The effect of chemical treatment of stainless steel wire surfaces on Zymomonas mobilis cell attachment and product synthesis

The attachment, growth and product synthesis of non-flocculating Zymomonas mobilis cell, fixed in stainless steel wire spheres (WS), were investigated. The carrier surface was activated by treatment with titanium (IV) chloride (TiCl₄) and γ-aminopropyltriethoxysilane (AS) in an attempt to raise the efficiency in the immobilization of the cells. System productivity for ethanol and levan production, using cells immobilized on a modified stainless steel in the batch fermentation of a sucrose medium, rose as a result of increased biomass compared to the productivity of cells fixed on untreated (control) metal surfaces. Stabilized ethanol synthesis was demonstrated in the course of four cycles (each cycle 48 h) of repeated fermentations with a stainless steel carrier treated with AS, and three cycles when TiCl₄ was used. Levan synthesis decreased after three cycles with cells immobilized on a silanized surface. System productivity for ethanol and levan production after the fourth cycle in experiments with TiCl₄-activated, silanized and unmodified carriers were Q_eth = 1.01, 1.06 and 0.27 g/l × h; Q_lev = 0.32, 0.29 and 0.12 g/l × h, respectively. However, the specific productivity of biomass for product synthesis was higher in fermentation systems with untreated stainless steel surfaces, probably due to some loss of physiological activity of cells attached to a modified carrier. Investigations of throughly washed activated stainless steel wire surfaces, by scanning electron microscopy after immobilization, showed significant attachment of cells to the carriers. A polymer layer covered the wire surface treated with TiCl₄ after fermentations. This may be explained as the binding of extracellular polysaccharide, such as the fructose-polymer levan and yeast extract components, to the modified support via chelation. After four fermentations, craters and holes in the polymer layer were evident, probably as a result of CO₂ formation. A small number of cells appeared on this layer. In view of the good ethanol formation during all fermentation cycles, it is probably that active Z. mobilis cells remained under the polymer layer. Wire treatment with AS resulted in the formation of long filamentous cells during fermentation and some disturbance of cellular fission. This may be partly explained by strong electrostatic interactions between the positively charged carrier surface and the predominately negatively charged surface of Z mobilis cells. However, this did not significantly affect other cellular functions. The surface of the wire treated with AG was practically without a polymer layer.     

Lactate production in an integrated process configuration: reducing cell adsorption by shielding of adsorbent

The problem of binding of microbial cells to an adsorbent matrix during in situ recovery of bioproducts from a fermentation broth has been addressed by shielding the adsorbent with a thin layer of a non-ionic polymer. Extractive bioconversion of lactic acid by integrating ion-exchange adsorption with the fermentation stage was studied. The effect of coating of the ion-exchanger with agarose on product recovery and cell adsorption was evaluated. Extractive fermentation with both uncoated and coated resin resulted in an increase in reactor productivity as compared to the normal fermentation. The free cell density in the system with agarose-coated beads was similar to that in control fermentation, but was significantly lower in the system with the uncoated ion-exchanger. Electron microscopic scanning of the bead surface after passage of the fermentation broth showed cells attached to the native adsorbent but not to the coated one.     

Extraction of polyhydroxyalkanoate from Sinorhizobium meliloti cells using Microbispora sp. culture and its enzymes

Sinorhizobium meliloti produced 50% polyhydroxyalkanoate (PHA) in the biomass in the presence of sucrose as carbon substrate. Isolation of the intracellular PHA was achieved through a secondary fermentation involving a cell lytic actinomycetes species namely Microbispora sp. without further supplementation of nutrients to the S. meliloti fermented broth, at 30 °C, 150 rpm up to 72 h. Microbispora sp. cells that showed pelleted growth was removed by filtration and the released polymer contained in the filtrate was extracted by chloroform or an admixture of Triton X 100 (0.6%) a surfactant and ethylene diamine tetra acetic acid (EDTA) a chelating agent. Yield of PHA obtained was 49, 41 and 7% of biomass weight after 24, 48 and 72 h of lytic culture fermentation, respectively. Corresponding recovery of the polymer was 94, 82 and 15% of 90% purity. Alternatively Microbispora sp. lytic enzyme was obtained by its cultivation in nutrient broth with S. meliloti cells as substrate and the supernatant was used for the hydrolysis of the PHA containing biomass to release PHA. A620 lytic activity value for the broth was 200 at 72 h. The enzyme showed optimized activity at 50 °C, pH 7 and this was used to hydrolyze 5 g/l of thermally inactivated biomass of S. meliloti to recover 94% of total PHA present in the cells and the polymer produced was 92% pure. Decreased cell lytic activity in the presence of soluble protein added in the form of bovine serum albumin indicated that the hydrolytic activity may be due to proteases. The polymer was characterized by GC, NMR and DSC and was found to be polyhydroxybutyrate-co-hydroxyvalerate (97:3 mol%) with a melt temperature of 169 °C.     

