Diacetyl production by co-immobilized citrate-positiveLactococcus lactis subsp.lactis 3022 and homogenized bovin liver in alginate fibers with double gel layers

Summary Diacetyl production by (Citr⁺)Lactococcus lactis subsp.lactis 3022 cells immobilized in Ca-alginate fine fibers with single layer in the presence of catalase was three times higher than that in the absence of catalase. A co-immobilized culture system of the lactic acid bacterial cells (outer) and the homogenized bovine liver (inner layer) in Ca-alginate fibers with double gel layers was developed. The culture system gave high diacetyl productivity (30 mg/l) for ten repeated batch cultures.     

Resistance of bacterial film to contamination during use as inoculum in repeated batch fermentation

Summary AnEscherichia coli strain constitutive for -galactosidase was immobilized onto cotton cloth. The resultingE.coli film was used as a resident inoculum in repeated batch fermentations for 30 days in the presence ofBrevibacterium ammoniagenes added as a contaminant. Analysis of -galactosidase production shows that contamination did not decrease the capacity of the film to generateE.coli cells, or decrease theE.coli population on the film.     

Enhancement of γ-linolenic acid production by Mucor ambiguus with nonionic surfactants

Summary -Linolenic acid (GLA) production by Mucor ambiguus IFO 6742, immobilised in Biomass Support Particles (BSPs), has been investigated in a fluidized-bed fermenter in the presence of nonionic surfactants. In this system, repeated batch cultivation was achieved at higher yield and productivity than by conventional methods, since microbial lipids inlcuding GLA were significantly secreted into the culture broth and/or on the surface of the cell wall.     

Stabilization of cetyltrimethylammonium bromide permeabilized yeast whole cell lactase

Summary Cetyltrimethylammonium bromide-permeabilized cells ofK. fragilis loose -galactosidase activity due to leaking of the enzyme into the medium. This leakage of the enzyme can be prevented by storing the permeabilized cells either in buffer containing 50% glycerol or by treating the permeabilized cells with 0.2% glutaraldehyde at 4°C for 10 min. In repeated batch hydrolysis of lactose in milk, glutaraldehyde treated cells could be repeatedly used very efficiently.     

Continuous culture of a recombinantEscherichia coli and plasmid maintenance for tryptophan production

Summary Production of tryptophan by a temperature sensitive recombinant microorganism (Escherichia coli W3110 trpLDtrpR ^ts tna ^– (pCRT185)) was investigated. In a single-stage continous culture, at an elevated temperature, 42°C (derepressed condition), tryptophan concentration increased in an early phase of the fermentation, and then gradually decreased with time. The reduction in the production rate was mostly due to the segregation of the plasmid and subsequent increase of plasmid-free cells. However, the plasmid could be maintained stable at 37°C, with repressed condition oftrp-operon, over 200 generations. A two-stage continuous culture system, i.e. cell growth was maintained in the first stage at 37°C and gene expression was induced in the second stage at 42°C, was therefore tested to improve the performance of the fermentation system. Operation of the two-stage system showed that the plasmid stability was significantly improved, and the specific rate of tryptophan production was maintained almost constant for more than 500 hours in the second stage.     

Continuous culture of CHO-K1 cells producing thrombomodulin and estimation of culture conditions

Recombinant Chinese hamster ovary (CHO-K1) cells expressing human soluble thrombomodulin (rsTM) were cultured in a continuous culture system with a fluidized-bed reactor. Cells were grown in a medium containing 1% serum for 10 d, and then cultured in a serum-free medium. The protein production rate increased remarkably in the serum-free culture, with a decrease in the lactate production rate. This suggests that CHO-K1 cells exhibit different physiological characteristics in response to serum removal from the medium, which resulted in a higher rsTM concentration (about 60 mg/l). A procedure for estimating protein productivity was developed using experimental glucose and lactate measurements. In this procedure, cell density was estimated from the glucose consumption rate, and the specific protein (rsTM) production rate was obtained from the ratio of lactate production/glucose consumption (ΔL/ΔG). Since the cell density and protein productivity in repeated batch culture were well estimated, the procedure was applied to continuous culture in a fluidized-bed bioreactor culture. The estimation procedure was also found to be effective in this continuous culture using the models derived from the repeated batch culture.     

