Fungus β-glycosidases: immobilization and use in alkyl-β-glycoside synthesis

Production of β-glycosidases: β-xylosidase and β-glucosidase by the fungus Sclerotinia sclerotiorum was optimized in the presence of different carbon sources. Immobilization supports with different physico-chemical characteristics were evaluated for use in continuous reactors. Immobilization and activity yields were calculated. Among the adsorption on Duolite, Amberlite, Celite and DEAE-sepharose, and entrapment in polyacrylamide gel or reticulation using glutaraldehyde, highest yields were obtained when β-xylosidase was adsorbed on Duolite A 7 and when β-glucosidase was adsorbed on DEAE-sepharose.

Enzyme preparations from S. sclerotiorum cultures were used in a biphasic (alcohol/aqueous) medium for the synthesis of alkyl-glycosides by trans-glycosylation of sugars and long-chain alcohols. The synthesis was studied under different conditions with primary and secondary alcohols as substrates, in the presence of free or immobilized enzyme. Xylan and cellobiose were used for the synthesis of alkyl-xylosides and alkyl-glucosides, respectively. The majority of the immobilized preparations were unable to catalyze the synthesis of alkyl-glycosides.

Highest yields were obtained when using xylan and C₄–C₆-alcohols. The reaction produced alkyl-β-xyloside and alkyl-β-xylobioside, as confirmed by MS/MS. Up to 22 mM iso-amyl-xyloside and 14 mM iso-amyl-xylobioside were produced from iso-amyl alcohol and xylan.     

Continuous biocatalytic synthesis of epoxypropane using a biofilm reactor

Mixed culture methanotrophic attached biofilms immobilized on diatomite particles in a three-phase fluidized bed reaction system were developed. Methane monooxygenase (MMO) activity on diatomite particles increased as soon as the lag phase ended. More than 90% of the MMO activity in the fluidized bed was attached. A biofilm concentration of 3.3c3.7mg dry weight cell (dwc) per g dry solid (DS) was observed. Batch experiments were performed to explore the possibility of producing epoxypropane by a propene–methane co-oxidation process. The effect of methane on the epoxidation of propene and the effect of propene on the growth of methanotroph was also studied. In continuous experiments, optimum mixed gas containing 35 methane, 20 propene and 45% oxygen were continuously circulated through the fluidized bed reactor to deliver substrates and extract product. Initial epoxypropane productivity was 110–150 μmol/day. The bioreactor operated continuously for 53 days without obvious loss of epoxypropane productivity.     

Continuous hydrolysis of oil by immobilized lipase in a countercurrent reactor

Lipase from Pseudomonas fluorescens biotype I was immobilized by adsorption of anion exchange resin using glutaraldehyde to enhance the adsorption. The activity yield of the immobilized lipase was very low (below 1%) when lipase activity was measured using emulsion substrate. The activity yield was 10-70% when lipase activity was measured using non-emulsion substrate. Countercurrent reactors for hydrolysis of oil using non-emulsion substrate were studied. A fluidized bed reactor was found to be superior to a fixed bed one since in a fixed bed reactor the separation rate of the two layers was slow and the flow rate of the reactor had to be slower than the separation rate. A fluidized bed reactor system equipped with settling compartments and stirring compartments was devised. Continuous lipolysis at 60 degrees C and continuous separation of oily product and water soluble product were performed. After continuous operation for more than 3 months, 70% of the initial activity of the immobilized lipase was observed at the end of the reaction.     

Countercurrent multistage fluidized bed reactor for immobilized biocatalysts: I. Modeling and simulation

For the application of immobilized enzymes, fixed bed reactors are used almost exclusively. Fixed bed reactors have specific disadvantages, especially for processes with a deactivating catalyst. Therefore, we have studied a novel reactor type with continuous transport of the immobilized biocatalyst. Flow of biocatalyst is countercurrent to the substrate solution. Because of a stagewise reactor design, back-mixing of biocatalyst is very limited and transport is nearly plug flow. The reactor operates at a constant flow rate and conversion, due to constant holdup of catalytic activity. The reactor performance is compared with a configuration of fixed bed reactors. For reactions in the first-order regime, enzyme requirements in this new reactor are slightly less than for fixed bed processes. The multistage fluidized bed appears to be an attractive reactor design to use biocatalyst to a low residual activity. However, nonuniformity of the particles might affect plug flow transport of the biocatalyst. A laboratory scale reactor and experiments are described in Part II(1) of this series. Hydrodynamic design aspects of a multistage fluidized bed are discussed in more detail in Part III.(2).     