Mechanisms for biopolymer accumulation in immobilized Acinetobacter calcoaceticus system

The gram-positive bacteria, Acinetobacter calcoaceticus, is capable of accumulating biopolymer in the carrier matrix of an immobilized cell system. Several possible mechanisms for the biopolymer accumulation are evaluated. It appears that direct solid surface polymer adsorption and polymer diffusion limitation within the pore space are minor factors in biopolymer accumulation. Calculations demonstrate that the cell bound polymer to dry cell weight ratio is much higher for immobilized cells than for free cells. The higher cell-bound polymer to dry-cell-weight ratio for immobilized cells as well as the accumulation of the immobilized cells in the Celite matrix are believed to be the main factors for biopolymer accumulation in the Carrier matrix. Further studies reveal that the cell-bound polymer to dry-cell-weight ratio is strongly affected by shear forces. At zero shear stress, such as would be present in the carrier matrix, cell bound polymer to dry cell weight ratio can be as high as 1.6. As the shear stress increases, this ratio decreases. When shear stress increases above 5 dyn/cm(2), a level equivalent to the shear experienced by free cells in a stirred tank fermentation, cell-bound polymer decreases to less than 20% of dry cell weight. A macroscopic model is developed to describe the effect of shear stress on the cell-bound polymer to dry-cell-weight ratio.     

Hydrocarbon assimilation by Candida lipolytica: Formation of a biosurfactant; Effects on respiratory activity and growth

Summary Candida lipolytica is shown to produce an extracellular polymer with emulsifying properties when grown on n-tetradecane or a mixture of linear hydrocarbons. A device for biosurfactant isolation is presented. The polymers recovered from the fermentation broth were found to be complex molecules with a protein, a lipid and a carbohydrate moiety. Their surface active properties suggest a possible role in hydrocarbon uptake by cells. Effectively, the addition of crude polymer resulted in an enhancement of respiration rate which was dependent on n-alkane concentration with glucose grown cells. Likewise in batch culture, maximum growth rate, cell productivity and yield were increased by the presence of the biosurfactant.     

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.     

Enhanced production of lactic acid through the use of a novel aqueous two-phase system as an extractive fermentation system

 In order to enhance the productivity of lactic acid and reduce the end-product inhibition of fermentation, the partitioning and growth of four different strains of lactic acid bacteria in three different aqueous two-phase systems were studied. Polyethyleneglycol/ dextran, polyethyleneglycol/hydroxypropyl starch polymer (HPS), and a random copolymer of ethylene oxide and propylene oxide (EO-PO)/HPS were used as polymer systems. One strain each of Lactococcus lactis subsp. lactis and of Lactobacillus delbrueckii subsp. delbrueckii partitioned completely to the interface and bottom phase in two-phase systems with low polymer concentrations of EO-PO/HPS100 and EO-PO/ HPS200. The growth and production of lactic acid by two of three L. lactis strains in a two-phase system with 5.5% (w/w) EO-PO and 12.0% (w/w) HPS100 were reduced by less than 10% compared with a reference fermentation in a normal growth medium. The viability of L. lactis subsp. lactis ATCC 19435 was maintained for at least 50 h and with four top-phase replacements during extractive fermentation in the EO-PO/HPS100 system. Moreover, when cell density reached the stationary phase in the first extractive fermentation, the lactate production in this aqueous two-phase system was maintained. Received: 2 October 1995/Received revision: 16 January 1996/Accepted: 22 January 1996     

In situ biobutanol recovery from clostridial fermentations: a critical review

Butanol is a precursor of many industrial chemicals, and a fuel that is more energetic, safer and easier to handle than ethanol. Fermentative biobutanol can be produced using renewable carbon sources such as agro-industrial residues and lignocellulosic biomass. Solventogenic clostridia are known as the most preeminent biobutanol producers. However, until now, solvent production through the fermentative routes is still not economically competitive compared to the petrochemical approaches, because the butanol is toxic to their own producer bacteria, and thus, the production capability is limited by the butanol tolerance of producing cells. In order to relieve butanol toxicity to the cells and improve the butanol production, many recovery strategies (either in situ or downstream of the fermentation) have been attempted by many researchers and varied success has been achieved. In this article, we summarize in situ recovery techniques that have been applied to butanol production through Clostridium fermentation, including liquid–liquid extraction, perstraction, reactive extraction, adsorption, pervaporation, vacuum fermentation, flash fermentation and gas stripping. We offer a prospective and an opinion about the past, present and the future of these techniques, such as the application of advanced membrane technology and use of recent extractants, including polymer solutions and ionic liquids, as well as the application of these techniques to assist the in situ synthesis of butanol derivatives.     

