Ethanol production by immobilized whole cells ofZymomonas mobilis in a continuous flow expanded bed bioreactor and a continuous flow stirred tank bioreactor

Continuous ethanol fermentation by immobilized whole cells ofZymomonas mobilis was investigated in an expanded bed bioreactor and in a continuous stirred tank reactor at glucose concentrations of 100, 150 and 200 g L^–1. The effect of different dilution rates on ethanol production by immobilized whole cells ofZymomonas mobilis was studied in both reactors. The maximum ethanol productivity attained was 21 g L^–1 h^–1 at a dilution rate of 0.36 h^–1 with 150 g glucose L^–1 in the continuous expanded bed bioreactor. The conversion of glucose to ethanol was independent of the glucose concentration in both reactors.     

Diol production byAeromonas hydrophila: Comparison of different immobilization techniques

Summary Techniques for immobilizing intact cells ofAeromonas hydrophila by cross-linking, attachment to an inorganic matrix, or entrapment in a polymeric gel are compared. Cells immobilized on a titanium (IV) hydroxide matrix were suitable for producing butane 2,3-diol from starch, whereas cells entrapped in polyacrylamide were a better catalyst for producing the diol from glucose.     

Preparation and properties of glucose isomerase of Streptomyces kanamyceticus cells entrapped in calcium alginate

Summary The properties of glucose isomerase in native, heat-treated and immobilized cells of Streptomyces kanamyceticus after heat and mineral treatment have been compared. The optimum pH for glucose isomerase in native cells was shifted from 8.2 to 8.6 by heat treatment and immobilization. There is no change in the optimum temperature (90°C) for activity of the enzyme by the above treatment. Heat-treated cells and immobilized cells show greater pH and thermal stability of the enzyme. The Km values of the enzyme of native cells, heat-treated cells and immobilized heat-mineral-treated cells are 208 mM, 212 mM and 166 mM respectively; Mg⁺⁺ and Co⁺⁺ enhance the activity of isomerase in all cases.     

Immobilization of baker's yeast using plaster of Paris

Summary Plaster of Paris was used as a matrix to bind radiation-killed cells ofSaccharomyces cerevisiae. Immobilized cells retained invertase activity for over 1 month of continuous operation and were about 20% more active than cells immobilized in polyacrylamide.     

Production of ethanol by adsorbed yeast cells

Summary Various ion exchange resins were tested for their ability to adsorb cells of Saccharomyces cerivisiae with the ultimate intention of developing a packed bed immobilized cell reactor for the continuous production of ethanol. The resins varied greatly in their ability to adsorb cells - the least effective resins retained less than 1 mg S. cerivisiae cells (dry weight)/g of resin (dry weight), and the most effective, 130–140 mg cells/g of resin. A column reactor packed with adsorbed yeast cells was operated continuously for over 200 hours using a 12% (w/v) glucose medium at dilution rates of 1.1 h^-1 and 1.44 h^-1 (based on void volume). High ethanol productivities of 53.1 and 62.0 g ethanol/l-h were obtained.     

Photoproduction of H2 and NADPH2 by polyurethane-immobilized cyanobacteria

Summary Cyanobacterial cells were grown in polyurethane foams (polyester or polyvinyl types). Chlorogloea fritschii, Nostoc muscorum and Mastigocladus laminosus remained immobilized in the foams and were used for continuous photoproduction of H₂ from ascorbate with methyl viologen (MV) and hydrogenase or Pt catalysts, for periods in excess of 9 days. Foam-immobilized N. muscorum continuously photoreduced exogenous NADP for at least 24 h in the presence of Fd-NADP reductase with ascorbate as electron donor.     

Could the improvements in the alcoholic fermentation of high glucose concentrations by yeast immobilization be explained by media supplementation?

Summary The maximal concentration of ethanol produced during the fermentation of 320 g/l glucose bySaccharomyces bayanus was higher when the yeast cells were immobilized either by adsorption on celite or by entrapment in k-carrageenan beads (from 10.5% with free cells up to 14.5% and 13.1% (v/v) respectively). This increase was due to medium supplementation with the compounds present in the immobilization supports.     

Simultaneous production of hydrogen and bioflocculant by Enterobacter sp. BY-29

Hydrogen and a bioflocculant could be produced simultaneously by anaerobic culture of Enterobacter sp. BY-29. For production of hydrogen and the bioflocculant by cell culture of the bacterium in batch cultures, cultivation at 37 °C in a medium containing glucose as a carbon source and Polypepton as a nitrogen source was found to be suitable. In continuous production of hydrogen and the bioflocculant by cell culture or immobilized cells of the bacterium, the hydrogen production rate and hydrogen yield by the immobilized cells on porous glass beads in stirred and column reactors were higher than those by the cell culture in a stirred reactor. However, production of the bioflocculant by the cell culture was superior to that by the immobilized cells in continuous production.     

