Continuous production of citric acid with recirculation of the fermentation broth after product recovery

For the production of citric acid a four stage process consisting of the fermentation stage, extraction stage, reextraction stage and product stage has been tested. The present paper discusses the results of the extraction and the reextraction stage. Further a fermentation with recirculation of the fermentation broth after the product recovery is explained. The product recovery is achieved by a liquid–liquid extraction in a spray column.     

Computer modeling of antibiotic fermentation with on-line product removal

The fermentation of Streptomyces griseus for the production of cycloheximide is similar to other antibiotic fermentations in that product synthesis is subject to feedback regulation and the desired product is degraded in the fermentation broth. The productivity of this fermentation can thus be dramatically increased by removing the antibiotic from the whole broth as it is produced. One means for effecting this on-line product removal is to contact the whole fermentation broth with neutral polymeric resin immobilized in hydrogel beads. The antibiotic adsorbs to the immobilized resin via hydrophobic interactions. In this work, the adsorption of the antibiotic onto the immobilized resin was characterized. A biochemical model of the fermentation was then used to describe the time profiles of biomass, substrate, and antibiotic in a fermentation system in which whole broth is circulated from the fermentor through a continuously stirred extractor containing the adsorbent beads. Various operating conditions were examined to optimize the productivity of the fermentation.     

甾体1，4-脱氢和11α-羟基化反应的两种不同微生物转化

Two kinds of micro-organism, Arthrobacter sp. AX86(1,4-dehdrogenator)and Absidia sp. A28(11α-hydroxylator) were used in this experiment. Two different fermentation techniques were performed to accomplish the multiple conversional reactions for producing 16β-methyl-11α, 17α, 21-trihydroxy-1,4-pregnadiene-3,20-dione (Ⅲ) from 16β-methyl-3β, 17α,21-trihydroxy-5α-pregnane-20-one-21-acetate(1) 1)To produce product(Ⅲ)by means of a two-step fermentation method which were independently performed first by Arthrobacter and next by Abslaia, and 2)the product was obtained by a sequential fermentation system of aforesaid two micro-organisms in a single fermentor without isolation of the intermediates from the mixture. Our results showed that in both fermentation systems high yield of product was obtained. However, according to the technical simplicity, shorter duration of fermentation cycle and efficient yield of product, the second method is better than the first one.     

Rheological properties of chromosomal and plasmid DNA during alkaline lysis reaction

The experimental apparatus for the simultaneous L-lactic acid fermentation by Rhizopus oryzae immobilized in calcium alginate beads and product separation process was set up in which a three-phase fluidized-bed bioreactor was used as a fermentor and an external electrodialyzer as a separator, and a pump was applied to recycle the fermentation broth between the bioreactor and the separator. The L-lactic acid produced in the fermentor was separated in the separator, product inhibition was alleviated without any addition of alkali or alkali salts and the product purification process could be simplified. The specific productivity and the yield in electrodialysis fermentation (ED-F) process operated in continuous feeding mode were almost the same as that in CaCO₃-buffered fermentation process. A mathematical model of L-lactic acid production in ED-F process was also suggested, in which the model equations for the bioreactor and the electrodialyzer were combined to describe the simultaneous fermentation and product separation. The model predictions were in good agreement with the experimental data.     

Aqueous two-phase: the system of choice for extractive fermentation

Extractive fermentation in aqueous two-phase systems is a meaningful approach to overcome low product yield in a conventional fermentation process, and by proper design of the two-phase system it is possible to obtain the product in a cell-free stream. The characteristics of an aqueous two-phase system, various polymers used for forming an aqueous two-phase system, the physicochemical parameters of the aqueous two-phase system, partitioning of biomolecules and cell mass and the effect of individual phase forming polymers on cell growth and product formation are reviewed in this article. The various extractive fermentation processes are also summarised here. At the end, the economic viability and scope of aqueous two-phase fermentation are briefly discussed in relation to the wider application of this topic. Received: 16 June 1999 / Received revision: 29 December 1999 / Accepted: 4 January 2000     

大豆蛋白复合酶解产物在促微生物生长和发酵中的初步应用研究

为探讨大豆蛋白复合酶解产物在促微生物生长和发酵中的可行性,利用2709碱性蛋白酶和中性纤维素酶复合酶解大豆蛋白,酶解产物经干燥、粉碎后添加到培养基中,通过接种微生物观察其生长状况和发酵情况表征效果。研究发现,大豆蛋白复合酶解产物可以促进微生物生长和发酵产酶,试验结论为微生物培养提供了新的代谢资源。     