Regulation of fructose metabolism and polymer synthesis by Fusobacterium nucleatum ATCC 10953.

Energy for the anaerobic growth of Fusobacterium nucleatum ATCC 10953 can be derived from the fermentation of sugar (fructose) or amino acid (glutamate). During growth on fructose, the cells formed large intracellular granules which after extraction yielded glucose by either acid or enzymatic hydrolysis. The endogenous polymer was subsequently metabolized, and after overnight incubation of the cells in buffer, the glucan granules were no longer detectable by electron microscopy. Anaerobically, washed cells grown previously on fructose fermented this sugar to a mixture of lactic, acetic, and butyric acids, and little intracellular glucan was formed. Aerobically, the cells slowly metabolized fructose to acetate. Provision of glutamic acid as an additional energy (ATP) source elicited rapid synthesis of polymer by glycolyzing cells. Intracellular granules were not present in glutamate-grown cells, and under anaerobic conditions, the resting cells failed to metabolize [14C] fructose. However, the addition of glutamic acid to the suspension resulted in the rapid accumulation of sugar by the cells. Approximately 15% of the 14C-labeled material was extractable with boiling water, and by 31P nuclear magnetic resonance spectroscopy, this phosphorylated derivative was identified as [14C]fructose-1-phosphate. The nonextractable material represented [14C]glucan polymer. Fructose-1-phosphate kinase activity in fructose-grown cells was fivefold greater than that in glutamate-grown cells. We suggest that the activity of fructose-1-phosphate kinase and the availability of ATP regulate the flow of fructose into either the glycolytic or polymer-synthesizing pathway in F. nucleatum.     

Extractive lactic acid fermentation in poly (ethyleneimine)-based aqueous two-phase system

The potential of an aqueous two-phase system composed of a polycation, poly(ethyleneimine) (PEI), and an uncharged polymer, (hydroxyethyl) cellulose (HEC), for extractive lactic acid fermentation was tested. Batch fermentation with 20 g/L glucose in two-phase medium using Lactococcus lactis without external pH control resulted in 3-4 times higher amount of lactate and biomass produced as compared to that in a conventional one-phase medium. Lactic acid was preferentially partitioned to the PEI-rich bottom phase. However, the cells which favored the HEC-rich top phase in a fresh two-phase medium were partitioned to a significant extent to the bottom phase after fermentation. Addition of phosphate buffer or pH adjustment to 6.5 after fermentation caused fewer cells to move to the bottom phase. With external pH control, fermentation in normal and two-phase medium showed no marked differences in glucose consumption and lactic acid yield, except that about 1.3 times higher cell density was obtained in the two-phase broth, especially at initial glucose concentrations of 50-100 g/L. Use of higher concentration of phosphate during batch fermentation in the two-phase medium with 50 g/L sugar provided a 15% higher yield of lactic acid, but the growth rate of cells was nearly half of the normal, thus affecting the productivity. Continuous fermentation with twice the normal phosphate concentration resulted in higher cell density, product yield, and productivity in two-phase medium than in monophasic medium. (c) 1996 John Wiley & Sons, Inc.     

Recovery of Clostridium thermosulfurogenes produced beta-amylase by (hydroxypropyl)methylcellulose partition.

A procedure for recovering Clostridium thermosulfurogenes produced beta-amylase from fermentation broth by partition was developed. The partition was achieved by addition of ammonium sulfate to an aqueous solution of the enzyme with (hydroxypropyl)methylcellulose. The beta-amylase-containing pellet formed upon centrifugation could be redissolved and the polymer recovered by a second salt addition. The process was not dependent on polymer/enzyme solution pH, but it was affected by temperature, polymer nominal molecular weight and loading, and fermentation carbon source. Unlike more traditional aqueous-phase partitions, such as poly(ethylene glycol)/dextran, the current approach appeared to be biospecific.     