Design of immobilized enzyme reactors for the continuous production of fructose syrup from whey permeate

Biocatalyst inactivation is inherent to continuous operation of immobilized enzyme reactors, meaning that a strategy must exist to ensure a production of uniform quality and constant throughput. Flow rate can be profiled to compensate for enzyme inactivation maintaining substrate conversion constant. Throughput can be maintained within specified margins of variation by using several reactors operating in parallel but displaced in time. Enzyme inactivation has been usually modeled under non-reactive conditions, leaving aside the effect of substrate and products on enzyme stability. Results are presented for the design of enzyme reactors under the above operational strategy, considering first-order biocatalyst inactivation kinetics modulated by substrate and products. The continuous production of hydrolyzed-isomerized whey permeate with immobilized lactase and glucose isomerase in sequential packed-bed reactors is used as a case study. Kinetic and inactivation parameters for immobilized lactase have been determined by the authors; those for glucose isomerase were taken from the literature. Except for lactose, all other substrates and products were positive modulators of enzyme stability. Reactor design was done by iteration since it depends on enzyme inactivation kinetics. Reactor performance was determined based on a preliminary design considering non-modulated first-order inactivation kinetics and confronted to such pattern. The new pattern of inactivation was then used to redesign the reactor and the process repeated until reactor performance (considering modulation) matched the assumed pattern of inactivation. Convergence was very fast and only two iterations were needed.     

Vertical Rotating Immobilized Cell Reactor of the bacteriumZymomonas mobilis for stable long-term continuous ethanol production

Summary Vertical Rotating Immobilized Cell Reactor was designed and built for glucose conversion into ethanol. Immobilized biomass units withZ. mobilis cells attached into polyurethane foam discs were fixed along a rotating shaft inside the bioreactor. The effect of rotation speed on the concentration of immobilized biomass was studied. Stability of the bioreactor over long-term operation was dependent on the concentration of the immobilized biomass. With fermentation carried out at 6 rpm a constant active immobilized cell concentration of only 34.5 g/l was maintained and used to convert up to 140 g glucose/l into more than 70 g ethanol/l with a volumetric ethanol productivity of 63 g/l/h.     

Continuous ethanol production by immobilized yeast in a fluidized reactor

Summary In order to minimize the adverse effect of CO₂ gas in a packed bed immobilized yeast reactor, a fluidized bed reactor was used for the continuous production of ethanol from glucose. Immobilized yeast was prepared by entrapping whole cells of Saccharomyces cerevisiae within a Caalginate matrix. It was found that the efficiency of the ethanol production in a fluidized bed reactor was 100% better than that for a packed bed reactor system. The alcohol productivity obtained was 21 g/l/hr in a fluidized bed reactor at 94% of conversion level.     

Production of L-DOPA from pyrocatechol and DL-serine by bioconversion using immobilized Erwinia herbicola cells

Summary Immobilized cells of Erwinia herbicola were used for L-DOPA production from pyrocatechol and DL-serine. Optimal conditions have been defined and utilized in batch and continuous reactors. A maximal volumetric productivity of 0.46 g/l.h in L-DOPA was obtained with a conversion yield of 18% (L-DOPA concentration 2.3 g/l).     

Continous production of free gluconic acid by Gluconobacter suboxydans IFO 3290 immobilized by adsorption on ceramic honeycomb monolith: effect of reactor configuration on further oxidation of gluconic acid to keto-gluconic acid

Summary Gluconobacter suboxydans IFO 3290 was immobilized by adsorption on ceramic honeycomb monolith, and continuous production of free gluconic acid from 100 g/l glucose was carried out in one- and three-stage monolith reactors. Further oxidation of gluconic acid to keto-gluconic acid by the immobilized cells has been found to be more suppressed in the three-stage monolith reactor. This finding can be explained by the fact that, with the three-stage reactor, the opportunity to oxidize gluconic acid further was decreased because the residence time of the reaction mixture at glucose conversion above the threshold value was shorter.     

