Comparative shotgun proteomic analysis of Clostridium acetobutylicum from butanol fermentation using glucose and xylose

Background

Cytokinin is a plant hormone that plays a crucial role in several processes of plant growth and development. In recent years, major breakthroughs have been achieved in the elucidation of the metabolism, the signal perception and transduction, as well as the biological functions of cytokinin. An important activity of cytokinin is the involvement in chloroplast development and function. Although this biological function has already been known for 50 years, the exact mechanisms remain elusive.

Results

To elucidate the effects of altered endogenous cytokinin content on the structure and function of the chloroplasts, chloroplast subfractions (stroma and thylakoids) from transgenic Pssu-ipt and 35S:CKX1 tobacco (Nicotiana tabacum) plants with, respectively, elevated and reduced endogenous cytokinin content were analysed using two different 2-DE approaches. Firstly, thykaloids were analysed by blue-native polyacrylamide gel electrophoresis followed by SDS-PAGE (BN/SDS-PAGE). Image analysis of the gel spot pattern thus obtained from thylakoids showed no substantial differences between wild-type and transgenic tobacco plants. Secondly, a quantitative DIGE analysis of CHAPS soluble proteins derived from chloroplast subfractions indicated significant gel spot abundance differences in the stroma fraction. Upon identification by MALDI-TOF/TOF mass spectrometry, these proteins could be assigned to the Calvin-Benson cycle and photoprotective mechanisms.

Conclusion

Taken together, presented proteomic data reveal that the constitutively altered cytokinin status of transgenic plants does not result in any qualitative changes in either stroma proteins or protein complexes of thylakoid membranes of fully developed chloroplasts, while few but significant quantitative differences are observed in stroma proteins.     

Effects of butanol on Clostridium acetobutylicum

The internal pH of Clostridium acetobutylicum was determined at various stages during the growth of the organism. Even in the presence of significant quantities of acetic, butyric, and lactic acids, an internal pH of 6.2 was maintained. Experiments using N,N'-dicyclohexylcarbodiimide indicated that a functioning H+-ATPase is necessary for internal pH control. Butanol, one of the end products of the fermentation, had numerous harmful effects on C. acetobutylicum. At a concentration high enough to inhibit growth, butanol destroyed the ability of the cell to maintain internal pH, lowered the intracellular level of ATP, and inhibited glucose uptake. Experiments done at two different external pH values suggested that the butanol-mediated decrease in ATP concentration was independent of the drop in internal pH. Glucose uptake was not affected by arsenate, suggesting that uptake was not ATP dependent. The effects of butanol on C. acetobutylicum are complex, inhibiting several interrelated membrane processes.     

Production of acetone and butanol by Clostridium acetobutylicum in continuous culture with cell recycle

Summary To increase the solvent productivity of the acetone-butanol fermentation, a continuous culture of Clostridium acetobytylicum with cell recycling was used. At a dry cell mass concentration of 8 g l^-1 and a dilution rate of D=0.64 h^-1, a solvent productivity of 5.4 g l^-1 h^-1 was attained. To prevent degeneration of the culture, which occurs with high concentrations of solvents (acetone, butanol and ethanol), different reactor cascades were used. A two-stage cascade with cell recycling and turbidostatic cell concentration control turned out to be the best solution, the first stage of which was kept at relatively low cell and product concentrations. A solvent productivity of 3 and 2.3 g l^-1 h^-1, respectively, was achieved at solvent concentrations of 12 and 15 g l^-1.Symbols D Dilution rate (h^-1) - r _p solvent productivity (g l^-1 h^-1) - s residual glucose concentration (g l^-1) - V _R reactor volume (l) - V _O overall volume (l) - x (dry) cell mass concentration (g l^-1) - Y _P/S solvent yield (g g^-1)     

Effects of butanol on Clostridium acetobutylicum.