Influence of different silica derivatives in the immobilization and stabilization of a Bacillus licheniformis protease (Subtilisin Carlsberg)

Alcalase 2T, a commercial preparation of Subtilisin Carlsberg, was covalent immobilized onto physiochemically characterized silica supports. The effect of mean pore diameter and surface chemistry on enzyme activity in the hydrolysis of casein has been examined. Two sets of chemically distinct silica supports were used presenting terminal amino (S_APTES) or hydroxyl groups (S_TESPM-pHEMA). The percentage of immobilized protein was smaller in S_APTES (31–39%) than in S_TESPM-pHEMA (62–71%), but presented higher total and specific activity. Silicas with large pores (S₁₀₀₀, 130/1200 Å) presented higher specific activities relative to those with smaller pore sizes (S₃₀₀, 130/550 Å). The influence of glutaraldehyde concentration and the time of enzyme coupling to the S₁₀₀₀S_APTES supports was examined. The apparent K_m value for the S₁₀₀₀S_APTES immobilized enzyme is lower than the soluble one which may be explained by the partitioning effects of the substrate. No intraparticle diffusion limitations were observed for the immobilized enzyme and therefore the substrate diffusion does not influence the observable kinetics. Finally, the optimum pH, optimum temperature, thermal stability, operational stability, and storage stability of the immobilized and freely soluble enzymes were compared.     

Continuous sucrose hydrolysis by an immobilized whole yeast cell biocatalyst

An immobilized biocatalyst with invertase activity prepared by immobilization of whole yeast cells without use of any insoluble carrier was tested in tubular fixed-bed reactors from the point of view of possible application for continuous full-scale sucrose hydrolysis. At inlet sucrose concentration above 60% (w/w) and reaction temperature 60–70°C, total sucrose hydrolysis was achieved at a flow rate of 0.6–1.5 bed volumes per hour. At a flow rate about 10 bed volumes per hour, the conversion was still 0.5. The specific productivity of the biocatalyst was 3–25 h⁻¹; the productivity of the reactor was 1–9 kg l⁻¹ h⁻¹. The half-life of the biocatalyst invertase activity was 815 h at 70°C. The specific pressure drop over the biocatalyst bed was less than 23 kPa m⁻¹. The biocatalyst was proved to be fully capable of continuous sucrose hydrolysis in fixed-bed reactors.     

生物酶/γ-Al2O3小球催化氧化柴油脱硫性能研究

通过吸附法将生物酶负载在γ-Al₂O₃小球载体上,并对生物酶/γ-Al₂O₃及载体进行扫描电镜(SEM)、比表面积分析(BET)、傅里叶红外光谱(FT-IR)及圆二色谱(CD)表征。结果表明:生物酶被吸附在载体上。将制备的生物酶/γ-Al₂O₃催化真实柴油氧化脱硫,考察了反应温度、反应流速和酶溶液浓度对真实柴油脱硫效果的影响,并对脱硫效果进行定性及定量分析;进一步对脱硫工艺条件进行响应面设计优化,找出最优反应条件。实验结果显示:反应温度49℃、反应流速1.0 mL/min、酶溶液浓度15.5%(酶载量为28.13 g),得出的最优脱硫率为93.16%;最后考察了该固定化酶的重复使用性能,该催化剂使用7次活性无明显降低,表明该固定化酶催化氧化柴油脱硫效果显著,具有潜在的工艺应用价值。     

Immobilization of β-galactosidase from Kluyveromyces lactis on silica and agarose: comparison of different methods