Production of recombinant h-AT III with mammalian cell cultures using capillary electrophoresis for product monitoring

The importance of mammalian cell cultures for biotechnological production processes is steadily increasing, despite the high demands of these organisms on their culture conditions. Efforts towards a more efficient bioprocess generally concentrate on maximizing the culture's life time, the cell number, and the product concentration. Here recombinant BHK 21 c13 cells are used to produce rh-AT III, an anticoagulant of high therapeutic value. The influence of the process mode (batch, repeated batch, continuous perfusion) and the process temperature (30°C vs. 37°C) on the above mentioned parameters is investigated. It is possible to increase the length of the culture from 140 h (batch) to more than 500 h (continuous perfusion culture), while concomitantly increasing the cell density from 0.72 10⁶/ml (batch) to 2.27 10⁶/ml (repeated batch) and 2.87 10⁶/ml (continuous perfusion culture). The accumulation of toxic metabolites, such as lactate, can be curtailed by reducing the bioreactor temperature from 37°C to 30°C during the later part of the exponential growth phase. Fast and reliable product monitoring became essential during process optimization. Capillary zone electrophoresis (CZE) in uncoated fused silica capillaries was studied for that purpose and compared to the standard ELISA. Under optimized conditions an AT III quantification could be done within 2 min with CZE. The detection limit was 5 g/ml. A relative standard deviation of less than 0.9% was calculated. The detection limit could be lowered by one order of magnitude by using a two dimensional system, where an liquid chromatographic (LC) system is coupled to the CZE. Concomitantly the resolution is improved. The two-dimensional analysis required 5 min. Membrane adsorbers (MA) were used as stationary phase in the LC-system, to allow the application of high flow rates (5–10 ml/min). The correlation between the LC-CZE analysis and the standard AT III-ELISA was excellent, with r²: 0.965. Using the assay for at line product monitoring, it is shown, that the process temperature is of no consequence for the productivity whereas the process mode strongly influences this parameter.     

Enhanced isopropanol and <Emphasis Type="Italic">n</Emphasis>-butanol production by supplying exogenous acetic acid via co-culturing two clostridium strains from cassava bagasse hydrolysate

The focus of this study was to produce isopropanol and butanol (IB) from dilute sulfuric acid treated cassava bagasse hydrolysate (SACBH), and improve IB production by co-culturing Clostridium beijerinckii (C. beijerinckii) with Clostridium tyrobutyricum (C. tyrobutyricum) in an immobilized-cell fermentation system. Concentrated SACBH could be converted to solvents efficiently by immobilized pure culture of C. beijerinckii. Considerable solvent concentrations of 6.19 g/L isopropanol and 12.32 g/L butanol were obtained from batch fermentation, and the total solvent yield and volumetric productivity were 0.42 g/g and 0.30 g/L/h, respectively. Furthermore, the concentrations of isopropanol and butanol increased to 7.63 and 13.26 g/L, respectively, under the immobilized co-culture conditions when concentrated SACBH was used as the carbon source. The concentrations of isopropanol and butanol from the immobilized co-culture fermentation were, respectively, 42.62 and 25.45 % higher than the production resulting from pure culture fermentation. The total solvent yield and volumetric productivity increased to 0.51 g/g and 0.44 g/L/h when co-culture conditions were utilized. Our results indicated that SACBH could be used as an economically favorable carbon source or substrate for IB production using immobilized fermentation. Additionally, IB production could be significantly improved by co-culture immobilization, which provides extracellular acetic acid to C. beijerinckii from C. tyrobutyricum. This study provided a technically feasible and cost-efficient way for IB production using cassava bagasse, which may be suitable for industrial solvent production.     

The D-xylose fermenting capacities of immobilizedPichia stipitis andPachysolen tannophilus

Summary The yeastsP. stipitis NRRL Y-7124 andP. tannophilus NRRL Y-2460 were entrapped in -carrageenan beads and used for repeated batch fermentation of D-xylose, in a series of four reactors. The operating conditions finally chosen gave an oxygen coefficient (K_La) of 0.83 min^–1, as measured by the sulphite method. Ethanol yields were 0.40 g/g forP. stipitis and 0.36 g/g forP. tannophilus (respectively 78.4% and 70.5% of the theoretical yields). In spite of its lower retention by the gel,P. stipitis exhibited greater fermenting capacities thanP. tannophilus.     

