Zeta potential as a measure of polyelectrolyte flocculation and the effect of polymer dosing conditions on cell removal from fermentation broth

Characterization of flocculation for cell removal from fermentation broth via polyelectrolyte addition is commonly based on qualitative methods such as physical appearance of the floc. The use of zeta potential as a quantitative measure of floc character was evaluated as an indicator of optimal polymer addition. Zeta potential was found to increase with increasing cationic polyelectrolyte dosage, but never reached zero regardless of the total amount of polymer added, indicating flocculation occurs at least partially through a bridging type mechanism. Experiments were conducted using various polymer concentrations (25-75 g/L) and dosing methods (batch, incremental and continuous addition) that resulted in variable overall polymer requirements to achieve optimum flocculation. Zeta potential was found to be constant at optimal floc character regardless of the total amount of polymer added, polymer concentration, or method of polymer addition. Experiments with two additional types of fermentation broth also showed characteristic zeta potentials at optimal flocculation. Polymer requirements to achieve a particular floc character can vary greatly, depending on polymer dosing conditions and fermentation batch. The effect of polymer dosing conditions on the polymer requirement to obtain optimal floc character was evaluated. Polymer dosing method and calcium concentration were both found to have a significant effect (P < 0.0001) with continuous polymer addition and high calcium concentration requiring less polymer than did batch polymer addition and low calcium concentration, respectively. Polymer dosing concentration did not significantly affect polymer requirement for optimal flocculation.     

微生物絮凝剂产生菌固定化条件的优化

采用多种固定化方法及载体,进行了微生物絮凝剂产生菌M09固定化方法及条件的研究,并对其所产絮凝剂在不同存储条件下絮凝活性的稳定性进行探讨。结果表明,选用粒径为0.5 cm×0.5 cm×0.5 cm的多孔聚氨酯泡沫为固定化载体,4 g/L的固液比,使用初始蔗糖浓度为2%,NaNO3为0.4%的培养基,28℃振荡培养60 h可获得较高活性的固定化细胞,发酵上清液能够保持较高的絮凝率。研究还发现,在室温条件下,利用此工艺所产高絮凝活性发酵液在含有菌体的反应器内自然静置,发酵液絮凝率仍可缓慢持续上升,维持较高水平达数日,具有较高的稳定性。     

The use of laminar tube flow in the study of hydrodynamic and chemical influences on polymer flocculation of Escherichia coli

The optimization of microbial flocculation for subsequent biomass separation must relate the floc properties to separation process criteria. The effects of flocculant type, dose, and hydrodynamic conditions on floc formation in laminar tube flow were determined for an Escherichia coli system. Combined with an on-line aggregation sensor, this technique allows the flocculation process to be rapidly optimized. This is important, because interbatch variation in fermentation broth has consequences for flocculation control and subsequent downstream processing. Changing tube diameter and length while maintaining a constant flow rate allowed independent study of the effects of shear and time on the flocculation rate and floc characteristics. Tube flow at higher shear rates increased the rate and completeness of flocculation, but reduced the maximum floc size attained. The mechanism for this size limitation does not appear to be fracture or erosion of existing flocs. Rearrangement of particles within the flocs appears to be most likely. The Camp number predicted the extent of flocculation obtained in terms of the reduction in primary particle number, but not in terms of floc size. (c) 1992 John Wiley & Sons, Inc.     

肌苷发酵液絮凝除菌体的研究

目前国内肌苷生产厂家普遍采用的提取方法是“双柱法”,即先用阳离子柱吸附,然后再用炭柱吸附。该方法不但周期长,工作量大,能耗高,而且提取收率低,一般只有60％左右,使我国肌苷的生产成本大大提高。因此,寻求新的提取方法,降低生产成本,是肌苷生产厂家及有关科技人员所共同关注的问题。肌苷发酵液的除菌体就是新法提取的步骤之一,它可以省去阳离子吸附柱,直接采用炭柱吸附,采用此法可使提取周期大大缩短,降低能耗,提高提取收率。 肌苷菌体较难清除,本研究采用能耗低、易操作,工作量小的絮凝方法,所用的絮凝剂为天然无毒物质,因此沉淀菌体可用作饲料蛋白,起到一举两得的作用。     

Use of a rotation chart for studying the flocculation of admixtures in native solutions]

The process of admixture flocculation in fermentation broth filtrates of penicillin was studied experimentally according to the schemes of rotatabel planning of the 2nd order. Equations describing the effect of the main factors on the process were worked out and the main effects of the pair interactions were found.     