Fermentative Production of Exocellular Glucans by Fleshy Fungi

Two specimens of higher fungi produced exocellular β-1, 3-glucans when their mycelial forms were cultivated under submerged aerobic conditions. Plectania occidentalis NRRL 3137 consumed up to 6% glucose or xylose with about 30% conversion to polymer in a medium composed of hydrolyzed soy protein, salts, and thiamine. A 5% inoculum was used in a 10-day shaken fermentation. After dilution of the culture liquors and partial disruption of mycelia with a blender, solids were removed by centrifugation, and the polymer was precipitated by the admixture of 2 volumes of ethyl alcohol. A second polymer was formed in 40 to 65% yield by fermentation with Helotium sp. NRRL 3129, which in the imperfect stage would be identified as Monilia sp. It consumed up to 4% glucose, fructose, mannose, or sucrose in 60 to 72 hr. A 2% inoculum in a medium composed of commercial defatted soy flakes, phosphate, and thiamine in tap water gave a satisfactory fermentation. This polymer was precipitated by the addition of 0.5 volume of ethyl alcohol. Both organisms have a broad pH optimum on the slightly acidic side and did best at about 25 C.     

Production of PHB and P (3HB-co-3HV) biopolymers by <Emphasis Type="Italic">Bacillus megaterium</Emphasis> strain OU303A isolated from municipal sewage sludge

Bacillus megaterium strain OU303A isolated from municipal sewage sludge was selected for the study of biosynthesis of polyhydroxybutyrate (PHB) and polyhydroxybutyrate-co-hydroxyvalerate P (HB-co-HV) copolymer. The strain yielded a maximum of 62.43% DCW polymer in the medium containing glycerol as carbon source, which was followed by 58.63% DCW polymer in glucose containing medium. We found that this strain was capable of producing 2.5% hydroxyvalerate copolymer from a single carbon substrate, glucose. The strain showed an increase in the amount of HV monomer content, when the precursor for the copolymer was included in the fermentation medium. The characterization of the biopolymers was carried out using FTIR, GC-MS, H¹ NMR and DSC. This is the first report of B. megaterium strain producing HV copolymer, without the addition of any precursor in the fermentation medium.     

Production of bacterial exopolysaccharides by solid substrate fermentation

In a comparison of submerged cultivation (SC) with solid substrate fermentation (SSF) for the production of bacterial exopolysaccharides (EPS), the latter technique yielded 2 to 4.7 times more polymer than the former, on the laboratory scale. SSF was performed using inert solid particles (spent malt grains) impregnated with a liquid medium. The polymer yields obtained from SSFs, as referred to the impregnating liquid volumes, were as follows: 38.8 g/litre xanthan from Xanthomonas campestris, 21.8 g/litre succinoglycan from Rhizobium hedysari and 20.3 g/litre succinoglycan from Agrobacterium tumefaciens PT45. These results make this technique promising for a potential application on the industrial scale. A further advantage with this fermentation process is found in the availability and low cost of substrates, which are obtained as by-products or wastes from the agriculture or food industry.     

Fed-batch production and simple isolation of succinoglycan from Agrobacterium tumefaciens

Succinoglycan production by Agrobacterium tumefaciens was increased from 9.5 g/l to 14 g/l when the microorganism was cultivated under fed-batch condition, as compared to batch fermentation. Cells and broth impurities were removed from the fermentation broth with activated charcoal at a temperature of 90°C, yielding a clear and odorless solution of the polymer. Viscosity mesurement, NMR spectroscopy and Mw determination proved that the polymer retains its main features, practically unaffected by the heat treatment.     

Cloning and expression of the PHA synthase genes phaC1 and phaC1AB into Bacillus subtilis

Summary Polyhydroxyalkanoates (PHAs) are polyesters of hydroxyalkanoates synthesized by numerous bacteria as intracellular carbon and energy storage compounds and accumulated as granules in the cytoplasm of cells. In this work, we constructed two recombinant plasmids, pBE2C1 and pBE2C1AB. The two plasmids were inserted into Bacillus subtilis DB104 and generated Bacillus subtilis/pBE2C1 and Bacillus subtilis/pBE2C1AB. The two recombinant strains were subjected to fermentation and showed PHA accumulation, the first reported example of medium-chain-length-PHA production in Bacillus subtilis. GC analysis identified the compound produced by Bacillus subtilis/pBE2C1 was a hydroxydecanoate-co-hydroxydodecanoate (HD-co-HDD) polymer while that produced by Bacillus subtilis/pBE2C1AB was a hydroxybutyrate-co-hydroxydecanoate-co-hydroxydodecanoate (HB-HD-HDD) polymer. The results also showed that the recombinant B. subtilis could utilize the malt waste in the medium as a carbon source better than that of glucose and thus could substantially lower the cost of production of PHA.     