The covalent immobilization of β-galactosidase from Kluyveromyces lactis (β-gal) on to two different porous carriers, CPC-silica and agarose, is reported. CPC-silica was silanizated and activated with glutaraldehyde. The activation of agarose via a cyanylating agent (CDAP) was optimized. Gel-bound protein and gel-bound activity were both measured directly, allowing the determination of apparent specific activities (S.A.). Higher amounts of β-gal were immobilized on the activated CPC-silica (maximum capacity, 23 mg ml⁻¹ of packed support) than on the CDAP-activated agarose. For the lower enzyme loading assayed (12.6 mg ml⁻¹ packed support), 100% of the enzyme was immobilized but only 34% of its activity was expressed. This inactivation during immobilization was confirmed by the S.A. values (22–29 EU mg⁻¹ for the CPC-derivatives and 80 EU mg⁻¹ for soluble β-gal). The K_app (3.4 mM) for the CDAP-derivative with ONPG as substrate was higher than the K_M value for soluble β-gal (2 mM). When the enzyme loading was increased five-fold, the K_app increased four-fold, to 13 mM. The V_app values for the CPC-derivatives were remarkably lower than the V_max for soluble β-galactosidase. CDAP-derivatives showed better thermal stabilities than CPC-derivatives but neither of them enhanced the stability of the soluble enzyme. When stored at 4°C, the activity of both derivatives remained stable for at least 2 months. Both derivatives displayed high percentages of lactose conversion (90%) in packed bed mini-reactors. Glucose production was 3.3-fold higher for the CPC-derivative than for the CDAP-derivative, as a consequence of the higher flow rates achieved.     

The F1-ATPase beta-subunit is the putative enterostatin receptor

It has been suggested that the F₁-ATPase β-subunit is the enterostatin receptor. We investigated the binding activity of the purified protein with a labeled antagonist, β-casomorphin_1–7, in the absence and presence of cold enterostatin. ¹²⁵I-β-casomorphin_1–7 weakly binds to the rat F₁-ATPase β-subunit. Binding was promoted by low concentrations of cold enterostatin but displaced by higher concentrations. To study the relationship between binding activity and feeding behavior, we examined the ability of a number of enterostatin analogs to affect β-casomorphin_1–7 binding to the F₁-ATPase β-subunit. Peptides that suppressed food intake promoted β-casomorphin_1–7 binding whereas peptides that stimulated food intake or did not affect the food intake displaced β-casomorphin_1–7 binding. Surface plasmon resonance measurements show that the β-subunit of F₁-ATPase binds immobilized enterostatin with a dissociation constant of 150 nM, where no binding could be detected for the assembled F₁-ATPase complex. Western blot analysis showed the F₁-ATPase β-subunit was present on plasma and mitochondrial membranes of rat liver and amygdala. The data provides evidence that the F₁-ATPase β-subunit is the enterostatin receptor and suggests that enterostatin and β-casomorphin_1–7 bind to distinct sites on the protein.     

Studies on neomycin production using immobilized cells of<Emphasis Type="Italic">S marinensis</Emphasis> NUV-5 in various reactor configurations: A technical note

Conclusion  Stirred tank, fluidized bed, and airlift reactors produced similar neomycin activity with immobilized cells. Packed bed reactor clearly under performed, probably because of insufficient aeration or mixing. Neomycin production using immobilized cells in fermentors requires good mixing and aeration.     

Properties of a glucose oxidase covalently immobilized on amorphous AlPO4 support

Glucose oxidase (GOD) was covalently immobilized on amorphous AlPO₄ as well as on an AlPO₄/clay mineral Sepiolite system. Immobilization of the enzyme was carried out through the -amino group of lysine residues through an aromatic Schiff's-base. Activation of the support was obtained after reaction of appropriate molecules with support surface –OH groups. The enzymatic activities of native, and different immobilized GOD systems and filtrates, were followed by the amount of liberated -gluconic acid obtained in the enzymatic β- -glucose oxidation with the aid of an automatic titrator. The kinetic properties of native and immobilized GOD were obtained for glucose concentrations in the range of physiological conditions and at different working conditions such as reaction temperature, reaction pH, and enzyme concentration.

The binding percentage of enzymes was in the 50–80% range, with residual and specific activities in the 65–80% and 90–150% ranges, respectively. No change in the pH optimum and only slight changes in the V_max and K_M kinetic parameters with respect to native GOD were observed, so that not only was little deactivation of enzyme obtained throughout the immobilization process but also that the stability of the covalently bound enzyme in the two supports appeared to have increased with respect to the soluble enzyme. GOD immobilization also increased its efficiency and operational stability in repeated uses on increasing the amount of immobilized enzyme.     