Routine manufacture of recombinant proteins using expanded bed adsorption chromatography

Two different recombinant human proteins were purified directly from Pichia pastoris whole cell fermentation broth, containing 30–44% biomass (wet weight percent), by strong cation exchange expanded bed adsorption chromatography. Expanded bed adsorption chromatography provided clarification, product purification and product concentration in a single unit operation at large scale (2000-l nominal fermentation volume). The efficiency of expanded bed adsorption chromatography resulted in a short process time, high process yield, and limited proteolytic degradation of the target proteins. The separations were operated using a 60-cm (d) column run at 14 l/min. For one protein, expanded bed adsorption chromatography resulted in an average product recovery of 113% (relative to fermentation supernatant) and a purity of 89% (n=10). For the other protein, the average product recovery was 99% (relative to fermentation supernatant) and the purity was 62.1 (n=10). Laboratory experiments showed that biomass reduced product dynamic binding capacity for protein 2.     

IN SITU SEPARATION OF ETHANOL WITH AQUEOUS TWO-PHASE SYSTEM AND ASSESSMENT OF KLa FOR YEAST GROWTH IN BATCH CULTIVATION

In the fermentation process, the separation of product and its purification is the most difficult and exigent task in the ground of biochemical engineering. Another major problem that is encountered in the fermentation is product inhibition, which leads to low conversion and low productivities. Extractive fermentation is a technique that helps in the in situ removal of product and better performance of the fermentation. An aqueous two-phase system was employed for in situ ethanol separation since the technique was biofriendly to the Saccharomyces cerevisiae and the ethanol produced. The two-phase system was obtained with polyethylene glycol 4000 (PEG 4000) and ammonium sulfate in water above critical concentrations, with the desire that the ethanol moves to the top phase while cells rest at the bottom. The overall mass transfer coefficient (K_La) was also estimated for the yeast growth at different rpm. The concentration and yield of ethanol were determined for conventional fermentation to be around 81.3% and for extractive fermentation around 87.5% at the end of the fermentation. Based on observation of both processes, extractive fermentation was found to be the best.     

蛹虫草菌胞外多糖发酵及其发酵动力学

蛹虫草菌(Cordyceps militaris)胞外多糖(EPS)的发酵过程和发酵动力学进行了研究。基于Logitic方程和Luedeking-Piret方程,得到了描述发酵过程的动力学数学模型和模型参数,同时对实验数据与模型进行了验证比较。模型计算与实验结果拟合良好,模型正确地反应了蛹虫草菌胞外多糖的发酵过程及其动力学机制。     

Use of in situ solid-phase adsorption in microbial natural product fermentation development

It has been half a century since investigators first began experimenting with adding ion exchange resins during the fermentation of microbial natural products. With the development of nonionic polymeric adsorbents in the 1970s, the application of in situ product adsorption in bioprocessing has grown slowly, but steadily. To date, in situ product adsorption strategies have been used in biotransformations, plant cell culture, the production of biofuels, and selected bulk chemicals, such as butanol and lactic acid, as well as in more traditional natural product fermentation within the pharmaceutical industry. Apart from the operational gains in efficiency from the integration of fermentation and primary recovery, the addition of adsorbents during fermentation has repeatedly demonstrated the capacity to significantly increase titers by sequestering the product and preventing or mitigating degradation, feedback inhibition and/or cytotoxic effects. Adoption of in situ product adsorption has been particularly valuable in the early stages of natural product-based drug discovery programs, where quickly and cost-effectively generating multigram quantities of a lead compound can be challenging when using a wild-type strain and fermentation conditions that have not been optimized. While much of the literature involving in situ adsorption describes its application early in the drug development process, this does not imply that the potential for scale-up is limited. To date, commercial-scale processes utilizing in situ product adsorption have reached batch sizes of at least 30,000 l. Here we present examples where in situ product adsorption has been used to improve product titers or alter the ratios among biosynthetically related natural products, examine some of the relevant variables to consider, and discuss the mechanisms by which in situ adsorption may impact the biosynthesis of microbial natural products.     

