Performance of rotating packed disk reactor with immobilized glucose oxidase

Summary Reactor performance was studied to investigate whether a rotating packed disk reactor (RPDR) can be used for the enzymatic oxidation of biochemicals. The disks were packed with calcium alginate beads with immobilized glucose oxidase and catalase, which catalyze the reaction of glucose and oxygen. The production rate of gluconic acid increased with the speed of rotation and the bulk flow rate. An optimum submergence for maximum productivity existed.     

Alginate/carbon composite beads for laccase and glucose oxidase encapsulation: application in biofuel cell technology

Alginate–carbon beads were prepared in order to develop a biocompatible matrix for laccase and glucose oxidase immobilization for application in biofuel cell technology. The enzyme loading capacity was high (91%) in pure alginate beads for glucose oxidase. For laccase, the loading capacity was enhanced from 75% to 83% by introducing carbon. Desorption out of the matrix was controlled by the enzymes’ diffusion and reached a plateau after 40 h for laccase and 70 h for glucose oxidase. Two-thirds of both enzymes was irreversibly retained inside the alginate beads. This proportion increased to 80% for laccase in combined alginate/carbon beads. Half-life of the adsorbed enzyme was enhanced to 74 days for laccase in carbon/alginate beads and 45 days for glucose oxidase in pure alginate as compared to 38 days and 23 days for free enzymes, respectively.     

Preparation and kinetic behavior of immobilized whole cell biocatalysts

Actinoplanes missouriensis (for glucose isomerase), Kluyveromyces fragilis (for beta-galactosidase), and Saccharomyces cerevisiae (for invertase) cells were successfully entrapped within cellulose and cellulose di- and triacetate beads employing several carried solvent systems. Cellulose beads prepared using a melt of dimethylsulfoxide (DMSO) and N-ethylpyridinium chloride (NEPC), or cellulose diacetate using a mixture of acetone and DMSO as solvent, were found to be promising as carriers for the invertase system, cellulose triacetate beads with DMSO as solvent for yeast beta-galactosidase, and cellulose beads with a melt of DMSO and NEPC as solvent for glucose isomerase. The kinetic behavior of A. missouriensis glucose isomerase whole cell cellulose beads in a plug-flow column reactor was studied as an example system in greater detail.     

Optimal covalent immobilization of glucose oxidase-containing liposomes for highly stable biocatalyst in bioreactor

The glucose oxidase-containing liposomes (GOL) were prepared by entrapping glucose oxidase (GO) in the liposomes composed of phosphatidylcholine (PC), dimyristoyl L-alpha-phosphatidylethanolamine (DMPE), and cholesterol (Chol) and then covalently immobilized in the glutaraldehyde-activated chitosan gel beads. The immobilized GOL gel beads (IGOL) were characterized to obtain a highly stable biocatalyst applicable to bioreactor. At first, the glutaraldehyde concentration used in the gel beads activation as well as the immobilizing temperature and time were optimized to enhance the immobilization yield of the GOL to the highest extent. The liposome membrane composition and liposome size were then optimized to obtain the greatest possible immobilization yield of the GOL, the highest possible activity efficiency of the IGOL, and the lowest possible leakage of the entrapped GO during the GOL immobilization. As a result, the optimal immobilization conditions were found to be as follows: the liposome composition, PC/DMPE/Chol = 65/5/30 (molar percentage); the liposome size, 100 nm; the glutaraldehyde concentration, 2% (w/v); the immobilizing temperature, 4 degrees C; and the immobilizing time, 10 h. Furthermore, the optimal IGOL prepared were characterized by its rapidly increasing effective GO activity to the externally added substrate (glucose) with increasing temperature from 20 to 40 degrees C, and also by its high stability at 40 degrees C against not only the thermal denaturation in a long-term (7 days) incubation but also the bubbling stress in a bubble column. Finally, compared to the conventionally immobilized glucose oxidase (IGO), the higher operational stability of the optimal IGOL was verified by using it either repeatedly (4 times) or for a long time (7 days) to catalyze the glucose oxidation in a small-scale airlift bioreactor.     