絮凝基因内衔接重复序列与酵母菌絮凝特性多样性及遗传稳定性

存在于酵母菌细胞表面的絮凝蛋白与邻近细胞表面寡聚甘露糖链相互作用,从而使细胞相互聚集形成细胞团的生理过程称为酵母菌絮凝。编码絮凝蛋白的基因中存在大量衔接重复序列,这些重复序列的变化不但使酵母菌呈现出絮凝特性的多样性,而且由重复序列驱动的基因内或基因间重组使酵母菌的絮凝特性具有非常明显的遗传不稳定性。文中综述了基因内重复序列对酵母菌絮凝特性和遗传稳定性的影响,将为基于序列调控策略改进酵母菌絮凝特性及遗传稳定性奠定理论基础,为絮凝特性在发酵工业或环境修复过程中的可控应用提供新的解决策略。     

Treatment and clarification of fermented broth in bacterial enzyme production

Summary Acetic acid, calcium chloride, aluminium sulphate and polyacrylamide were tried for flocculation and settling of suspended solids. Adjustment of pH, centrifugation, precoat filtration with filter aid were studied for clarification of fermentation broth in alpha-amylase production. Combination of aluminium sulphate and polyacrylamide as flocculating agents and precoat filtration was found to be the best strategy for alpha-amylase enzyme recovery from the broth.     

发酵抑制物对絮凝酵母戊糖发酵的影响

将絮凝剂加入酵母溶液中,使酵母絮凝成颗粒以此作为固定化酵母进行戊糖发酵。研究了常见发酵抑制物(甲酸、乙酸、糠醛和乳酸等)对絮凝酵母发酵木糖的影响。结果表明:在60.0g/L木糖发酵液中,经过24h发酵,木糖利用率达94.6%,当分别添加抑制物甲酸、乙酸、糠醛、乙醇和乳酸时,聚氧乙烯絮凝酵母分别对其的耐受浓度为0.5、0.5、1.0、30.0和8.0g/L。当抑制物添加量超过各自的耐受浓度后,对絮凝酵母发酵会产生明显的抑制作用。     

Differential spectrophotometric method of analysing levorin in the culture broth and in the mycelium]

It was shown on model experiments that the microbiological method was not applicable for determination of levorin content in industrial intermediate products containing in addition levoristatin, since the presence of the latter made higher the results of the microbiological assay. Because of this till to the present date the quantitative content of levorin in the industrial intermediate products was determined photometrically using alcohol (pure solvent) as the reference solution. Still, this method also made higher the results of the assay, especially when the content of levorin was determined in the fermentation broth. In the solid phase levorin is contained in the mycelium which occupies only 1 to 2 per cent of the fermentation broth, while the liquid phase or the fermentation broth filtrate occupies 98 to 99 per cent. It was found that the fermentation broth filtrate contained protein admixtures which coagulated on addition of alcohol to the fermentation broth and formed fine colloid solutions. As a result the absorption values became higher. In the present study not the pure solvent but an extract of the fermentation broth filtrate containing neither levorin, nor levoristatin was used as the reference solution. Such a differential method provided elimination of all errors due to the presence of various metabolites in the fermentation broth filtrate which varied both qualitatively and quantitatively.     

Continuous ethanol fermentation of concentrated sugar solutions coupled with membrane distillation using a PTFE module

Continuous ethanol fermentation of concentrated glucose and molasses solutions was coupled with membrane distillation using a PTFE ethanol stripping module. Experimental results indicated that the PTFE module can remove a high concentration of ethanol from the fermentation broth and thus maintain a low ethanol concentration in the broth, thereby alleviating the problem of product inhibition. Accordingly, the product yield and the specific ethanol production rate increased. During the continuous fermentation runs, long-time operation using the PTFE module was found to be possible (i.e. 430 h using the glucose medium and 695 h using the molasses medium) and no significant change in the ethanol separation performance of the PTFE module was observed. Although cell flocculation became undetectable when a concentrated molasses medium containing 316 g/l sugar solution was used, the ethanol separation performance of the ethanol stripper was not adversely affected by the presence of the free cells. This suggests that clogging of the membrane pores by cells or other particulates is not a major problem when using the PTFE module in continuous ethanol fermentation.     

