The effect of particle morphology and concentration on the directly measured yield stress in filamentous suspensions

The influence of concentration (mass and volume fraction) and particle morphology on the yielding properties of filamentous broths ofAspergillus niger and Strepto-myces levoris was investigated using the rotating vane technique and compared with those of pulp suspensions. Two methods were applied to determine the volume fraction of the cells growing in filamentous form: the measurement of interstitial volume using a high molecular weight dye or dextran, and the measurement of dewatered broth filter cake volume by displacement using a pycnometer. The latter method provided the most reliable results. Cell concentrations ranging from 3 to 20 g dw/L, with corresponding volume fractions between 0.005 and 0.05, were obtained with broths generated in stirred tank and shake flask fermentations. The yield stress values obtained using the vane technique (0.1 相似文献   

A model for estimating the medium properties of Avicel to ethanol conversion

Simultaneous saccharification and fermentation received an increasing level of attention over recent decades, with the primary focus on the development of improved enzyme and organism performance. Little literature is available on the effects of the various fermentation components on the apparent dynamic viscosity of the fermentation broth for use in reactor design and analysis. This work investigates density and settling properties of Avicel PH-101 particles and the effects of base medium composition, yeast concentration and cellulose particles on the apparent dynamic viscosity of the fermentation mixture. Dynamic viscosity measurements were obtained using a rotational viscometer equipped with a DG 26.7 double gap concentric cylinder measuring system. Results indicated that Avicel particles experience a greater drag force compared to similar sized spherical particles and have a measured density of 1,605.7 kg m^?3. The Ostwäld-de Waele formulation was used to describe the dynamic viscosity of the particles due to it shear-thinning nature. Correlation between the predicted particle effects and experimental results deviated with a root mean square error of 8.46 %.     

Oxygen transfer in slurry bioreactors

The oxygen transfer in bioreactors with slurries having a yield stress was investigated. The volumetric mass transfer coefficients in a 40-L bubble column with simulated fermentation broths, the Theological properties of which were represented by the Casson model, were measured. Experimental data were compared with a theoretical correlation developed on the basis of a combination of Higbie's penetration theory and Kolmogoroff's theory of isotropic turbulence. Comparisons between the proposed correlation and data for the simulated broths show good agreement. The mass transfer data for actual mycelial fermentation broths reported previously by the authors were re-examined. Their Theological data was correlated by the Bingham plastic model. The oxygen transfer rate data in the mycelial fermentation broths fit the predictions of the proposed theoretical correlation.     

Hydrodynamics in bubble column bioreactors with fermentation broths having a yield stress

Summary The hydrodynamics in a bubble column bioreactor with fermentation broths having a yield stress are studied. Specifically, the liquid velocity at the reactor axis, the axial dispersion coefficient, and the gas hold-up are examined. The liquid velocity at the reactor axis and the gas hold-up are measured in a 40-1 bench-scale bubble column fermentor using carboxypolymethylene (Carbopol) aqueous solutions as simulated broths. Theoretical correlations for the liquid velocity at the reactor axis, the axial dispersion coefficient, and the gas hold-up are derived on the basis of an energy balance and the mixing length theory. The correlations are compared with the present data and a reasonable agreement is found. The theoretical predictions are also in satisfactory agreement with the re-examined data for actual fermentation broths which are Chaetomium cellulolyticum and Neurospora sitophila cultured in a 1000-1 pilot-plant scale airlift fermentor.     

Characterization of pellet morphology during submerged growth of Streptomyces tendae by image analysis

Many filamentous bacteria and fungi tend to form pellets, or mixtures of dispersed mycelium and pellets in liquid fermentation broths. In some cases, a specific kind of morphology is required for optimum product yield. When quantitative analysis and characterization of the pellet morphology are needed, an image processing system can be used. It allows a fast and reproducible analysis of the frequency distribution of pellet size, mean pellet size, contents of pellets, or their shape. The use of such a system allows for an on-line analysis. For a demonstration of the method, results of two fermentations of Streptomyces tendae are shown.     

