A novel, repeated fed-batch, ethanol production system with extremely long term stability achieved by fully recycling fermented supernatants

Using Saccharomyces cerevisiae, a novel, repeated fed-batch ethanol production system from corn flour by fully recycling fermented supernatants is demonstrated. With recovery of ethanol by evaporation coupled with consecutive removal of the insoluble and soluble inhibitory substances accumulated, either completely or partially by filtration, the concentrations of the soluble inhibitors in the system could be maintained at their equilibria. As a result, a sustained high concentration of ethanol (up to 15% v/v) and significant pollution control performance were obtained.     

The production of biocatalysts and biomolecules from extremophiles

The discovery of life in seemingly prohibitive environments continues to challenge conventional concepts of the growth-limiting conditions of many cellular organisms. The diversity of extremophiles has barely been tapped –estimates generally agreeing that <1% of the microorganisms in the environment have been cultivated in pure cultures to date. The production of extremophilic biomass is very important to provide sufficient material for enzyme and biomolecule isolation and characterization, eventually revealing particular features of industrial interest. Hence, special equipment and custom-tailored processes have been developed and are currently under evaluation for the improvement of fermentation productivity. Despite the remarkable opportunities that these uncommon organisms present for biotechnological applications only few instances can be reported for actual exploitation. This lack of progress from the research findings at a laboratory-scale to the actual development of pilot and large-scale production is correlated with the difficulties encountered in extremophile cultivations. Here, we report recent achievements in the production of biomass and related enzymes and biomolecules from extremophile sources, especially focusing on the application of novel fermentation strategies.     

Optimization of exopolysaccharide production by Tremella mesenterica NRRL Y-6158 through implementation of fed-batch fermentation

In liquid culture conditions, the yeast-like fungus Tremella mesenterica occurs in the yeast state and synthesizes an exopolysaccharide (EPS) capsule, which is eventually released into the culture fluid. It is composed of an α-1,3-D-mannan backbone, to which β-1,2 side chains are attached, consisting of D-xylose and D-glucuronic acid. Potato dextrose broth (PDB) seemed to be an excellent medium for both growth of the yeast cells and synthesis of the EPS. This medium is composed solely of an extract of potatoes to which glucose was added. Yet an important disadvantage of this production medium is the presence of starch in the potato extract, since Tremella cells are not capable of metabolizing this component; furthermore, it coprecipitates upon isolation of the polymer [3]. In this respect, it was essential to remove the starch in order to achieve high polysaccharide production and recovery. A good method was the removal of starch through ultrafiltration of the PDB medium before inoculation of the strain. This resulted in an excellent starch-free medium in which other components essential for polysaccharide production were still present [3]. Through implementation of single and cyclic fed-batch fermentations with glucose feed, 1.6- and 2.2-fold increases in EPS yield were obtained, respectively. Lowering the carbon source level by using a cyclic fed-batch technique might decrease the osmotic effect of glucose or any catabolite regulation possibly exerted by this sugar on enzymes involved in EPS synthesis. Journal of Industrial Microbiology & Biotechnology (2002) 29, 181–184 doi:10.1038/sj.jim.7000276 Received 18 March 2002/ Accepted in revised form 20 May 2002     

Rapid intensification of an established CHO cell fed-batch process

Currently, the mammalian biomanufacturing industry explores process intensification (PI) to meet upcoming demands of biotherapeutics while keeping production flexible but, more importantly, as economic as possible. However, intensified processes often require more development time compared with conventional fed-batches (FBs) preventing their implementation. Hence, rapid and efficient, yet straightforward strategies for PI are needed. In this study we demonstrate such a strategy for the intensification of an N-stage FB by implementing N-1 perfusion cell culture and high inoculum cell densities resulting in a robust intensified FB (iFB). Furthermore, we show successful combination of such an iFB with the addition of productivity enhancers, which has not been reported so far. The conventional CHO cell FB process was step-wise improved and intensified rapidly in multi-parallel small-scale bioreactors using N-1 perfusion. The iFBs were performed in 15 and 250 ml bioreactors and allowed to evaluate the impact on key process indicators (KPI): the space–time yield (STY) was successfully doubled from 0.28 to 0.55 g/L d, while product quality was maintained. This gain was generated by initially increasing the inoculation density, thus shrinking process time, and second supplementation with butyric acid (BA), which reduced cell growth and enhanced cell-specific productivity from ~25 to 37 pg/(cell d). Potential impacts of PI on cell metabolism were evaluated using flux balance analysis. Initial metabolic differences between the standard and intensified process were observed but disappeared quickly. This shows that PI can be achieved rapidly for new as well as existing processes without introducing sustained changes in cellular and metabolic behavior.     

