Fructose production by immobilizedArthrobacter cells

Summary ImmobilizedArthrobacter cells (NRRL-B-3728) were used for continuous isomerization of glucose to fructose in a bioreactor system. The system utilized stationary phase (55h) cells (2.2×10⁹ CFU/ml saline) immobilized onto K-carrageenan (3% w/v) beads [cells were heated at 65°C for 10 min to inactivate endogenous proteolytic enzymes]. Immobilized-cell preparations were hardened using three different glutaraldehyde systems. Glutaraldehyde (0.2 M) treated-immobilized cells (pH 7.0, 5°C for 30 min) exhibited good gel strength and high glucose isomerase activities. Maximal bioreactor isomerization of 44% was achieved when a buffered feedstock containing 40% glucose was fed into the column (60°C) at a flow rate of 0.2 ml/min. The biological half-life of glucose isomerase activities in this system was 400 h. Scanning electron microscopy revealed large numbers of cells distributed within the beads. A thin layer surrounding the beads following glutaraldehyde treatment was mainly due to cross-linking reactions between cell proteins and glutaraldehyde. This layer prevented leaking of cells during continuous isomerization reaction.     

Use of agarose-entrapped Aspergillus niger cells for the production of citric acid from soy whey

Aspergillus niger cells immobilized in agarose beads were utilized for the productin of citric acid from soy whey, a by-product generated during the tofu-making process. Soy when samples supplemented with 10% sucrose were inoculated with 10% (w/v) free and immobilized cells and incubated at 30°C in a shaker water bath at a speed of 200–220 rpm. Maximal citric acid yields of 21 g/l and 27 g/l with free and immobilized cells, respectively, were recorded on the 10th day under repeated batch conditions.     

Gel beads composed of collagen reconstituted in alginate

Spherical gel beads of collagen/alginate were prepared by discharging droplets of a mixture containing collagen (1.07-1.9 mg/ml) and alginate (1.2-1.5% w/v) into 1.5% w/v CaCl2 solution at 4°C. Collagen in the gel beads was reconstituted by raising the temperature to 37°C after alginate was liquefied by citrate. Scanning electron microscopy of the beads revealed the characteristic fibrous structure of collagen. To demonstrate the application of this new technique in cell culture, GH3 rat pituitary tumor cells were entrapped and grown in the gel beads. The immobilized cells proliferated to a density of 1.95 x 106 cell/ml which is about an order of magnitude higher than that grown in the alginate beads.     

Integrated immobilized cell reactor-adsorption system for β-cyclodextrin production: a model study using PVA-cryogel entrapped Bacillus agaradhaerens cells

Production of cyclodextrins (CDs) by immobilized cells of the alkaliphilic Bacillus agaradhaerens LS-3C with integrated product recovery was studied. The microorganism was entrapped in polyvinyl alcohol-cryogel beads and used as a convenient source of immobilized cyclodextrin glycosyltransferase (CGTase). On activation by incubation in the cultivation medium containing 1% (w/v) starch, the entrapped cells multiplied and secreted CGTase with an activity of 2–3 mg -cyclodextrin h^–1 g^–1 beads. The immobilized biocatalyst exhibited maximum activity at pH 9 and 50 °C, and formed cyclodextrins comprising 92–94% -CD and remaining -CD. The cyclodextrin product from the immobilized cell bioreactor was continuously recovered by adsorption to Amberlite XAD-4 in a recycle batch mode. The product adsorption was facilitated at low temperature while hot water was used for elution.     

Fermentation of xylose and rice straw hydrolysate to ethanol byCandida shehatae NCL-3501

Candida shehatae NCL-3501 utilized glucose and xylose efficiently in batch cultures. The specific rate of ethanol production was higher with mixtures of glucose and xylose (0.64–0.83 g g^–1 cells d^–1) compared to that with individual sugars (0.38–0.58 g g^–1 cells d^–1). Although the optimum temperature for growth was 30°C, this strain grew and produced appreciable levels of ethanol at 45°C. A stable ethanol yield (0.40–0.43 g g^–1 substrate utilized) was obtained between 10 g L^–1 and 80 g L^–1 of initial xylose concentration. Conversion efficiency was further improved by immobilization of the cells in calcium alginate beads. Free or immobilized cells ofC. shehatae NCL-3501 efficiently utilized sugars present in rice straw hemicellulose hydrolysate, prepared by two different methods, within 48 h. Ethanol yields of 0.45 g g^–1 and 0.5 g g^–1 from autohydrolysate, and 0.37 g g^–1 from acid hydrolysate were produced by free and immobilized cells, respectively.     