Conducting elastomer surface texturing: a path to electrode spotting. Application to the biochip production

A new active support for electro-chemiluminescent biochip preparation has been developed. This material was based on an original material composed of graphite modified polydimethyl siloxane (PDMS). The addressed inclusion of Sepharose beads at the surface of this elastomeric electrode generated interesting local high specific surface. The electrode was characterised by electrochemical (cyclic voltametry, chronoamperomatry) and imaging (scanning electron microscopy (SEM)) methods, and a surface area increase factor of 50 was found, linked to the texturing of the surface generated by the presence of the Sepharose beads. The consequence of this increase was shown to be a jump of the local electrochemical activity which induced a well defined and localised electro-chemiluminescent signal. The new material was used to design biochips based on the electro-chemiluminescent reaction of luminol with enzymatically produced hydrogen peroxide. Thus, when using beads bearing bio-molecules such nucleic acid or human IgG, in conjunction with glucose oxidas-labelled DNA or antibody, sensitive biochips could be obtained with detection limits of 10(11) and 10(10) molecules, respectively. Multi-parameter enzyme-based biochips could also be achieved by locally adsorbing, at the PDMS-graphite surface, either glucose oxidase, lactate oxidase or choline oxidase. Detection limits of 10 microM for lactate and choline and 20 microM for glucose were found, with detection ranging over two decades at least.     

Calcium alginate immobilized hybridomas grown using a fluidized-bed perfusion system with a protein-free medium

Hybridoma SPO1 cells were immobilized in calcium alginate beads and were further grown in a fluidized-bed perfusion system with a protein-free medium. The presence of serum in the steps of entrapment was shown to be helpful for the preservation of cell viability. Each step during immobilization was investigated with respect to the extent of cell damage caused. The immobilization process using small beads caused a lower cell viability initially but allowed a higher rate of cell growth subsequently, compared to those in large beads. In a perfusion system for the continuous production of monoclonal antibodies (MAb), the viable cell density reached 2×10⁷ cells per ml of beads with a viability of 40%. Compared with the cells in suspension culture, the immobilized SPO1 cells showed higher viable cell based specific rates of substrate uptake (glucose and glutamine) and of MAb production. A significant drop in the formation of lactate after the cell growth entered a steady state suggested a higher activity of the Tricarboxylic Acid Cycle in the cells when the cell density became high.     

结冷胶固定化保加利亚乳杆菌及在玉米秸秆连续发酵d-乳酸中的应用

秸秆生物炼制化学品是解决秸秆资源利用附加值低、减轻秸秆焚烧带来的环境污染的主要方法之一。本研究制备了结冷胶固定化保加利亚乳酸杆菌(Lactobacillus bulgaricus)T15凝胶珠(结冷胶-T15凝胶珠),并对其性质进行表征,建立了结冷胶-T15凝胶珠固定化细胞循环连续发酵产D-乳酸发酵工艺。结冷胶-T15凝胶珠的断裂应力为(91.68±0.11) kPa,较海藻酸钙固定化T15凝胶珠(海藻酸钙-T15凝胶珠)提高了125.12%,表明结冷胶-T15凝胶珠的强度更强。以结冷胶-T15凝胶珠为出发菌株,葡萄糖为发酵基质,10批次循环(720h)发酵,其D-乳酸最高批次产量为(72.90±2.79)g/L,较海藻酸钙-T15凝胶珠提高了33.85%,较游离T15提高了37.70%。将葡萄糖更换为玉米秸秆酶解液,使用结冷胶-T15凝胶珠进行10批次循环(240 h)发酵,D-乳酸生产强度可达(1.74±0.79)g/(L·h),远高于游离菌。10批次循环发酵后结冷胶-T15凝胶珠磨损率小于5%,表明结冷胶是一种细胞固定化的良好载体,可广泛应用于细胞固定化工业发酵领域。本研究为细胞...     