Simultaneous quantification of phytohormones in fermentation extracts of Botryodiplodia theobromae by liquid chromatography–electrospray tandem mass spectrometry

Fermentation broth and biomass from three strains of Botryodiplodia theobromae were characterized by high performance liquid chromatography–electrospray tandem mass spectrometry (HPLC–ESI–MS/MS) method, in order to quantify different phytohormones and to identify amino acid conjugates of jasmonic acid (JA) present in fermentation broths. A liquid–liquid extraction with ethyl acetate was used as sample preparation. The separation was carried out on a C18 reversed-phase HPLC column followed by analysis via ESI–MS/MS. The multiple reaction monitoring mode was used for quantitative measurement. For the first time, indole-3-acetic acid, indole-3-propionic acid, indole-3-butyric acid and JA were identified and quantified in the ethyl acetate extracts from the biomass, after the separation of mycelium from supernatant. The fermentation broths showed significantly higher levels of JA in relation to the other phytohormones. This is the first report of the presence of gibberellic acid, abscisic acid, salicylic acid and the cytokinins zeatin, and zeatin riboside in fermentation broths of Botryodiplodia sp. The presence of JA-serine and JA-threonine conjugates in fermentation broth was confirmed using HPLC-ESI tandem mass spectrometry in negative ionization mode, while the occurrence of JA-glycine and JA-isoleucine conjugates was evidenced with the same technique but with positive ionization. The results demonstrated that the used HPLC–ESI–MS/MS method was effective for analysing phytohormones in fermentation samples.     

Fluid dynamics of liquid egg products

The rheological behavior of liquid egg products (egg yolk, egg white, and whole liquid egg) was studied using a concentric cylinder viscometer. Eggs of three poultry specimens were used: hen (Isa Brown), Japanese quail (Coturnix japonica), and goose (Anser anser f. domestica). Rheological behavior was pseudoplastic and flow curves fitted by the power law model (Herschel–Bulkley and Ostwald–De Waele). The meaning of rheological parameters on friction factors and velocity profiles during flow of liquid egg products in tube has been shown.     

Colorimetric alcohol assays with alcohol oxidase

A method is described for manufacturing crude alcohol oxidase (EC 1.1.3.13) preparations which are suitable for application in colorimetric alcohol assays. The procedure involves a one-step removal of catalase activity from a partially purified preparation of alcohol oxidase from the yeast Hansenula polymorpha via dialysis against 3-amino-1,2,4-triazole and hydrogen peroxide. Thus, the irreversible inactivation of more than 90% of the catalase present was achieved, which is prerequisite for the use of alcohol oxidase preparations in colorimetric alcohol assays via peroxidase-mediated oxidation of dyes. This type of assay was shown to be rapid, accurate and sensitive. The influence of the relative concentrations of the various assay constituents such as alcohol oxidase, catalase and peroxidase is discussed. It is concluded that this colorimetric alcohol assay is particularly suitable for the determination of ethanol in fermentation broths, both in qualitative and in quantitative tests.     

Oxygen transfer to mycelial fermentation broths in an airlift fermentor

Oxygen transfer rates and gas holdups were measured in mycelial fermentation broths of Chaetomium cellulolyticum and Neurospora sitophila, each cultured in a 1300-L pilot-plant-scale airlift fermentor. These cultures exhibited highly non-Newtonian flow behavior coupled with a substantial decrease in oxygen transfer rates. The volumetric mass transfer coefficients in these cultures were found to be 65-70% lower than those in water. The data were compared with the available correlations obtained for simulated fermentation broths. In general, the data for C. cellulolyticum are in satisfactory agreement with the correlations for the model media but the data for N. sitophila are higher than that predicted by the correlations. Model media based correlations are found to be applicable to the fermentation processes if the culture medium does not possess a high yield stress.     