Batch and continuous butanol fermentations with free cells: integration with product recovery by gas-stripping

Summary In a butanol batch fermentation the substrate consumption was increased threefold using in-situ product recovery by gas-stripping, in comparison with a control fermentation without product recovery. In a continuous fermentation in-situ recovery led to an increase in the biomass concentration, resulting in a threefold increase in productivity. The substrate consumption was increased by 10%. An external stripper was used as apparatus for the butanol recovery.     

Production of ethanol by coupling fermentation and solvent extraction

Summary A new technology of fermentation is proposed. The inhibitor product is removed continuously by coupling fermentation and solvent extraction. Applied to ethanol fermentation this technology is suitable to any case where the terminal product is inhibitory.The proposed technology uses both plug flow reactor and liquid-liquid extraction to achieve continuously the extractive fermentation of ethanol. The solvent used for liquid-liquid extraction is dodecanol. A new reactor was used. It is a column packed with a porous material . The fermentation broth is pulsed (a) to increase the interfacial area between the liquid medium and the dodecanol, and (b) to: decrease the gas hold up.Alcoholic fermentations were performed on glucose syrup at 35°C using Saccharomyces cerevisiae, with adsorbed cells as reference, with adsorbed cells and extractive fermentation. The results show that the fermentation is substantially improved. By this new method the ethanol productivity was multiplied by 5 and a solution of 407 g/l of glucose was totally fermented with a yeast which cannot normally transform more than 200 g/l glucose.     

Assessing viability and cell-associated product of recombinant protein producing Pichia pastoris with flow cytometry

This paper describes the establishment of flow cytometric methods for recombinant Pichia pastoris strains, and their application to a lab scale fed batch fermentation. Using a strain which secretes human trypsinogen, the viability and the product which remained associated to the cell were measured with propidium iodide and immunofluorescent staining, respectively. Viability decreases significantly below 70% during the methanol fed batch phase, indicating a stress situation triggered by the fermentation conditions. Cell associated product is accumulated earlier after methanol induction than secreted product. These data demonstrate that flow cytometry is a powerful tool for the analysis and optimization of recombinant protein production processes, and they indicate the need to further improve a widely used fermentation protocol for P. pastoris.     

Modeling of an integrated fermentation/membrane extraction process for the production of 2-phenylethanol and 2-phenylethylacetate

An unstructured model for an integrated fermentation/membrane extraction process for the production of the aroma compounds 2-phenylethanol and 2-phenylethylacetate by Kluyveromyces marxianus CBS 600 was developed. The extent to which this model, based only on data from the conventional fermentation and separation processes, provided an estimation of the integrated process was evaluated. The effect of product inhibition on specific growth rate and on biomass yield by both aroma compounds was approximated by multivariate regression. Simulations of the respective submodels for fermentation and the separation process matched well with experimental results. With respect to the in situ product removal (ISPR) process, the effect of reduced product inhibition due to product removal on specific growth rate and biomass yield was predicted adequately by the model simulations. Overall product yields were increased considerably in this process (4.0 g/L 2-PE+2-PEA vs. 1.4 g/L in conventional fermentation) and were even higher than predicted by the model. To describe the effect of product concentration on product formation itself, the model was extended using results from the conventional and the ISPR process, thus agreement between model and experimental data improved notably. Therefore, this model can be a useful tool for the development and optimization of an efficient integrated bioprocess.     

固态发酵苦荞制备多肽菌种的筛选

【目的】筛选固态发酵苦荞高产多肽及发酵产物液具有抗菌、抗氧化活性的菌株。【方法】采用米曲霉、酱油曲霉、雅致放射毛霉和少孢根霉分别对苦荞进行固态发酵,以蛋白酶活力、水解度、可溶性肽得率、抑菌率和体外自由基清除率作为筛菌指标。【结果】米曲霉固态发酵苦荞的可溶性肽得率最高达38.83%±1.18%,发酵产物液对大肠杆菌和金黄色葡萄球菌的抑菌率分别为96.62%±1.66%和97.54%±0.54%,同时羟自由基(·OH)清除率和二苯基苦味酰基苯肼自由基(DPPH·)清除率分别为55.65%±1.25%和10.84%±1.03%。对米曲霉发酵2 d发酵产物液的不同分子量分布及活性分析表明,分子量大小对抗菌及抗氧化活性有一定的影响。【结论】米曲霉可作为固态发酵苦荞制备多肽且发酵产物液具有抗菌及抗氧化活性的最佳菌株,并在多肽产量提升及抗菌、抗氧化活性的研究上具有巨大空间。     

Optimization of L-phenylalanine production of Corynebacterium glutamicum under product feedback inhibition by elevated oxygen transfer rate.