Some observations on the measurement of estradiol-17β in human plasma by radioimmunoassay

The use of specific and non-specific antisera for estradiol-17β (E₂17β) were compared in the radioimmunoassay of the steroid. The effects of various “blank” mateirials on the standard curve and on the accuracy of recovery of E₂17β added to plasma before and after chromatography on LH-20 Sephadex were examined. It was concluded that the use of the specific antiserum (anti-6-oxoE₂17β -6-(O-carboxymethyl)oxime-bovine serum albumin(antiE₂17β-6-BSA) was an improvement on the non-specific serum anti-E₂17β-17-hemisuccinyl-bovine serum albumin (antiE₂ 17β-17-BSA) following chromatography of extracts. However, although a precise result could be obtained with the anti-E₂17β-6-BSA without the Chromatographic step, recovery of E₂17β added to plasma was only possible if the step was included.

The cross-reactivity of estrone (E₁)with E₂17β using anti-E₂17β-17-BSA as defined by Abraham (J. Clin. Endocr. , 866 (1969) was examined under conditions of constant and of changing E₁:E₂17β ratio.     

Enzymatic Synthesis of Carbohydrate Derivatives Using β-Glycosidase of Sulfolobus Solfataricus

Enzymatic synthesis of different β-D-glycosides was obtained using as biocatalyst immobilized cells, crude homogenate, and homogeneous native and recombinat β-glycosidase activity of the thermophilic archaeon Sulfolobus solfataricus. In particular our investigation was concerned with the selectivity in the glycosylation of hydroxybenzyl alcohols, salicin, 1,2-propanediol, and more complex polyols as well as the use of immobilized cells for the synthesis of hexyl-β-D-glucoside. The aromatic glucosides obtained by enzyme-catalyzed transglucosylation were used for kinetic studies of purified Sulfolobus solfataricus enzyme in the hydrolysis reaction.     

Hydrolysis of particulate tributyrin in a fluidized lipase reactor.

Pancreatic lipase has been immobilized onto stainless steel beads by adsorption followed by crosslinking, and onto polyacrylamide by covalent bonding. The activities of the two types of immobilized enzyme toward the particulate substrate, tributyrin emulsion droplets, were determined experimentally, and rate constants based on Michaelis-Menten kinetics were calculated. The activity of the stainless steel-lipase was determined for various flow conditions and for various support sizes by the use of a differential fluidized bed recycle reactor. The rate constants calculated indicate that the experimental reaction rate is free from mass transfer influences, since the observed Michaelis constant does not vary with the fluidization velocity or with the support particle size. In addition, the Michaelis constant of the stainless steel-lipase was found to be equal to that of the free enzyme, suggesting that adsorption and subsequent crosslinking does not alter the enzyme-substrate affinity. The emulsion substrate mass transfer rates, calculated from the filtration theory, indicate that each substrate particle which contact the immobilized enzyme is hydrolyzed to a significant extent. The experimentally determined kinetic rate constants may be used directly to predict the size of integral fluidized bed reactors.     

Bioconversion of phospholipids by immobilized phospholipase A2

Phospholipase A₂ selectively hydrolyses the ester linkage at the sn-2 position of phospholipids forming lysocompounds. This bioconversion has importance in biotechnology since lysophospholipids are strong bioemulsifiers. The aim of the present work was to study the kinetic behaviour and properties of immobilized phospholipase A₂ from bee venom adsorbed into an ion exchange support. The enzyme had high affinity for CM-Sephadex^® support and the non-covalent interaction was optimum at pH 8. The activity of immobilized phospholipase A₂ was comparatively evaluated with the soluble enzyme using a phospholipid/Triton X-100 mixed micelle as assay system. The immobilized enzyme showed high retention activity and excellent stability under storage. The activity of the immobilized system remained almost constant after several cycles of hydrolysis. Immobilized phospholipase A₂ was less sensitive to pH changes compared to soluble form. The kinetic parameters obtained (V_max 883.4 μmol mg⁻¹ min⁻¹ and a K_m 12.9 mM for soluble form and V_max = 306 μmol mg⁻¹ min⁻¹ and a K_m = 3.9 for immobilized phospholipase A₂) were in agreement with the immobilization effect. The results obtained with CM-Sephadex^®-phospholipase A₂ system give a good framework for the development of a continuous phospholipid bioconversion process.     