An efficient method for separation of surfactin from Bacillus amyloliquefaciens fmb50 broth by flocculation

An efficient method for removing microbial cells and macromolecular impurities and purification of surfaction from fermentation broth produced by Bacillus amyloliquefaciens fmb50 was carried out in this study. Among three inorganic flocculants and a macromolecular flocculants, the combination use of CaCl₂ and Na₂HPO₄ was the most effective separation process. Addition of 50% ethanol into fermentation broth could not only disrupt the surfactin micells, but also promote the permeating of surfactin in filtration. The flocculation condition was optimized by an L₉ (3⁴) orthogonal design. The light transmittance, surfactin recovery rate, protein removal rate and filtration flux could reach to 96.3%, 95.31%, 56.59% and 3204.41 L m⁻² h⁻¹ respectively, the surfactin purity reached to 79.5% and the residual protein was 8.1% in separated product under the optimal flocculation condition (flocculants dosage 0.5%, pH 5.0, and temperature 35 °C). Validation test also demonstrated stable results under the optimal conditions. Due to higher efficiency, lower cost and scale-up more easily of flocculation and filtration processes, it is feasible to separate surfactin from fermentation broth.     

Identification and functional study of a new FLO10-derivative gene from the industrial flocculating yeast SPSC01

Yeast flocculation is an important property for the brewing industry as well as for ethanol fermentation to facilitate biomass recovery by sedimentation from the fermentation broth, which is cost-effective. In this study, a new flocculating gene FLO10 (spsc) of 4,221 bp homologous to FLO10 was identified in the industrial flocculating yeast SPSC01. Sequence analysis indicated that the N- and C-terminus of the deduced protein of this new FLO gene are 99 % identical to that of FLO10, but more intragenic repeats are included. The study on the function of FLO10 (spsc) by its integrative expression in the non-flocculating industrial yeast indicated severe inhibition in the flocculation of the transformant by mannose and maltose, moderate inhibition by sucrose and glucose and no inhibition by xylose and galactose, and thus the NewFlo type was established. Meanwhile, the flocculation of the transformant was stable when the temperature was below 50 °C and the pH was in the range of 4.0-6.0. Furthermore, the medium containing 250 g/l glucose was completely fermented within 48 h by the transformant, with about 110 g/l ethanol and 5.5 g(DCW)/l biomass produced, and no significant difference in ethanol fermentation performance was observed compared to its wide-type strain. Therefore, the FLO gene and corresponding transformation strategy provide a platform for engineering yeast strains with the flocculation phenotype to facilitate biomass recovery.     

产微生物絮凝剂的菌株筛选、鉴定及发酵条件优化

微生物絮凝剂是一类新型的水处理制剂,因其具有高效、无毒、易降解等特点,已成为水处理剂开发的研究热点。为了扩大微生物絮凝剂的种类,本研究从活性污泥和土壤样品中筛选絮凝剂产生菌,最终获得一株具有絮凝活性的菌株,通过16S rDNA鉴定,该菌株为蒙氏假单胞菌(Pseudomonas monteilii),因此命名为P. monteilii YR-1。利用单因素实验和正交试验对该菌株的发酵条件进行了优化,其最佳碳、氮源分别为25 g/L葡萄糖和2 g/L复合氮源(酵母浸粉:尿素:硫酸铵=5:5:2),培养基初始pH值为10,培养温度为28℃,发酵时间为72 h。在最佳培养条件下,其发酵液的絮凝率从37.68%提高到63.52%。这是关于蒙氏假单胞菌产絮凝剂的首次报道。     

Recovery of alkaline proteases by membrane filtration

This work describes the recovery of an extracellular alkaline protease from fermentation broths of a Bacillus sp ATCC 21536, at pH=10.0 using ultrafiltration (MWCO 100,000) and microfiltration (0.1 m) membranes in hollow fiber devices. The influence of membrane pore size and polymeric material and membrane filtration performance was studied. High protein recoveries and high average flux rates were obtained with polysulfone membranes. A decrease of concentration polarization was obtained, simultaneously with enhancement of filtration flux rate and enzyme recovery by using submicron sized charged particles. These polymers lead to flocculation and adsorption of whole cells and soluble factors from the fermentation broth. The best results were obtaiend by combination of cationic (0.1%) and anionic (0.04%) polymers.     