Production feedback inhibition both on cell growth and on product formation of phenylalanine fermentation might be alleviated by elevated oxygen supply. Batch fermentations by a high phenylalanine producing strain Corynebacterium glutamicum CCRC 18335 at various initial phenylalanine concentrations (P(0)) ranging from 0 to 20 g/L and different oxygen transfer rate coefficients (K(L)a) ranging from 23 to 76 h(-1) were studied. The fermentation parameters with respect to P(0) were strongly dependent on K(L)a. Cell yield favored higher K(L)a and lower P(0). Product yield with respect to varying phenylalanine concentration was evaluated by the relative oxygen availability (ROA). The optimal ROA for phenylalanine formation was strongly dependent on the product concentration. While P(0) was low, the product inhibition was less significant and the maximum product yield occurred while ROA was at 0.5-0.6. While P(0) was high, the product inhibition was significant and the maximum product yield occurred while ROA was at 0.8-0.9. These results suggest that the product feedback inhibition of phenylalanine fermentation processes can be alleviated by a gradual increase in oxygen supply rate while the increasing product concentration is taken into account. The strategy is demonstrated in a fed-batch culture with elevated oxygen supply. The final phenylalanine concentration was 23.2 g/L, which was 45% better than that of the fed-batch fermentation without elevated oxygen supply. Likewise, the maximum productivity was improved by 42% at 0.37 g/(L x h).     

Model aided dynamic process analysis and optimization for the nourseothricin fermentation

The relation between product formation and growth kinetics could be characterized by two facts: the specific product formation rate depends on the ageing of the population and on the specific growth rate. These relation was formulated and quantified by a mathematical model, which was fitted to experimental data of a representative fermentation run und used to predict an optimal fermentation mode. In the result of this discussion cyclic fed batch fermentation was found to be optimal.     

Stimulation of malo-lactic fermentation in eastern grape musts

Induced malo-lactic fermentation was stimulated in Eastern grape musts by the addition of a new fermentation enhancer product.     

Influence of solid substrate fermentation on the chemical composition of chickpea

A basic procedure was developed to produce a fermented product by solid substrate fermentation using Rhyzopus oligosporus and chickpea as substrate. Water activity was kept at 0.92 throughout the process. Fermentation increased total, ‘true’ and soluble proteins, soluble solids and soluble carbohydrates, and decreased fiber content and pH. About 12% of solids were lost during 72 h of fermentation. The content of most fatty acids was enhanced by fermentation, whereas peroxide value and tannins declined. The color of the fermented product was not deteriorated after 72 h of fermentation. Scanning electron microscopy studies of microbial growth on the substrate showed penetration of the fungus hyphae and degradation effects on the chickpea cotyledon cells.     

Design and evaluation of a continuous semipartition bioreactor for in situ liquid‐liquid extractive fermentation

Extractive fermentation (or in situ product removal (ISPR)) is an operational method used to combat product inhibition in fermentations. To achieve ISPR, different separation techniques, modes of operation and physical reactor configurations have been proposed. However, the relative paucity of industrial application necessitates continued investigation into reactor systems. This article outlines a bioreactor designed to facilitate in situ product extraction and recovery, through adapting the reaction volume to include a settler and solvent extraction and recycle section. This semipartition bioreactor is proposed as a new mode of operation for continuous liquid‐liquid extractive fermentation. The design is demonstrated as a modified bench‐top fermentation vessel, initially analysed in terms of fluid dynamic studies, in a model two‐liquid phase system. A continuous abiotic simulation of lactic acid (LA) fermentation is then demonstrated. The results show that mixing in the main reaction vessel is unaffected by the inserted settling zone, and that the size of the settling tube effects the maximum volumetric removal rate. In these tests the largest settling tube gave a potential continuous volumetric removal rate of 7.63 ml/min; sufficiently large to allow for continuous product extraction even in a highly productive fermentation. To demonstrate the applicability of the developed reactor, an abiotic simulation of a LA fermentation was performed. LA was added to reactor continuously at a rate of 33ml/h, while continuous in situ extraction removed the LA using 15% trioctylamine in oleyl alcohol. The reactor showed stable LA concentration of 1 g/L, with the balance of the LA successfully extracted and recovered using back extraction. This study demonstrates a potentially useful physical configuration for continuous in situ extraction.