Regulated production of recombinant echistatin by yeast

Summary The -mating factor pre-pro-leader sequence under the regulation of theGAL10 promoter was used to direct the secretion of echistatin by recombinant yeasts. Optimization of the culture medium and host strain increased the productivity of shake flask cultures twenty-fold to 8 mg/L. In fermentors, the production of echistatin was greater than 40 mg/L.     

Production of biosurfactants by the resting cells ofPseudomonas aeruginosa CFTR-6

A resting cell system was used for the production of glycolipids byPseudomonas aeruginosa CFTR-6. In this, the growth phase was separated from the production phase to overcome the inhibition of glycolipid production by inorganic phosphate. It was shown that when the cells were transferred after the growth phase into a medium devoid of phosphate, glycolipid production was increased nearly twofold. The maximum glycolipid concentration was attained much more rapidly than the conventional batch fermentation system, thus increasing the productivity.     

Production of Acinetobacter radioresistens lipase with repeated batch culture in presence of nonwoven fabric.

Cultivation of Acinetobacter radioresistens on n-hexadecane for lipase production was investigated with repeated batch culture in the presence of a hydrophobic nonwoven fabric. Lipase production followed the growth-associated model, and the repeated batch culture could achieve both high enzyme yield and increased volumetric productivity. The fabric was shown to be able to disperse n-hexadecane, to adsorb the unused hydrocarbon, and to retain bioemulsifiers excreted from the cells; therefore, it enhanced cell growth and, in turn, lipase production. In the repeated batch culture in the absence of the fabric, lipase yield and volumetric productivity were found to be 21 U/mL and 875 U/L. h, respectively. However, if the fabric was equipped in the fermentor, lipase yield and volumetric productivity increased to 30 U/mL and 2500 U/L. h, respectively. The lipase production profile could be further improved by raising the amount of nitrogen source and, as a result, a lipase yield of 54 U/mL and a volumetric productivity of 2250 U/L. h were obtained. In this study we assess the beneficial effects of nonwoven fabric on lipase production.     

Effect of operational conditions on the rate of citric acid production by rotating disk contactor using Aspergillus niger

The effect of operational conditions such as the specific biofilm area, oxygen concentration, and rotation speed on citric acid production by a rotating disk contactor (RDC) was examined. The overall productivity for a repeated batch culture was also compared with that for a non-repeated batch culture. The citric acid production rate per unit biofilm area (P) was almost constant regardless of the value of the specific film area. The rotation speed of the disks had no effect on P in the range of 5–20 rpm. The apparent saturation constant of dissolved oxygen concentration was 2.05 mg/l. Overall citric acid productivity for a 3-times-repeated batch culture was 1.7 times higher than that for the non-repeated batch culture.     

Biobutanol production in a Clostridium acetobutylicum biofilm reactor integrated with simultaneous product recovery by adsorption

Background

Clostridium acetobutylicum can propagate on fibrous matrices and form biofilms that have improved butanol tolerance and a high fermentation rate and can be repeatedly used. Previously, a novel macroporous resin, KA-I, was synthesized in our laboratory and was demonstrated to be a good adsorbent with high selectivity and capacity for butanol recovery from a model solution. Based on these results, we aimed to develop a process integrating a biofilm reactor with simultaneous product recovery using the KA-I resin to maximize the production efficiency of biobutanol.

Results

KA-I showed great affinity for butanol and butyrate and could selectively enhance acetoin production at the expense of acetone during the fermentation. The biofilm reactor exhibited high productivity with considerably low broth turbidity during repeated batch fermentations. By maintaining the butanol level above 6.5 g/L in the biofilm reactor, butyrate adsorption by the KA-I resin was effectively reduced. Co-adsorption of acetone by the resin improved the fermentation performance. By redox modulation with methyl viologen (MV), the butanol-acetone ratio and the total product yield increased. An equivalent solvent titer of 96.5 to 130.7 g/L was achieved with a productivity of 1.0 to 1.5 g?·?L^-1?·?h^-1. The solvent concentration and productivity increased by 4 to 6-fold and 3 to 5-fold, respectively, compared to traditional batch fermentation using planktonic culture.

Conclusions

Compared to the conventional process, the integrated process dramatically improved the productivity and reduced the energy consumption as well as water usage in biobutanol production. While genetic engineering focuses on strain improvement to enhance butanol production, process development can fully exploit the productivity of a strain and maximize the production efficiency.     