The internal pH of Clostridium acetobutylicum was determined at various stages during the growth of the organism. Even in the presence of significant quantities of acetic, butyric, and lactic acids, an internal pH of 6.2 was maintained. Experiments using N,N'-dicyclohexylcarbodiimide indicated that a functioning H+-ATPase is necessary for internal pH control. Butanol, one of the end products of the fermentation, had numerous harmful effects on C. acetobutylicum. At a concentration high enough to inhibit growth, butanol destroyed the ability of the cell to maintain internal pH, lowered the intracellular level of ATP, and inhibited glucose uptake. Experiments done at two different external pH values suggested that the butanol-mediated decrease in ATP concentration was independent of the drop in internal pH. Glucose uptake was not affected by arsenate, suggesting that uptake was not ATP dependent. The effects of butanol on C. acetobutylicum are complex, inhibiting several interrelated membrane processes.     

Continuous production of acetone and butanol with shear-activated Clostridium acetobutylicum

Summary When using shear activation of Clostridium acetobutylicum by pumping the cells through capillaries, the cell growth, glucose consumption and product formation rates are considerably increased. Shear-activated continuous cell culture can be used as an inoculum with a welldefined fermentation activity for batch cultures. Different runs of such batch cultivation yield well-reproducible results which could not be obtained from inocula of other cultures or even of heat-shocked spores. The cells can attain a growth rate higher than 1.6 h^-1.The shear-activated continous culture growth is affected already at a butanol concentration lower than 1.6 g/l^-1.     

Continuous production of butanol from a glucose/xylose mixture with an immobilized cell system coupled to pervaporation

Summary Glucose and xylose can be converted continuously and simultaneously to butanol using immobilized cells. Xylose is only converted when glucose is completely consumed and the biocatalyst is not fully inhibited by butanol. With pervaporation for in-situ butanol recovery the complete conversion of a feed containing 60 kg/m³ of mixed sugars is achieved.     

Shotgun proteomic monitoring of Clostridium acetobutylicum during stationary phase of butanol fermentation using xylose and comparison with the exponential phase

Economically viable production of solvents through acetone-butanol-ethanol (ABE) fermentation requires a detailed understanding of Clostridium acetobutylicum. This study focuses on the proteomic profiling of C. acetobutylicum ATCC 824 from the stationary phase of ABE fermentation using xylose and compares with the exponential growth by shotgun proteomics approach. Comparative proteomic analysis revealed 22.9% of the C. acetobutylicum genome and 18.6% was found to be common in both exponential and stationary phases. The proteomic profile of C. acetobutylicum changed during the ABE fermentation such that 17 proteins were significantly differentially expressed between the two phases. Specifically, the expression of five proteins namely, CAC2873, CAP0164, CAP0165, CAC3298, and CAC1742 involved in the solvent production pathway were found to be significantly lower in the stationary phase compared to the exponential growth. Similarly, the expression of fucose isomerase (CAC2610), xylulose kinase (CAC2612), and a putative uncharacterized protein (CAC2611) involved in the xylose utilization pathway were also significantly lower in the stationary phase. These findings provide an insight into the metabolic behavior of C. acetobutylicum between different phases of ABE fermentation using xylose.     

Isolation of Clostridium acetobutylicum strains producing butanol and acetone

Summary A system is described for the isolation of bacteria (Clostridium acetobutylicum) from broad beans, potatoes or maize. The isolates were tested in molasses medium and solvent yields up to 18–20 g/litre of butanol plus acetone were obtained.     

The improvement of glucose/xylose fermentation by Clostridium acetobutylicum using calcium carbonate

Batch fermentation of 60g/l glucose/xylose mixture by Clostridium acetobutylicum ATCC 824 was investigated on complex culture medium. Different proportions of mixtures, ranged between 10 and 50g of each sugar/l, were fermented during pH control at 4.8 (optimum pH for solventogenesis) or during CaCO₃ addition. Using xylose-pregrown cells and pH control, an important amount of xylose was left over at the end of the fermentation when the glucose concentration was higher than that of xylose. The addition of 10g of CaCO₃/l (to prevent the pH dropping below 4.8) increased xylose uptake: a substantial decrease of residual xylose was observed when xylose-pregrown cells as well as glucose-pregrown cells were used as inoculum for all the mixture proportions studied. MgCO₃ (Mg²⁺-containing compound) and CaCl₂ (Ca²⁺-containing compound) reduced residual xylose only during pH control at 4.8 by NaOH addition. As butanol is the major limiting factor of xylose uptake in C. acetobutylicum, fermentations were carried out with or without CaCO₃ in butanol-containing media or in iron deficient media (under iron limitation, butanol synthesis occurred early and could inhibit xylose uptake). Results showed that an excess of CaCOCaCO₃ could increase butanol tolerance which resulted in an increase in xylose utilization. This positive effect seem to be specific to Ca²⁺- or Mg²⁺-containing compounds, going beyond the buffering effect of carbonate.     