Repeated fed-batch lactic acid production in a packed bed-stirred fermentor system using a pH feedback feeding method

Lactic acid production by repeated fed-batch fermentation using free and immobilized cells of Lactobacillus lactis-11 in a packed bed-stirred fermentor (PBSF) system filled with different support materials including ceramic beads, macro-activated carbon cylinders and glass fiber balls was investigated. The results showed that the optimal support materials were the ceramic beads with diameters of 1–2 mm. Compared with the free cell fermentation system, lactic acid production and volumetric productivity in the PBSF system increased by 16.6 and 12.5%, respectively. Though the concentration of free cells decreased sharply, lactic acid production remained stable in five consecutive fed-batch runs using the PBSF system. pH gradients, immobilized cell concentration and mass diffusion in the packed bed were all affected by the recirculation rate of the culture broth. Maximum lactic acid production, productivity and yield occurred at a recirculation rate of 50 mL min⁻¹.     

Mannose production from fructose by free and immobilized <Emphasis Type="SmallCaps">d</Emphasis>-lyxose isomerases from <Emphasis Type="Italic">Providencia stuartii</Emphasis>

A recombinant d-lyxose isomerase from Providencia stuartii was immobilized on Duolite A568 beads which gave the highest conversion of d-fructose to d-mannose among the various immobilization beads evaluated. Maximum activities of both the free and immobilized enzymes for fructose isomerization were at pH 7.5 and 45°C in the presence of 1 mM Mn²⁺. Enzyme half-lives were 14 and 30 h at 35°C and 3.4 and 5.1 h at 45°C, respectively. The immobilized enzyme in 300 g fructose/l (replaced hourly), produced 75 g mannose/l at 35°C = 25% (w/w) yield with a productivity of 75 g mannose l⁻¹ h⁻¹ after 23 cycles.     

Storage and growth of neuroblastoma cells immobilized in calcium-alginate beads

Summary Mouse neuroblastoma cells (N18) were immobilized in calcium-alginate gel beads. Under standard culture conditions (37° C; 5% CO₂), cell growth was observed inside the beads. The number of cells increased threefold during 7 days of culture with cell division and differentiation visualized by electron microscopy. Cell properties maintained after short-term storage (2–3 days at 4° C) included: (i) properties of voltage-dependent ionic channels tested by patch-clamp electrophysiological techniques; (ii) expression of cell-adhesion membrane proteins tested by immunohistochemistry (iii) morphological differentiation obtained by depletion of foetal calf serum in culture medium. The advantages of such an immobilization technique as applied to neurone cells are discussed. Offprint requests to: M. Simonneau     

Increasing the stability of immobilizedLactococcus lactis cultures stored at 4 °C

Summary Immobilized cell technology was used to prepare concentrated cultures ofLactococcus lactis that lost only 22% of viability over a 30-day storage period at 4°C. Concentrated cultures ofL lactis CRA-1 were immobilized in calcium alginate beads and added to glycerol, NaCl or sucrose-NaCl solutions in order to obtain a_w readings ranging from 0.91 to 0.97. The suspensions were subsequently placed at 4°C and viability (CFU g^–1 of bead) was followed during storage. Viability losses were high at a_w readings of 0.95 and 0.97 and pH dropped significantly (up to one unit) in the unbuffered solutions. Addition of 1% soytone or glycerophosphate helphed stabilize pH, and a beneficial effect on viability during storage was observed in the glycerol-soytone mix when the beads were added to the conservation solutions immediately following immobilization. When beads were added to the conservation solution immediately following immobilization, a 70% drop in cell counts occurred during the first 5 days of incubation. Dipping theL lactis-carrying beads in milk for 2h before mixing with the glycerolsoytone 0.93 a_w solution reduced this initial 5-day viability loss. Cultures grown in the alginate beads also had good stability in the 0.93 a_w glycerol-soytone solution, where 78% of the population was viable after 30 days at 4°C. The process could be used to store immobilized cells at a processing plant, or by suppliers of lactic starters who wish to ship cultures without freezing or drying.     