Acetate-mediated pH-stat fed-batch cultivation of transconjugant <Emphasis Type="Italic">Enterobacter</Emphasis> sp. BL-2S over-expressing <Emphasis Type="Italic">glmS</Emphasis> gene for excretive production of microbial polyglucosamine PGB-1

A unique cationic polyglucosamine biopolymer PGB-1 comprising more than 95% D-glucosamine was excretively produced from a new bacterial strain Enterobacter sp. BL-2 under acetate-mediated culture conditions. Since the biopolymer PGB-1 could be synthesized from the UDP-N-acetylglucosamine monomer derived from the hexosamine pathway, three glmS, glmM, and glmU genes in the hexosamine pathway were cloned from Enterobacter sp. BL-2, and their molecular structures were elucidated. The cloned glmS, glmM, and glmU genes were reintroduced into the parent strain Enterobacter sp. BL-2 through a conjugative transformation for the overproduction of the biopolymer PGB-1. The biopolymer production increased 1.5-fold in the transconjugant Enterobacter sp. BL-2S over-expressing the first-step glmS gene encoding glucosamine-6-phosphate synthase. The transconjugant Enterobacter sp. BL-2S was cultivated pH-stat fed-batch widely, while intermittently feeding an acetate solution to maintain a constant pH level of 8.0 for 72 h, resulting in 1.15 g/L of the extracellular polyglucosamine biopolymer PGB-1.     

Production of Alkaline Protease with <Emphasis Type="Italic">Teredinobacter turnirae</Emphasis> in Controlled Fed-batch Fermentation

By using our previously optimized media and a fed-batch operation controlled by LabVIEW Software, the key parameter for a high production of alkaline protease using the marine bacterium, Teredinobacter turnirae, was to maintain a low concentration of C and N-sources ( < 2 g sucrose l⁻¹ and < 0.2 g NH₄C l l⁻¹) using an appropriate fed-batch culture system. A maximum protease activity of 8250 U ml⁻¹ was thus achieved.     

Comparative proteome analysis of robust <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> insights into industrial continuous and batch fermentation

A robust Saccharomyces cerevisiae strain has been widely applied in continuous and batch/fed-batch industrial fermentation. However, little is known about the molecular basis of fermentative behavior of this strain in the two realistic fermentation processes. In this paper, we presented comparative proteomic profiling of the industrial yeast in the industrial fermentation processes. The expression levels of most identified protein were closely interrelated with the different stages of fermentation processes. Our results indicate that, among the 47 identified protein spots, 17 of them belonging to 12 enzymes were involved in pentose phosphate, glycolysis, and gluconeogenesis pathways and glycerol biosynthetic process, indicating that a number of pathways will need to be inactivated to improve ethanol production. The differential expressions of eight oxidative response and heat-shock proteins were also identified, suggesting that it is necessary to keep the correct cellular redox or osmotic state in the two industrial fermentation processes. Moreover, there are significant differences in changes of protein levels between the two industrial fermentation processes, especially these proteins associated with the glycolysis and gluconeogenesis pathways. These findings provide a molecular understanding of physiological adaptation of industrial strain for optimizing the performance of industrial bioethanol fermentation. Electronic supplementary material  The online version of this article (doi:) contains supplementary material, which is available to authorized users.     

Powdered activated carbon added biological treatment of pre-treated landfill leachate in a fed-batch reactor

Biological treatment of landfill leachate usually results in low treatment efficiencies because of high chemical oxygen demand (COD), high ammonium-N content and also presence of toxic compounds such as heavy metals. A landfill leachate with high COD content was pre-treated by coagulation-flocculation followed by air stripping of ammonia at pH = 12. Pre-treated leachate was biologically treated in an aeration tank operated in fed-batch mode with and without addition of powdered activated carbon (PAC). PAC at 2 g l^–1 improved COD and ammonium-N removals resulting in nearly 86% COD and 26% NH₄-N removal.     

Production of poly(3-hydroxybutyric acid) by fed-batch culture of Alcaligenes eutrophus with glucose concentration control

Alcaligenes eutrophus NCIMB 11599 was cultivated to produce poly(3-hydroxybutyric acid) (PHB) from glucose by the automatic fed-batch culture technique. The glucose concentration of the culture broth was controlled at 10 to 20 g/L by two methods: using exit gas data obtained from a mass spectrometer and using an on-line glucose analyzer. The effect of ammonium limitation on PHB synthesis at different culture phases was studied. The final cell concentration, PHB concentration, and PHB productivity increased as ammonia feeding was stopped at a higher cell concentration. High concentrations of PHB (121 g/L) and total cells (164 g/L) were obtained in 50 h when ammonia feeding was stopped at the cell concentration of 70 g/L. The maximum PHB content reached 76% of dry cell weight and the productivity was 2.42 g/L h with the yield of 0.3 g PHB/g glucose.     

植物乳杆菌Lp-2的高密度发酵

高密度培养植物乳杆菌是制作其发酵剂的重要环节。首先,研究了不同的溶氧和pH对植物乳杆菌的分批发酵的影响。在分批发酵的基础上,为进一步提高发酵液中的菌体浓度,进行了补料分批发酵实验。最终通过对蔗糖反馈补料发酵试验对比改造获得了pH反馈补料发酵工艺。此发酵补料工艺可以控制蔗糖残糖量始终处于较低的水平,因此获得了最高的菌体产量。菌体干重达到13.56g/L,较分批培养提高90.05%。