豚草种带内生真菌及其对种子发芽和幼苗生长的影响

内生真菌是一类共生于植物体内,能够不同程度影响宿主植物生态适应性和竞争能力的微生物。分析内生真菌在豚草种子中的分布、种群结构,以及内生真菌发酵液对种子发芽和幼苗生长的作用。结果显示:发生于6个地区的豚草种子均能分离获得内生真菌,分离率在19%—92.63%之间,不同地区之间差异极显著(P0.01)。内生真菌主要存在于种子的总苞部位,分离率达到65.52%。发生于福建省长乐市松下镇的豚草种带内生真菌种群包含5个属,以链格孢属(Alternaria)真菌为优势菌群,占82.26%;其次为镰孢属(Fusarium)真菌,占9.68%;其它3个属的真菌发生较少,均低于5%。内生真菌主要以水平传播方式在豚草不同世代之间传播。供试的7个内生真菌菌株的发酵液均不同程度地抑制豚草种子发芽,降低幼苗地上部高度、根长度、根数量和总生物量,但不同菌株发酵液之间抑制程度差异明显,显示不同菌株对豚草种子发芽和幼苗生长产生不同的影响。内生真菌发酵液处理后的种子仍然保持较高程度的活力;不同内生真菌发酵液处理后,有活力的种子维持在50%—87.5%之间,均高于(或等于)清水处理的种子,说明内生真菌代谢产物只是抑制种子的发芽,但并不导致种子的腐烂和死亡。这些研究结果初步显示种子携带的内生真菌可能在豚草入侵生物学中发挥重要的作用。     

Production of isoprene,one of the high-density fuel precursors,from peanut hull using the high-efficient lignin-removal pretreatment method

Background

Isoprene as the feedstock can be used to produce renewable energy fuels, providing an alternative to replace the rapidly depleting fossil fuels. However, traditional method for isoprene production could not meet the demands for low-energy consumption and environment-friendliness. Moreover, most of the previous studies focused on biofuel production out of lignocellulosic materials such as wood, rice straw, corn cob, while few studies concentrated on biofuel production using peanut hull (PH). As is known, China is the largest peanut producer in the globe with an extremely considerable amount of PH to be produced each year. Therefore, a novel, renewable, and environment-friendly pretreatment strategy to increase the enzymatic hydrolysis efficiency of cellulose and reduce the inhibitors generation was developed to convert PH into isoprene.

Results

The optimal pretreatment conditions were 100 °C, 60 min, 10% (w/v) solid loading with a 2:8 volume ratio of phosphoric acid and of hydrogen peroxide. In comparison with the raw PH, the hemicellulose and lignin were reduced to 85.0 and 98.0%, respectively. The cellulose–glucose conversion of pretreated PH reached up to 95.0% in contrast to that of the raw PH (19.1%). Only three kinds of inhibitors including formic acid, levulinic acid, and a little furfural were formed during the pretreatment process, whose concentrations were too low to inhibit the isoprene yield for Escherichia coli fermentation. Moreover, compared with the isoprene yield of pure glucose fermentation (298 ± 9 mg/L), 249 ± 6.7 and 294 ± 8.3 mg/L of isoprene were produced using the pretreated PH as the carbon source by the engineered strain via separate hydrolysis and fermentation and simultaneous saccharification and fermentation (SSF) methods, respectively. The isoprene production via SSF had a 9.8% glucose–isoprene conversion which was equivalent to 98.8% of isoprene production via the pure glucose fermentation.

Conclusions

The optimized phosphoric acid/hydrogen peroxide combination pretreatment approach was proved effective to remove lignin and hemicellulose from lignocellulosic materials. Meanwhile, the pretreated PH could be converted into isoprene efficiently in the engineered Escherichia coli. It is concluded that this novel strategy of isoprene production using lignocellulosic materials pretreated by phosphoric acid/hydrogen peroxide is a promising alternative to isoprene production using traditional way which can fully utilize non-renewable fossil sources.

     

Effect of the degree of dilution of the antibiotic fermentation broths on the filtration indices]

Dilution of the fermentation broths with water before the mycelium separation lowered the specific cake resistance. The effect of the dilution on the filtration duration was different and depended on the fermentation broth type. As for the erythromycin fermentation broth, the time of its filtration decreased after the dilution, while the filtration time of the fermentation broths of the other 2 antibiotic-producing organisms increased after the dilution.     