Berberine production by batch and semi-continuous cultures of immobilized Thalictrum cells in an improved bioreactor

A new bioreactor (liquid-gas two-phase system) was devised for berberine-secreting Thalictrum minus cells immobilized in calcium alginate beads, which were alternately soaked in medium, and exposed to air. The highest yield of berberine (875 mg/l) was obtained by setting the cycle of medium supply and air supply for 30 seconds and 2 minutes, respectively, during a culture period of 30 days. Under such conditions of batch culture, the berberine productivity of immobilized cells was as high as that of freely suspended cells. Furthermore, the rate of berberine production by immobilized cells remained constant at a high value (50 mg/l/day) for a period of 60 days of semi-continuous culture achieved by renewal of medium at intervals of 10 days.     

α-Amylase production in batch and continuous cultures by Bacillus caldolyticus

Summary The concentration and productivity of -amylase increased remarkably, 15- and 11-fold respectively, in a continuous culture of Bacillus caldolyticus DSM 405 compared with batch culture, provided starch was used as the sugar source in a casitone medium. In the casitone medium with or without glucose hardly any improvement of enzyme production was observed in continuous culture. The addition of a small amount of starch to the glucose-casitone medium had a marked effect in stimulating amylase formation in continuous culture but no effect in batch culture.It was suggested that the higher production of -amylase in the continuous culture using starch as the inducer was partly related to the predominance of some conditional non-sporulating variants with a higher amylase forming activity and to derepression of the enzyme at a low glucose concentration.     

Production of l-glutamate by immobilized protoplasts

Summary Protoplasts of Brevibacterium flavum cultured in a medium containing 50 g·l^-1 of biotin were prepared with lysozyme and immobilized in matrices of agar-acetylcellulose filters. The immobilized protoplasts were applied to l-glutamate production from glucose and urea in a batch system. The productivity of l-glutamate by the immobilized protoplasts was 2.5 times higher than that by immobilized whole cells under optimal conditions. Maximal productivity initially reached 1.5 mg·ml^-1. The immobilized protoplasts of B. flavum could be used six times for l-glutamate production with retention of about 70% of the initial productivity.     

Anther culture of some perennial triticeae

Three field grown Agropyron spp. (crested wheatgrasses) and two Thinopyrum spp. (intermediate and tall wheatgrasses) were evaluated for anther culture response. Hormonally modified potato extract and 85D12 media induced pollen embryogenesis. Modified Murashige and Skoog media were tested for their effects on callus proliferation and plantlet regeneration. Callus induction frequency and plantlet production were highest (25.0% and 45.8%, respectively) for Thinopyrum ponticum (2N=70) (tall wheatgrass). One-hundred and nine albino plantlets were produced from T. ponticum Jose both by direct regeneration on 85D12 medium and through a callus phase from potato extract media. This is the first report of plantlet production from anther culture of a Triticeae perennial forage grass. Further experimentation with environmental and cultural conditions may result in the production of green plantlets.Abbreviations MS Murashige and Skoog (1962) medium - NAA naphthaleneacetic acid - 2,4-D 2,4-dichlorophenoxyacetic acid - 2-ip 2-isopentenyladenosine - 2,4,5-T 2,4,5-trichlorophenoxyacetic acid Cooperative investigations of the USDA-Agricultural Experiment Station and the Utah Agricultural Experiment Station, Logan, UT 84322. Approved as Journal Paper No. 3596     

Stability of plasmid PBR322 in Escherichia coli immobilized on cotton cloth during use as resident inoculum

Summary E. coli cells harbouring plasmid pBR322 which confers ampicillin resistance were immobilized on cotton cloth. The resulting film was used as an inoculum in daily repeated batch culture in ampicillin-free medium. During two months, the film was able to produce cultures which, at the late log phase, showed little sensitivity to 10 mg/ml ampicillin. Thus such a bacterial film can effectively be used as an inoculum for the production of recombinant DNA products by means of pBR322 or its derivatives in the absence of ampicillin.     

Isolation and immobilization ofSclerotium rolfsii protoplasts

Summary Protoplasts fromSclerotium rolfsii were prepared usingTrichoderma harzianum lytic enzymes and immobilized in Ca alginate gels. The immobilized protoplasts when incubated with 1% carboxymethylcellulose in osmotically stabilized induction medium, could secrete endoglucanase and -glucosidase. On repeated use the immobilized preparation retained 36% endoglucanase and 26% -glucosidase activity after 5 cycles.NCL Communication No. 3798