Pervaporative butanol fermentation by Clostridium acetobutylicum B18

Extractive acetone-butanol-ethanol (ABE) fermentation was carried out successfully using pervaporation and a low-acid-producing Clostridium acetobutylicum B18. A pervaporation module with 0.17 m(2) of surface area was made of silicone membrane of 240 mum thickness. Pervaporation experiments using make-up solutions showed that butanol and acetone fluxes increased linearly with their concentrations in the aqueous phase. Fickian diffusion coefficients were constants for fixed air flow rates, and increased at higher sweep air flow rates. During batch and fed-batch fermentations, pervaporation at an air flow rate of 8 L/min removed butanol and acetone efficiently. Butanol concentration was maintained below 4.5 g/L even though Clostridium acetobutylicum B18 produced butanol steadily. Pervaporation could not remove organic acids efficiently, but organic acids did not accumulate because strain B18 produced little organic acid and recycled added organic acids efficiently. With pervaporation, glucose consumption rate increased compared to without pervaporation, and up to 160 g/L of glucose was consumed during 80 h. Cell growth was not inhibited by possible salt accumulation or oxygen diffusion through the silicone tubing. The culture volume was maintained relatively constant during fed-batch operation because of an offsetting effect of water and product removal by pervaporation and addition of nutrient supplements. (c) 1994 John Wiley & Sons, Inc.     

Confirmation and elimination of xylose metabolism bottlenecks in glucose phosphoenolpyruvate-dependent phosphotransferase system-deficient Clostridium acetobutylicum for simultaneous utilization of glucose, xylose, and arabinose

Efficient cofermentation of D-glucose, D-xylose, and L-arabinose, three major sugars present in lignocellulose, is a fundamental requirement for cost-effective utilization of lignocellulosic biomass. The Gram-positive anaerobic bacterium Clostridium acetobutylicum, known for its excellent capability of producing ABE (acetone, butanol, and ethanol) solvent, is limited in using lignocellulose because of inefficient pentose consumption when fermenting sugar mixtures. To overcome this substrate utilization defect, a predicted glcG gene, encoding enzyme II of the D-glucose phosphoenolpyruvate-dependent phosphotransferase system (PTS), was first disrupted in the ABE-producing model strain Clostridium acetobutylicum ATCC 824, resulting in greatly improved D-xylose and L-arabinose consumption in the presence of D-glucose. Interestingly, despite the loss of GlcG, the resulting mutant strain 824glcG fermented D-glucose as efficiently as did the parent strain. This could be attributed to residual glucose PTS activity, although an increased activity of glucose kinase suggested that non-PTS glucose uptake might also be elevated as a result of glcG disruption. Furthermore, the inherent rate-limiting steps of the D-xylose metabolic pathway were observed prior to the pentose phosphate pathway (PPP) in strain ATCC 824 and then overcome by co-overexpression of the D-xylose proton-symporter (cac1345), D-xylose isomerase (cac2610), and xylulokinase (cac2612). As a result, an engineered strain (824glcG-TBA), obtained by integrating glcG disruption and genetic overexpression of the xylose pathway, was able to efficiently coferment mixtures of D-glucose, D-xylose, and L-arabinose, reaching a 24% higher ABE solvent titer (16.06 g/liter) and a 5% higher yield (0.28 g/g) compared to those of the wild-type strain. This strain will be a promising platform host toward commercial exploitation of lignocellulose to produce solvents and biofuels.     

