, and then generates a piecewise polynomial F on the Bernstein-Bezier (BB) basis within the scaffold. An ASMS model of the molecular surface is extracted as the zero contours of F, which is nearly C1 and has dual implicit and parametric representations. The dual representations allow us easily do the point sampling on the ASMS model and apply it to the accurate estimation of the integrals involved in the electrostatic solvation energy computations. Meanwhile comparing with the trivial piecewise linear surface model, fewer number of sampling points are needed for the ASMS, which effectively reduces the complexity of the energy estimation.     

Optimization of sodium percarbonate pretreatment for improving 2,3-butanediol production from corncob

Sodium percarbonate (SP), a kind of alkaline strong oxidant, was applied to corncob pretreatment. The optimized pretreatment conditions were at 4% (w/v) SP concentration with solid-to-liquid (SLR) ratio of 1:10 treating for 4?hr at 60°C. This pretreatment resulted in 91.06% of cellulose and 84.08% of hemicellulose recoveries with 34.09% of lignin removal in corncob. The reducing sugar yield from SP-pretreated corncob was 0.56?g/g after 72?hr of enzymatic hydrolysis, 1.75-folds higher than that from raw corncob. 2,3-butanediol production by Enterobacer cloacae in simultaneous saccharification fermentation was 29.18?g/L using SP-pretreated corncob as a substrate, which was 11.12 times of that using raw corncob. Scanning electron microscope, X-ray diffraction, and Fourier transform infrared spectra analysis indicated that physical characteristics, crystallinity, and structure of corncob had changed obviously after SP pretreatment. This simple and novel pretreatment method was effective for delignification and carbohydrate retention in microbial production of 2,3-butanediol from lignocellulose biomass.