Biosorption and desorption studies of chromium (III) by free and immobilized Rhizobium (BJVr 12) cell biomass

Experiments with free cell biomass (cells + exopolysaccharides) ofRhizobium BJVr 12 (mungbean isolate) showed that amount ofCr³⁺ ion sorbed is influenced by the amount of biomass toCr³⁺ concentration ratio and time of contact. A ratio of 0.5 gfresh biomass to 10.0 ml 5.03 ppm Cr³⁺ sorbed 0.0275 mg Crequivalent to an uptake of 2.86 mg Cr g-¹ dry biomass and 1.0g: 10.0 ml sorbed 0.0366 mg Cr equivalent to an uptake of 1.9 mg Crg-¹ biomass. Immobilized cell biomass in ceramic beads and inaquacel (a porous cellulose carrier with a charged surface) were moreefficient than free cell biomass in adsorbing Cr(III). A reduction of49.7percnt; of Cr(III) for free cells, 95.6% for cells immobilized inceramic beads and 94.6% for cells in aquacel was achieved after 48hours under shaken conditions. Sorption capacities of immobilized cellbiomass in ceramic beads and aquacel ranged from 5.01 to 5.06 mg Crg^-1 dry cell biomass. The biosorption of Cr³⁺follows generally the Langmuir and Freundlich models of adsorption at lowCr³⁺ concentrations. The Langmuir constant for immobilizedcells in ceramic beads are: Q₀, 0.065 mmol Crg^-1 biomass; b (affinity constant), - 694 lmmol^-1 Cr and for cells in aquacel Q, 0.07 mmol Crg^-1 biomass; b, - 694 l mmol Cr g^-1 Cr. TheFreundlich constants are: K, 0.071 mmol Cr g^-1 biomass; n,0.13 g^-1 biomass l^-1 and for aquacel: K, 0.074mmol g^-1 biomass; n, 0.13 g^-1 biomass. Biotrapsmade up of immobilized cells in ceramic beads and aquacel were tested foradsorbing Cr(III) using two different flow rates: 0.5 ml/min and 1.5 ml/min.A significantly higher amount of Cr(III) was adsorbed at the lower flow rateof 0.5 ml/min. Biosorption of Cr³⁺ is competitive. Thetreatment of a waste water sample containing 6.03 ppm Cr³⁺ andother cations with the biomass reduced the Cr³⁺ concentrationto that much lower than for the test solution containing only Cr. Recoveryof biosorbed Cr(III) was by treatment at a different pH using dilute HClsolution. Recovery was higher for cells imbibed in ceramic beads thanaquacel. Percentage recoveries for cells in aquacel are 46.4% at pH1.0, 33.0% at pH 3.0 and 6.6% at pH 6.0–7.0. For cellsin ceramic beads, percentage recoveries are: 93.1% at pH 1.0,75.6% at pH 3.0 and 16.4% at pH 6.0–7.0. Biosorption ofCr³⁺ by cells immobilized in ceramic beads is reversible butonly partially for cells in aquacel.     

Alcoholic fermentation by agar-immobilized yeast cells

Immobilized yeast cells in agar gel beads were used in a packed bed reactor for the production of ethanol from cane molasses at 30°C, pH 4.5. The maximum productivity, 79.5g ethanol/l.h was obtained with 195g/l reducing sugar as feed. Substrate (64.2%) was utilized at a dilution of 1.33h^-1. The immobilized cell reactor was operated continuously at a constant dilution rate of 0.67h^-1 for 100 days. The maximum specific ethanol productivity and specific sugar uptake rate were 0.610g ethanol/g cell.h and 1.275g sugar/g cell.h, respectively.     

Inhibition of psychrotrophic bacteria in raw milk by immobilized lactic acid bacteria

Summary Cells ofLactococcus lactis orLactobacillus helveticus were immobilized in calcium-alginate beads, added to raw milk, and incubated 48 h at 7°C. The addition of 2.7×10⁷ immobilizedLc.lactis or 13×10⁷ immobilizedLb. helveticus cells per mL reduced the development of the psychrotrophic bacteria of raw milk by approximately 50%. The pH of the raw milk dropped 0.10 to 0.22 units under these conditions. Periodic agitation of the seeded raw milk increased the inhibitory activity of the immobilized lactic acid bacteria (LAB). Free LAB cells in the system were only of 0.5% of total LAB. The use of immobilized LAB to inhibit psychrotrophic bacteria might be extended to raw milks destined to the manufacture of non-fermented dairy products.     