Separation of bio‐based chemicals from fermentation broths by salting‐out extraction

The possibility of creating a biorefinery using inexpensive biomass has attracted a great deal of attention, which is mainly focused on the improvement of strains and fermentation, whereas few resources have been spent on downstream processing. Bio‐based chemical downstream processing can become a bottleneck in industrial production because so many impurities are introduced into the fermentation broth. This review introduces a technique referred to as salting‐out extraction, which is based on the partition difference between chemicals in two phases consisting of salts and polymers or hydrophilic solvents, hydrophobic solvents, and amphipathic chemicals. The effects of solvents and salts on the formation of two phases were discussed, as was the use of this method to recover bio‐based chemicals. This review focused on the separation of hydrophilic chemicals (1,3‐propanediol, 2,3‐butanediol, acetoin, and lactic acid) from fermentation broths. Diols could be recovered at a high yield from fermentation broths without pretreatment especially with a hydrophilic solvent‐based system, whereas the recovery of organic acids was slightly lower. Most of the impurities (cells and proteins) were removed during the same step. Extractive fermentations were also used for polymer‐based aqueous two‐phase systems.     

Salting-out extraction and crystallization of succinic acid from fermentation broths

In this study, salting-out extraction (SOE) and crystallization were combined to recover succinic acid from fermentation broths. Of the different SOE systems investigated, the system consisting of organic solvents and acidic salts appeared to be more favorable. A system using acetone and ammonium sulfate was investigated to determine the effect of phase composition and pH. The highest partition coefficient (8.64) and yield of succinic acid (90.05%) were obtained by a system composed of 30% (w/w) acetone and 20% (w/w) ammonium sulfate at a pH of 3.0. Additionally, 99.03% of cells, 90.82% of soluble proteins, and 94.89% of glucose could be simultaneously removed from the fermentation broths. Interestingly, nearly 40% of the pigment was removed using the single-step salting-out extraction process. The analysis of the effect of pH on salting-out extraction indicates that a pH lower than the pK of succinic acid is beneficial for the recovery of succinic acid in an SOE system. Crystallization was performed for the purification of succinic acid at 4 °C and pH 2.0. By combining salting-out extraction with crystallization, an identical total yield (65%) and a higher purity (97%) of succinic acid were obtained using a synthetic fermentation broth compared with the actual fermentation broth (65% and 91%, respectively).     

Determination of the filtration characteristics of the fermentation broths of antibiotic producers]

Main filtration characteristics of the fermentation broths are necessary for estimation of the filtration equipment, rational choice of the filtering apparatus, determination of the optimal conditions for their exploitation. In this connection studies were carried out with a purpose of determining the specific resistance and the content of the solid phase in the fermentation broths of the main antibiotics. It was shown that the above characteristics were closely connected with the biosynthetic conditions and medium composition. It was noted that the specific resistance of the precipitates of the fermentation broths of various antibiotic-producing organisms significantly differed, sometimes by several orders. Preliminary treatment of the fermentation broths before filtration provided a marked decrease in the resistance of the precipitate.     

Aqueous two-phase extraction of 2,3-butanediol from fermentation broths using an ethanol/phosphate system

Separation of 2,3-butanediol from the complex fermentation broths is a difficult task and becomes a bottleneck in industrial production. Aqueous two-phase systems composed of hydrophilic solvents and inorganic salts could be used to extract 2,3-butanediol from fermentation broths. Aqueous two-phase extraction of 2,3-butanediol from fermentation broths was studied by ethanol and dipotassium hydrogen phosphate system. The influences of phase composition on partition of 2,3-butanediol, removal of cells and biomacromolecules were investigated. The partition coefficient and recovery of 2,3-butanediol reached up to 28.34 and 98.13%, respectively, and the selective coefficient of 2,3-butanediol to glucose was 615.87 when the system was composed of 24% (w/w) ethanol and 25% (w/w) dipotassium hydrogen phosphate. Simultaneously, cells and proteins could be removed from the fermentation broths and the removal ratio reached 99.63 and 85.9%, respectively. This process is convenient and economic, furthermore, the operation is easy to scale-up, that is, this method provides a new possibility for the separation and refining of 2,3-butanediol.     