Enhancement of oxygen absorption by magnetite-containing beads of immobilized glucose oxidase

Rates of oxygen absorption into glucose solutions were measured using an immobilized-enzyme reactor, in which magnetite-containing beads of immobilized glucose oxidase were moved by a revolving magnetic field to reduce the mass transfer resistances at the gas–liquid interface and around the bead. Data were also obtained for oxygen absorption into glucose solutions containing soluble or immobilized glucose oxidase (without magnetite), as well as for physical absorption of oxygen. The rates of physical absorption for the runs with the magnetite-containing beads increased because of mechanical stirring caused by spinning of the beads at the gas-liquid interface. In this case the experimental enhancement factors were found to be larger than those predicted on the basis of the film theory for gas absorption with a pseudo-first order reaction.     

Adaptation of a manometric biosensor to measure glucose and lactose

A manometric sensor previously developed to measure urea was modified to measure glucose and lactose through enzymatic oxidation. Change in pressure in an enclosed cavity was correlated to the depletion of oxygen resulting from the enzymatic oxidation of glucose or lactose. The response of the sensor was linear and could be made adjustable over a large range by adjusting the amount of sample loaded into the fixed volume reactor. Because of the slow mutarotation of glucose, the oxidation of glucose was not allowed to proceed to completion. Therefore, the precision of the sensor (approximately 0.2 mM in a range from 0 to 5 mM) was limited by variations in the oxidation rate of glucose by glucose oxidase. Because the assay for lactose measured glucose subsequent to the hydrolysis of lactose by beta-galactosidase, the same degree of precision was observed in lactose. Milk lactose, typically at concentrations of about 150 mM, was estimated using the lactose assay after first diluting the samples. For many fluids such as milk, the use of manometric sensors for oxidizable substrates may be preferable to optical and electrochemical methods because they are robust and suffer a low degree of optical and chemical interferences. Glucose and lactose are representative of many important oxidizable substrates, which may be determined in this manner, many of which do not suffer from limitations caused by mutarotation. In theory, detection limits less than 1 microM may be achieved using these methods.     

Extractive Synthesis of Ethyl‐Oleate Using Alginate Gel Co‐Entrapped Yeast Cells and Lipase Enzyme

To synthesize ethyl‐oleate ester, a complex Ca‐alginate gel co‐entrapped system was prepared. The gel beads contained two kinds of biocatalysts (living yeast cells and a lipase enzyme) and various amounts of glucose (100–400 g/L). These alginate beads dispersed directly in pure oleic acid. To follow the bioconversion of the cell growth, the glucose uptake of yeast cells, the concentration of ethanol inside the gel beads and the ethyl‐oleate concentration in oleic acid phase was monitored. The glucose was quantitatively taken up by yeast cells during 24–72 h, depending on the concentration of glucose. After this 24–72‐hour period, the glucose uptake was stopped. In accordance with changes in glucose concentration, the concentration of ethanol and ethyl‐oleate increased rapidly during the first day of fermentation and thereafter slowed down. It is supposed that the inhibitory effect of produced ethanol would be resolved by co‐immobilization of lipase in the same gel particles. Using lipase, one is able to transform ethanol to ethyl‐oleate, which is soluble in oleic acid. According to the data obtained a minimum of 4 U/mL lipase is required to increase ethyl‐oleate production significantly. Summing up it can be concluded that by means of this system a maximum yield of ethanol and ethyl‐oleate was achieved when gel beads containing 100 g/L glucose and 4 U/mL lipase enzyme were used.     

Glucose oxidation in a dual hollow fiber bioreactor with a silicone tube oxygenator

A dual hollow fiber bioreactor, consisting of an outer silicone membrane for oxygen supply and an inner polyamide membrane for substrate permeation, was used as an immobilized enzyme reactor to carry out enzymatic glucose oxidation. Attaching a silicone tube oxygenator to provide an additional oxygen supply improved the conversion in glucose oxidation when the oxygen supply was rate-limiting. The reactor was operated in both diffusion and ultrafiltration modes. In the latter case, the conversion was much higher, but the stability of the immobilized enzyme was better maintained in the diffusion mode. As the inlet glucose concentration increased from 10mM to 500mM, the conversion decreased from 70 to 20%.     