Transformation of arachidonic acid to 19-hydroxy- and 20-hydroxy-eicosatetraenoic acids using Candida bombicola

Candida bombicola (ATCC 22214) and C. apicola (ATCC 96134), grown on glucose (100 g l^–1) and arachidonic acid (5Z, 8Z, 11Z, 14Z-eicosatetraenoic acid; AA), 1.25 g l^–1, synthesized sophorolipid up to 0.93 g l^–1. Acid hydrolysis of sophorolipid yielded 19-hydroxy-5Z, 8Z, 11Z, 14Z-eicosatetraenoic acid (19-HETE) and 20-hydroxy-5Z, 8Z, 11Z, 14Z-eicosatetraenoic acid (20-HETE) which were identified by TLC and GC-MS; the ratio of synthesis was 73:27, respectively. Conversion of AA by immobilized Candida bombicola, suspended in beads of 2% (w/v) calcium alginate for 96 h, gave an 83% conversion of 1 g AA l^–1 to 19- and 20-HETE. There was no significant loss in the efficiency of the immobilized cells after ten uses.     

Immobilization of <Emphasis Type="Bold">β</Emphasis>-fructofuranosidase from <Emphasis Type="Italic">Aspergillus japonicus</Emphasis> on chitosan using tris(hydroxymethyl)phosphine or glutaraldehyde as a coupling agent

A partially purified -fructofuranosidase from Aspergillus japonicus was covalently immobilized on to chitosan beads using either glutaraldehyde or tris(hydroxymethyl)phosphine (THP) as a coupling agent. Compared with the glutaraldehyde-immobilized and the free enzyme, the THP-immobilized enzyme had the highest thermal stability with 78% activity retained after 12 days at 37 ° C. The THP-immobilized enzyme also had higher reusability than that immobilized by glutaraldehyde, 75% activity was retained after 11 batches (or 11 days) at 37° C for the THP immobilized enzyme system. Less yield (48%) of fructooligosaccharides (FOS) were produced by the THP-immobilized enzyme compared with the free enzyme system (58%) from 50 (w/v) sucrose at 50 ° C.     

Batch fermentation with entrapped growing cells ofLactobacillus casei

Summary Growing cells ofLactobacillus casei were entrapped in-carrageenan/locust bean gum (LBG) (2:1 or 2.75%:0.25% w/w respectively) mixed gel beads (two ranges of diameter: 0.5–1.0 and 1.0–2.0 mm) to fermentLactobacillus Selection (LBS) medium and produce biomass. The results showed significant influence of initial cell loading of the beads and bead size on the fermentation rate. The highest cell release rates were obtained with 2.75%:0.25%-carrageenan/LBG small diameter gel beads. However, 17 h fermentation of LBS medium with immobilized cells resulted in substantial softening of the gel matrix, prohibiting reuse of immobilized biocatalysts as inoculum in subsequent batch fermentation. A dynamic shear rheological study showed that the gel weakness was related to chemical interactions with the medium. Results indicated that part of the matrix-stabilizing K⁺ ions diffused back to the medium. Stabilization of the gel was obtained by adding potassium ions to the LBS medium;L. casei growth was not altered by this supplementation. Fermentation of LBS medium supplemented with KCl byL. casei showed higher cell counts in the broth medium with immobilized cells than with free cells, reaching 10¹⁰ cells/ml after about 10 h with entrapped cells in 0.5–1.0 mm diameter beads and 17 h with free cells. Counts in the gel beads after fermentation were higher than 10¹¹ cells/ml and bead integrity was maintained throughout fermentation.     