Thiolase engineering for enhanced butanol production in Clostridium acetobutylicum

Biosynthetic thiolases catalyze the condensation of two molecules acetyl‐CoA to acetoacetyl‐CoA and represent key enzymes for carbon–carbon bond forming metabolic pathways. An important biotechnological example of such a pathway is the clostridial n‐butanol production, comprising various natural constraints that limit titer, yield, and productivity. In this study, the thiolase of Clostridium acetobutylicum, the model organism for solventogenic clostridia, was specifically engineered for reduced sensitivity towards its physiological inhibitor coenzyme A (CoA‐SH). A high‐throughput screening assay in 96‐well microtiter plates was developed employing Escherichia coli as host cells for expression of a mutant thiolase gene library. Screening of this library resulted in the identification of a thiolase derivative with significantly increased activity in the presence of free CoA‐SH. This optimized thiolase comprised three amino acid substitutions (R133G, H156N, G222V) and its gene was expressed in C. acetobutylicum ATCC 824 to assess the effect of reduced CoA‐SH sensitivity on solvent production. In addition to a clearly delayed ethanol and acetone formation, the ethanol and butanol titers were increased by 46% and 18%, respectively, while the final acetone concentrations were similar to the vector control strain. These results demonstrate that thiolase engineering constitutes a suitable methodology applicable to improve clostridial butanol production, but other biosynthetic pathways involving thiolase‐mediated carbon flux limitations might also be subjected to this new metabolic engineering approach. Biotechnol. Bioeng. 2013; 110: 887–897. © 2012 Wiley Periodicals, Inc.     

In situ butanol recovery from Clostridium acetobutylicum fermentations by expanded bed adsorption

Although butanol is a promising biofuel, its fermentative production suffers from inhibition caused by end product toxicity. The in situ removal of butanol from cultures via expanded bed adsorption offers an effective strategy for mitigating the effects of product toxicity while eliminating the need to clarify cultures via microfiltration. The hydrophobic polymer resin Dowex Optipore L‐493 was found to be both an effective butanol adsorbent and suitable for use in expanded bed adsorption. Recirculation rates through the adsorption column were strongly correlated with and ultimately controlled rates of butanol uptake from the media which, reaching as high as 41.1 g/L h, easily exceed those of its production in a typical fermentation. Vacuum application with vapor collection was found to be an effective means of adsorbent regeneration, with an average of 81% butanol recovery possible, with butanol concentrations in the cold trap reaching as high as 85.8 g/L. Integration of expanded bed adsorption with a fed‐batch Clostridium acetobutylicum ATCC 824 fermentation and its continuous operation for 38.5 h enabled the net production (i.e., in solution and adsorbed) of butanol and total solvent products at up to 27.2 and 40.7 g/L of culture, respectively, representing 2.2‐ and 2.3‐fold improvements over conventional batch culture. While adsorbent biofouling was found to be minimal, further investigation of biofouling in longer‐term studies will provide useful and further insight regarding the robustness of the process strategy. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 30:68–78, 2014     

Continuous butanol production from whey permeate with immobilized Clostridium beyerinckii LMD 27.6

Summary The aim of this study was to find the conditions necessary for the continuous butanol production from whey permeate with Clostridium beyerinckii LMD 27.6, immobilized in calcium alginate beads. The influence of three parameters on the butanol production was investigated: the fermentation temperature, the dilution rate (during start-up and at steady state) and the concentration of calcium ions in the fermentation broth. It was found that both a fermentation temperature of 30° C and a dilution rate of 0.1 h^-1 or less during the start-up phase are required to achieve continuous butanol production from whey permeate. Butanol can be produced continuously from whey permeate in reactor productivities sixteen times higher than those found in batch cultures with free C. beyerinckii cells on whey media.     

电子载体对丁醇发酵的影响

研究在培养基中加入不同电子载体对丁醇发酵的影响。结果表明:添加微量的苄基紫精可以促进丁醇的产生,同时可强烈抑制丙酮的合成,丁醇体积分数由66.92%提高到82.35%。苄基紫精可促进菌株快速进入产溶剂期,发酵周期明显缩短,丁醇生产强度显著提高。7%玉米培养基中加入40 mg/L苄基紫精,丁醇产量最高达16.10 g/L,生产强度为0.37 g/(L.h),分别较对照提高10.96%和60.87%。在初始丁醇体积分数较低的条件下,苄基紫精对丁醇合成的促进作用更明显。