Measurement of the activity of attached bacteria using a sorption microcalorimeter

A method is described in which a flow sorption microcalorimeter was used to measure the heat production of Vibrio alginolyticus attached to polyacrylamide beads. Starved cells were attached to the beads and placed in the column of the calorimeter. Heat production from the metabolism of glucose by the attached cells was then determined. The specific rate of heat production of cells on the surface is compared with that of cells growing in solution. The results show a lowered rate of heat production per cell by the attached bacteria.     

Activation of hepatic glycogenolysis by phagocytic stimulation

Infusion of latex beads into isolated perfused rat livers transiently increased glucose output, perfusate lactate/pyruvate ratio and portal vein pressure, mimicking hepatic effects of heat-aggregated IgG (HAG). Indomethacin attenuated hepatic responses to latex beads, and extracellular calcium was required for full expression of hepatic responses. Prior infusion of HAG inhibited the glycogenolytic response to latex beads, supporting a common mechanism of action for the two agents.     

The importance of bead size measurement in mass-transfer modelling with immobilised cells

The effective diffusivity of O₂ inside immobilised cell particles has been much discussed. Most reported estimates are based on fitting a mass-transfer reaction model to measured total oxygen uptake rates. The particle diameter has the largest single influence in such models, but its accurate measurement has probably recieved insufficient attention. We have studied sorbitol and glucose oxidation by cells of Gluconobacter suboxydans entrapped in calcium alginate gel beads. These beads were found to shrink rapidly in air, so that size measurement under water is essential. By comparison with rigid particles of similar known size, it was shown that measurement of the microscopic image gives a systematic underestimate. In consequence, the fitted oxygen diffusivity will be around 20% too low. Careful attention to size measurement gave good agreement between diffusivity estimates from beads with different mean sizes and cell loadings, with a best value of 2.51 × 10⁹ m²s^–1, 92% of the value for pure water. The estimated diffusivity is not significantly affected by a distribution of bead sizes with up to 10% standard deviation about the same mean.     

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.     

Effects of diabetes on glucose oxidation in rat aorta after hypophysectomy and adrenalectomy

The influence of diabetes, hypophysectomy and adrenalectomy on glucose oxidation in rat aorta was studied. Diabetes was induced in normal, adrenalectomized and hypophysectomized-cortisone substituted rats by streptozotocin (65 mg/kg body weight). The oxidation of glucose to CO2 was determined during incubation of rat aorta in vitro for 2-3 hours. The aortic glucose oxidation was reduced after hypophysectomy but was unaffected by adrenalectomy. After streptozotocin treatment the rise in blood glucose concentration was similar in normal, adrenalectomized and hypophysectomized-cortisone substituted rats. In shamoperated diabetic rats the aortic glucose oxidation was reduced after a diabetes duration of 4 days. In adrenalectomized diabetic rats the aortic glucose oxidation was not significantly affected after 4 days but was reduced after a diabetes duration of 14 days. When adrenalectomized diabetic rats were treated with hydrocortisone the aortic glucose oxidation was reduced after diabetes for 4 days. After incubation of normal rat aorta in vitro for 6 hours with cortisol (1 microgram/ml) in the incubation medium a decrease in the aortic glucose oxidation was found. Incubation of aorta with only growth hormone had no effect. These results suggest that cortisol is of importance for the lowered glucose oxidation in diabetic rat aorta.     