Non-Newtonian behaviour of yeast suspensions

Summary The rheological properties of yeast (Baker's yeast) suspensions in water and in water-methanol-electrolyte solutions have been investigated using a Fann V.G. concentric cylinder viscometer. The resulted rheograms could be described by the power law model for non-Newtonian fluids with the flow behaviour index n<1 indicating pseudo-plastic behaviour. This flow behaviour index was constant under all operating conditions while the consistancy index k increased exponentially with increasing wet yeast volume fraction. The addition of methanol and electrolytes had a negligible effect on the rheological properties. Changing the pH of the suspension acidic to lowered the apparent viscosities.     

A programmable, computer-controlled cone-plate viscometer for the application of pulsatile shear stress to platelet suspensions

Described is a special purpose cone-plate viscometer that is capable of acceleration or deceleration through a step change in speed in less than 0.7s. The speed of the rotating cone is controlled by a microcomputer which can be programmed to generate speed vs time ramp functions of variable slope. Prior calibration of motor power required to shear Newtonian fluids of known viscosity at various speeds provides the basis for determination of apparent suspension viscosity and enables the viscometer automatically to compensate for changing sample viscosity during shear. The viscometer was used to carry out a series of preliminary studies in which platelet-rich plasma (PRP) was subjected to continuous and pulsatile shear stress at 37 degrees C. Shear-induced platelet aggregation (SIPAG) was significantly greater in response to pulsatile versus continuous shearing except at the lowest applied stress (10 dyn/cm2). Increases ranged from about 40 percent at a stress amplitude of 25 dyn/cm2 to nearly 55 percent at dyn/cm2. This increasing trend with stress amplitude might be interpreted as a positive correlation between SIPAG and the loading rate. Dense granule release, as indicated by serotonin release, was dependent on both stress amplitude and number of pulses even at the higher stress where SIPAG was independent of pulse number.     

甘油影响红曲菌产色素的碳源选择性探究

红曲菌(Monascus spp.)是我国重要的药食同源微生物,红曲色素(Monascus pigments,MPs)是其主要次级代谢产物之一。有研究表明,甘油可促进红曲菌产MPs,但作用机制不明。以丛毛红曲菌(Monascus pilosus)MS-1为实验菌株,考察甘油与葡萄糖或蔗糖复合对红曲菌产MPs的影响。在不含碳源的合成培养基中,将甘油与葡萄糖或蔗糖复合,采用分光光度法和高效液相色谱法等分析MPs的产量和组分、生物量及发酵液pH。当甘油与葡萄糖复合,添加甘油后发酵液pH、生物量无显著变化(P0.05),总色价显著降低(P0.05)。当2 g/L或40 g/L甘油与蔗糖复合,发酵液pH显著降低而生物量及总色价显著增加(P0.05)。当40 g/L甘油与蔗糖复合时,总色价是仅以蔗糖为碳源时的16.5倍,且MPs同系物数量明显增多(P0.05)。在合成培养基条件下,甘油促进红曲菌产MPs具有碳源种类的选择性。该结果可为研究甘油影响红曲菌产MPs的作用机制提供参考,为甘油用于MPs生产提供依据。     

The characterization of a viscoelasticity parameter and other rheological properties of various xanthan gum fermentation broths and solutions

Viscoelasticity has important implications in mass transfer and mixing processes. Previous studies regarding to the viscoelastic behaviour of xanthan solutions have been carried out with diluted solutions or they have not covered a wide range of polymer concentrations. In this study, it was shown that the first normal stress difference measured in fermentation broths is highly dependent on shear rate, and this viscoelastic level is modified by the heat treatment to which the broths are subjected as a postfermentative procedure. The viscoelasticity level is different for xanthan solutions prepared with products arising from different sources and for fermentation broths before the heat treatment, if compared with that measured in end-products. In general, the higher the polymer concentration, the higher the viscoelasticity (expressed as first normal stress difference or Weissenberg number). The addition of a biocide, the change in ionic strength and the addition of sucrose to the xanthan solutions, lead to significant changes in the first normal stress difference.List of Symbols A Pa.S^b constant in first normal stress difference power law (N ₁= ) - b constant in first normal stress difference power law (N ₁= ) - c kg m^–3 polymer concentration - K Nsⁿ m^–2 consistency index - N ₁ Pa first normal stress difference - n flow behaviour index - Wi Weissenberg number,N ₁/ - s^–1 shear rate - Pa shear stress - _y Pa Yield stress