Comparative analysis of PHAs production by Bacillus megaterium OUAT 016 under submerged and solid-state fermentation

In view of risk coupled with synthetic polymer waste, there is an imperative need to explore biodegradable polymer. On account of that, six PHAs producing bacteria were isolated from mangrove forest and affilated to the genera Bacillus & Pseudomonas from morpho-physiological characterizations. Among which the potent PHAs producer was identified as Bacillus megaterium OUAT 016 by 16S rDNA sequencing and in-silico analysis. This research addressed a comparative account on PHAs production by submerged and solid-state fermentation pertaining to different downstream processing. Here, we established higher PHAs production by solid-state fermentation through sonication and mono-solvent extraction. Using modified MSM media under optimized conditions, 49.5% & 57.7% of PHAs were produced in submerged and 34.1% & 62.0% in solid-state fermentation process. Extracted PHAs was identified as a valuable polymer PHB-co-PHV and its crystallinity & thermostability nature was validated by FTIR, ¹H NMR and XRD. The melting (Tm) and thermal degradation temperature (Td) of PHB-co-PHV was 166 °C and 273 °C as depicted from DTA. Moreover, FE-SEM and SPM surface imaging indicated biodegradable nature, while FACS assay confirmed cytocompatibility of PHB-co-PHV.     

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.     

Immobilized <Emphasis Type="Italic">Kluyveromyces marxianus</Emphasis> cells in carboxymethyl cellulose for production of ethanol from cheese whey: experimental and kinetic studies

Cheese whey fermentation to ethanol using immobilized Kluyveromyces marxianus cells was investigated in batch and continuous operation. In batch fermentation, the yeast cells were immobilized in carboxymethyl cellulose (CMC) polymer and also synthesized graft copolymer of CMC with N-vinyl-2-pyrrolidone, denoted as CMC-g-PVP, and the efficiency of the two developed cell entrapped beads for lactose fermentation to ethanol was examined. The yeast cells immobilized in CMC-g-PVP performed slightly better than CMC with ethanol production yields of 0.52 and 0.49 g ethanol/g lactose, respectively. The effect of supplementation of cheese whey with lactose (42, 70, 100 and 150 g/l) on fermentative performance of K. marxianus immobilized in CMC beads was considered and the results were used for kinetic studies. The first order reaction model was suitable to describe the kinetics of substrate utilization and modified Gompertz model was quite successful to predict the ethanol production. For continuous ethanol fermentation, a packed-bed immobilized cell reactor (ICR) was operated at several hydraulic retention times; HRTs of 11, 15 and 30 h. At the HRT of 30 h, the ethanol production yield using CMC beads was 0.49 g/g which implies that 91.07 % of the theoretical yield was achieved.     

Significance of metal ion supplementation in the fermentation medium on the structure and anti-tumor activity of Tuber polysaccharides produced by submerged culture of Tuber melanosporum

The significance of metal ion supplementation in the fermentation medium on the structure and anti-tumor activity of Tuber polysaccharides was systematically studied in the submerged fermentation of Tuber melanosporum. The lowest weight-average molecular weight (M_w) (i.e., 115.3 × 10⁴ g/mol) of intracellular polysaccharides (IPS) was obtained when Mg²⁺ and K⁺ was added in the fermentation medium. The IPS with the lower M_w exhibited a higher inhibition ratio against S-180 tumor cells. The compact conformation of extracellular polysaccharides (EPS) was formed when only K⁺ was supplied in the fermentation medium. Interestingly, EPS with compact conformation exhibited a higher inhibition ratio (i.e., 59.2%) than EPS with branched polymer chain (i.e., 9.2%) against A549 tumor cells. The highest inhibition ratio for EPS with α-glycosidic linkages against the tumor cell line HepG2 reached 32.2% when Mg²⁺ or K⁺ was supplied in the fermentation medium. The addition of metal ion Mg²⁺, K⁺, and their combination to the fermentation medium is a vital factor affecting the structures of Tuber polysaccharides, which further determine their anti-tumor activities. The information obtained in this work will be useful for the efficient and directed production of polysaccharides with anti-tumor activities by the submerged fermentation of edible fungi mycelium.