New concepts for rapid yeast settling. II. pH switching with an inert powder

A new technique is outlined for the rapid settling of yeast cells in fermentation media. The technique involved the addition of dense, inert particles (nickel powder) to a yeast suspension (Saccharomyces cerevisiae) at pH 4.5 and a rapid change of pH to 8.0-9.0. When the pH was changed large flocs formed immediately and settled rapidly, leaving a clear supernatant. On returning the pH to 4.5 the flocs were destroyed. This technique gave larger flocs and higher settling rates than the constant pH method, and much lower nickel/yeast ratios were required. Good flocculation also occurred in a fermentation medium. The technique was used to recycle yeast cells to a semicontinuous ethanol fermentation. Application of the technique to this and similar systems is discussed. The factors affecting yeast/inert powder flocculation are also discussed and a model is proposed to explain the observed experimental behavior for flocculation with a rapid change in pH.     

Effect of the aeration and agitation states on tetracycline biosynthesis in semiproduction-capacity apparatus]

The results of the experiments on determination of the effect of aeration and agitation conditions on biosynthesis of tetracycline in the apparatus of semi-production capacity are discussed. It was shown that the antibiotic production level was not connected with the rate of oxygen solution expressed in the sulphite numbers, i.e. this parameter cannot be used as a scaling-up criterion. Accumulation of the antibiotic in the fermentation broth depended on the volume of the air supplied for aeration. It was determined that the level of CO2 dissolved in the fermentation broth did not reach the values having an inhibitory effect on the biosynthetic process.     

Use of a polarographic method for determining trichothecin]

The polarographic behaviour of trichothecin was studied. It was shown that the antibiotic could be detected in solutions at concentrations of 7.10(-7) moles with the help of the polarographic method. Conditions for the polarographic determination of trichothecin in fermentation broth were developed. The error was not more than 3 per cent. The reliability of the results was shown by statistical treatment of data performed in accordance with the requirement of the USSR State Pharmacopeia, X ed., prescribing that the precision of the assay is such that the fiducial limits at p = 95 per cent deviate from the average value by not more than 5 per cent. Comparison of the results of trichothecin determination in the fermentation broth with the polarographic and biological methods showed no significant difference. Therefore, the polarographic method may be recommended for trichothecin determination in the fermentation broth.     

细脚拟青霉代谢产物清除自由基和抑制单胺氧化酶活性的研究

用二苯代苦味肼基自由基(DPPH)-TLC法和酶标仪法对一株细脚拟青霉RCEF0394发酵液甲醇提取物的清除自由基活性进行了定性和定量测定,发现该提取物具有较强的清除自由基活性,在浓度为5.0mg/mL,于37℃下保温10min时,它对0.4mg/mL的DPPH自由基的清除率可达75.4%。以大鼠肝脏线粒体单胺氧化酶为靶标的体外实验发现供试细脚拟青霉发酵液有较强的抑制单胺氧化酶活性,且其活性和浓度呈量效关系。该发酵液冻干品对单胺氧化酶的半数抑制浓度IC50为118.1μg/mL。其三氯甲烷提取物对单胺氧化酶的抑制活性明显强于发酵液冻干品,表明该抑制剂可能为极性较低的化合物。进一步的分型试验表明该三氯甲烷提取物对A型单胺氧化酶呈混合抑制,对B型呈竞争性抑制,其Km值分别为0.44mg/L,0.34mg/L。     

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 %.     

Purification during crossflow electromicrofiltration of fermentation broth

The present study was to investigate the purification of a fermentation broth by an electromicrofiltration membrane. Microfiltration runs with a crude and a centrifuged broth, with solution of particles recovered from centrifugation and with permeates from microfiltration experiments were thus compared.Microfiltration performances were governed by colloids and small particles that induced sharp initial flux declines. For these results, the evolution of the overall membrane resistance was increased by 80% in comparison with the electromicrofiltration membrane. The main focus of this study was set on the enhancement of the filtrate flux by an electric field. This pressure electrofiltration leads to a drastic improvement of the filtration by 100% and the filtration time was thereby reduced. Pressure electrofiltration serves as an interesting alternative to the cross-flow filtration and it effectively separates advantageous constituents such as amino acids and biopolymers from a fermentation broth. They were equally maintained during the microelectrofiltration, although they were significantly reduced by 45% by the microfiltration without the application of an electric field. Accordingly, since the electrofiltration membrane was provided more permeability, this study experimentally demonstrates that the permeability inside a membrane can be controlled using an electric field.