Optimization of lactic acid production by immobilized <Emphasis Type="Italic">Lactococcus lactis</Emphasis> IO-1

Production of lactic acid from glucose by immobilized cells of Lactococcus lactis IO-1 was investigated using cells that had been immobilized by either entrapment in beads of alginate or encapsulation in microcapsules of alginate membrane. The fermentation process was optimized in shake flasks using the Taguchi method and then further assessed in a production bioreactor. The bioreactor consisted of a packed bed of immobilized cells and its operation involved recycling of the broth through the bed. Both batch and continuous modes of operation of the reactor were investigated. Microencapsulation proved to be the better method of immobilization. For microencapsulated cells at immobilized cell concentration of 5.3 g l⁻¹, the optimal production medium had the following initial concentrations of nutrients (g l⁻¹): glucose 45, yeast extract 10, beef extract 10, peptone 7.5 and calcium chloride 10 at an initial pH of 6.85. Under these conditions, at 37 °C, the volumetric productivity of lactic acid in shake flasks was 1.8 g l⁻¹ h⁻¹. Use of a packed bed of encapsulated cells with recycle of the broth through the bed, increased the volumetric productivity to 4.5 g l⁻¹ h⁻¹. The packed bed could be used in repeated batch runs to produce lactic acid.     

Production of molecular hydrogen with immobilized cells ofRhodospirillum rubrum

Summary Cells ofRhodospirillum rubrum have been immobilized in various gels and tested for photobiological hydrogen production. Agar proved to be the best immobilizing agent with respect to production rates as well as stability. Agar immobilized cells were also superior compared to liquid suspension cultures. Growth conditions of the cells prior to immobilization, e.g. cell age, light intensity or nutrient composition, were of primary importance for the activity in the later immobilized state. A reactor with agar immobilized cells has been operated successfully over 3000 h with a loss of the activity of about 60%. Mean rates for hydrogen production for immobilized cells in this work during the first 60 to 70 hours after immobilization were in the range of 18 to 34 μl H₂ mg⁻¹ d.w. h⁻¹ and thus by a factor of up to 2 higher than liquid cultures under the same conditions. Maximal rates of hydrogen production (57 μl H₂ ml⁻¹ immobilized cell suspension) were reached in agar gel beads with cells immobilized after 70 h growth in liquid culture in the light and a cell density of 1.0 mg ml⁻¹, 70 h after immobilization.     

2-Ethyl-1-hexanol fatty acid esters from rapeseed oil by transesterification

Summary Fatty acid esters of 2-ethyl-1-hexanol were produced in a small pilot scale from rapeseed oil by Candida cylindracea lipase catalyzed transesterification (alcoholysis) without added solvent. Up to 90% conversion of rapeseed oil (97% of theoretical) was obtained in 8 h in 2 kg scale at 37° C with 3.4% (w/w) lipase immobilized on an anion exchange resin Amberlite XAD-7, rapeseed oil:2-ethyl-1-hexanol substrate molar ratio of 2.8, and 3% (w/w) of added water.     

Synthesis of ethyl ferulate in organic medium using celite-immobilized lipase

In the present work we have evaluated synthesis of ethyl ferulate by the esterification reaction of ferulic acid and ethanol catalyzed by a commercial lipase (Steapsin) immobilized onto celite-545 in a short period of 6 h in DMSO. The immobilized lipase was treated with cross-linking agent glutaraldehyde (1%; v/v). The optimum synthesis of ethyl ferulate was recorded at 45 °C, pH 8.5 and 1:1 ratio of ethanol and ferulic acid. Co²⁺, Ba²⁺and Pb²⁺ ions enhanced the synthesis of ethyl ferulate Hg²⁺, Cd³⁺and NH⁴⁺ ions had mild inhibitory effect. The celite-bound lipase produced 68 mM of ethyl ferulate under optimized reaction conditions.     

壳聚糖球固定化酵母细胞的研究

以戊二醛为交联剂,将壳聚糖球交联引入醛基,然后将交联的壳聚糖球浸泡在酵母细胞悬浮液中,制备了固定化酵母细胞壳聚糖球。以苯乙酮酸为底物,催化合成了D-扁桃酸。最优固定化条件是戊二醛的质量分数w(GA)=1%,酵母细胞与交联壳聚糖球的质量比m(Y):m(CB)0=0.5,交联时间为6h,固定化时间为18h,底物浓度为10mmol/L,在此条件下反应最大转化率和产物光学纯度分别高达67.86%和98.05?。固定化酵母壳聚糖球具有良好的重复使用性和贮存稳定性。