海藻酸钙固定赤霉菌菌丝产素的研究

将赤霉菌丝固定在海藻酸钙微球中进行连续发酵,考察产赤霉素情况。对海藻酸钠和钙盐浓度固定赤霉菌菌丝的微球稳定性进行初步研究,讨论了固定不同菌龄的赤霉菌微球在不同葡萄糖浓度下的产素能力及菌丝生长能力。实验表明:菌丝微球较稳定的固定条件是菌丝8 g/L、海藻酸钠浓度3 g/L和钙离子浓度3 mol/L;摇瓶发酵72 h,90 h的菌丝微球中菌丝营养生长基本停止,当培养液葡萄糖浓度为2 g/L时,赤霉素终浓度为1 145.5 μg/ml,比生产速率为4.61×10^-3/h;在该条件下固定菌丝球的床层式连续发酵,赤霉素比生产速率为4.82×10^-3/h,是相应分批发酵过程中最大赤霉素生产速率的1.87倍。     

Glucose enhancement of LDL oxidation is strictly metal ion dependent

Recent evidence suggests that lipoprotein oxidation is increased in diabetes, however, the mechanism(s) for such observations are not clear. We examined the effect of glucose on low-density lipoprotein (LDL) oxidation using metal ion-dependent and -independent oxidation systems. Pathophysiological concentrations of glucose (25 mM) enhanced copper-induced LDL oxidation as determined by conjugated diene formation or relative electrophoretic mobility (REM) on agarose gels. Similarly, iron-induced LDL oxidation was stimulated by glucose resulting in 4- to 6-fold greater REM than control incubations without glucose. In contrast, glucose had no effect on metal ion-independent LDL oxidation by aqueous peroxyl radicals. The effect of glucose on metal ion-dependent LDL oxidation was associated with enhanced reduction of metal ions, and in the case of iron-induced LDL oxidation, was completely inhibited by superoxide dismutase. The effect of glucose was mimicked by other reducing sugars, such as fructose and mannose, and the extent to which each sugar enhanced LDL oxidation was closely linked to its metal ion-reducing activity. Thus, promotion of LDL oxidation by glucose is specific for metal ion-dependent oxidation and involves increased metal ion reduction. These results provide one potential mechanism for enhanced LDL oxidation in diabetes.     

Effects of immobilization on the kinetics of enzyme-catalyzed reactions. I. Glucose oxidase in a recirculation reactor system.

Glucose oxidase from Aspergillus niger was immobilized on nonporous glass beads by covalent bonding and its kinetics were studied in a packed-column recycle reactor. The optimum pH of the immobilized enzyme was the same as that of soluble enzyme; however, immobilized glucose oxidase showed a sharper pH-activity profile than that of the soluble enzyme. The kinetic behavior of immobilized glucose oxidase at optimum pH and 25 degrees C was similar to that of the soluble enzyme, but the immobilized material showed increased temperature sensitivity. Immobilized glucose oxidase showed no loss in activity on storage at 4 degrees C for nearly ten weeks. On continuous use for 60 hr, the immobilized enzyme showed about a 40% loss in activity but no change in the kinetic constant.     

Phosphorus-31 and carbon-13 nuclear magnetic resonance study of glucose and xylose metabolism in agarose-immobilized Candida tropicalis.

Candida tropicalis can ferment both hexose and pentose sugars. Here, we have used 31P and 13C nuclear magnetic resonance spectroscopy to study the capacity of this yeast species to metabolize glucose or xylose when immobilized in small (< 1-mm-diameter) agarose beads. Immobilized C. tropicalis metabolizing glucose showed rapid initial growth within the beads. A corresponding drop in the intracellular pH (from 7.8 to 7.25) and hydrolysis of intracellular polyphosphate stores were observed. Although the initial rate of glucose metabolism with immobilized C. tropicalis was similar to the rate observed previously in cell suspensions, a decrease by a factor of 2.5 occurred over 24 h. In addition to ethanol, a significant amount of glycerol was also produced. When immobilized C. tropicalis consumed xylose, cell growth within the beads was minimal. The intracellular pH dropped rapidly by 1.05 pH units to 6.4. Intracellular ATP levels were lower and intracellular Pi levels were higher than observed with glucose-perfused cells. Consumption of xylose by immobilized C. tropicalis was slower than was previously observed for oxygen-limited cell suspensions, and xylitol was the only fermentation product.