Visual detection of β-fructofuranosidase (inulase) —Regulatory mutants ofKluyveromyces fragilis

Summary Inulase constitutive mutant cells of the yeastKluyveromyces fragilis were enumerated in continuous culture cell populations. After cloning and growth on glycerol agar plates, mutant colonies stained red when exposed to a mixture of sucrose and a chromogenic reagent for glucose.Mutants with improved inulase production on glucose were isolated from opaque agar plates containing undissolved inulin. Mutant colonies were surrounded with clearing zones. Attempts to isolate similar mutants by selection for 2-deoxyglucose resistance proved unsuccessful withK. fragilis.     

Production of 2-keto-3-deoxygluconate by immobilized cells of Sulfolobus solfataricus

Summary 2-Keto-3-deoxygluconate, an intermediate of glucose breakdown inSulfolobus solfataricus, was produced by enzymic dehydration of gluconate using whole cells of the micro-organism immobilized in crude egg white. The degradation of 2-keto-3-deoxygluconate to pyruvate and glyceraldehyde was avoided by inhibiting the aldolase activity in the cells by sodium borohydride treatment.     

Scale-up of flat-plate reactors for enzymatic hydrolysis of fats and oils

To determine the feasibility of continuous enzymatic fat-splitting, immobilized lipase reactors were constructed from alternating layers of enzyme support material and separator screens. Partially purified lipase from Thermomyces lanuginosus was loaded onto the support material at pH 5.5 by irreversible adsorption. Melted edible tallow at 51°C was pumped through the immobilized enzyme layers and swept from the downstream separator screens by buffer recycled from a continuous oil/water separator. Results from continuous operation of 10-layer reactors were compared with data from single-layer reactors. The activity per square centimeter of 10-layer reactors was nearly as much as that of single-layer reactors at the same enzyme loading and oil feed rate. Data were fitted to an empirical mathematical model.     

Film fermentor for ethanol production by yeast immobilized on cotton cloth

Summary Saccharomyces cerevisiae cells were immobilized on cotton cloth. The resulting yeast films were placed in parallel in a rectangular fermentor which was designed for scale-up. Ethanol production from sugars in the hydrolysate of Jerusalem artichoke tubers was studied in three modes of operation: batch, circulated batch and continuous flow. Circulated batch fermentation gave the shortest time of fermentation and accordingly the highest average ethanol productivity.     

Itaconic acid production by immobilizedAspergillus terreus from xylose and glucose

Summary Aspergillus terreus NRRC 1960 spores were entrapped in calcium alginate gel beads or alternotely the fungal mycelium was immobilized either on Celite R-626 or in agar gel cubes, and the biocatalyst was employed both in repeated batch and in continuous column reactors to produce itaconic acid from D-xylose or D-glucose. The highest itaconic acid yield obtained in a submerged culture batch fermentation was 54.5% based on total initial glucose (55 g/l) with a volumetric productivity of 0.32 g/l h, and 44.8% from xylose (67 g/l) with a productivity of 0.20 g/l h. In a repeated batch fermentation mycelium immobilized in agar gel had a productivity of 0.112 g/l h, and mycelium grown from spores immobilized in calcium alginate gel 0.06 g/l h, both from xylose (60 g/l). With the best immobilized biocatalyst system used employing Celite R-626 as a carrier, volumetric productivities of 1.2 g/l h from glucose and 0.56 g/l h from xylose (both at 60 g/l) were obtained in continuous column operation for more than 2 weeks.     

Phenolics production by encapsulated Nicotiana tabacum cells

Plant cells of tobacco (Nicotiana tabacum L.) were grown for several generations in suspension cultures. Cells were immobilized in continuous bioreactors in calcium alginate (Ca Alg) beads or in poly-L-lysine (PLL) encapsulated calcium alginatehydrogels. In each case, the cells were fed continuously a modified Linsmaier-Skoog plant cell culture medium. The bioreactor effluent was analyzed for total phenolic compounds. The net specific productivity of phenolics was calculated on a daily basis for several test runs. For comparison, productivity in suspension cultures was monitored. Productivity of suspended cells declined to zero within 9 d; both immobilized and encapsulated cells remained productive for 16 d following inoculation. Specific productivity by encapsulated cells was higher than that by immobilized cells; in both types similar rates of decline in productivity occurred.     

Preparation of lactose free milk by fermentation using immobilizedSaccharomyces fragilis

Summary Saccharomyces fragilis cells (40% w/v) were immobilized in 2% Ca-alginate and were used in a batch process for the removal of lactose from milk by fermentation. Immobilized cells (10 g) could completely desugarate 100 mL of milk in 3.5 h. The immobilized preparation was used repeatedly in 15 batches without decrease in the activity.