Distribution of 17β-hydroxysteroid dehydrogenase gene expression and activity in rat and human tissues

The interconversion of estrone (E₁) and 17β-estradiol (E₂), androstenedione (4-ene-dione) and testosterone (T), as well as dehydroepiandrosterone and androst-5-ene-3β,17β-diol is catalyzed by 17β-hydroxysteroid dehydrogenase (17β-HSD). The enzyme 17β-HSD thus plays an essential role in the formation of all active androgens and estrogens in gonadal as well as extragonadal tissues. The present study investigates the tissue distribution of 17β-HSD activity in the male and female rat as well as in some human tissues and the distribution of 17β-HSD mRNA in some human tissues. Enzymatic activity was measured using ¹⁴C-labeled E₁, E₂, 4-ene-dione and T as substrates. Such enzymatic activity was demonstrated in all 17 rat tissues examined for both androgenic and estrogenic substrates. While the liver had the highestlevel of 17β-HSD activity, low but significant levels of E₂ as well as T formation were found in rat brain, heart, pancreas and thymus. The oxidative pathway (E₂→E₁, T→4-ene-dione) was favored over the reverse reaction in almost all rat tissues while in the human, almost equal rates were found in most of the 15 tissues examined. The widespread distribution of 17β-HSD in rat and human tissues clearly indicates the importance of this enzyme in peripheral sex steroid formation or intracrinology.     

Nitrogen fixation by immobilized Azotobacter chroococcum

A nitrogen-fixing bacterium, Azotobacter chroococcum, was immobilized in 2% agar gel. The optimum partial oxygen pressure, pO₂, of immobilized cells was 0.2 atm, wherea s that of native cells was 0.05 atm. When continual nitrogen fixation was performed under aerobic conditions, the nitrogenase activity of immobilized cells increased with increasing time. On the other hand, the activity of native cells decreased rapidly. Increase of nitrogenase activity was attributed to growth of the bacteria in the gel matrix. The production rate of total nitrogen compounds by the immobilized bacteria was also increased during the first 4 days. Nitrogen compounds produced by the immobilized cells were mainly amino acids such as γ-aminobutyrate, glutamate and arginine.     

Kinetic analysis of enzymic activities: Prediction of multiple forms of 17β-hydroxysteroid dehydrogenase

An overview of the application of kinetic methods to the delineation of 17β-hydroxysteroid dehydrogenase (17β-HSD) heterogeneity in mammalian tissues is presented. Early studies of 17β-HSD activity in animal liver and kidney subcellular fractions were suggestive of multiple forms of the enzyme. Subsequently, detailed characterization of activity in cytosol and subcellular membrane fractions of human placenta, with particular emphasis on inhibition kinetics, yielded evidence of two kinetically-differing forms of 17β-HSD in that organ. Gene cloning and transfection experiments have confirmed the identity of these two proteins as products of separate genes. 17β-HSD type 1 is a cytosolic enzyme highly specific for C₁₈ steroids such as 17β-estradiol (E₂) and estrone (E₁). 17β-HSD type 2 is a membrane bound enzyme reactive with testosterone (T) and androstenedione (A), as well as E₂ and E₁. Useful parameters for the detection of multiple forms of 17β-HSD appear to be the E₂/T activity ratio, NAD/NADP activity ratios, steroid inhibitor specificity and inhibition patterns over a wide range of putative inhibitor concentrations. Evaluation of these parameters for microsomes from samples of human breast tissue suggests the presence of 17β-HSD type 2. The 17β-HSD enzymology of human testis microsomes appears to differ from placenta. Analysis of human ovary indicates granulosa cells are particularly enriched in the type 1 enzyme with type 2-like activity in stroma/theca. Mouse ovary appears to contain forms of 17β-HSD which differ from 17β-HSD type 1 and type 2 in their kinetic properties.     

Hydrogen peroxide degradation by immobilized cells of alkaliphilic Bacillus halodurans

Whole cells of Bacillus halodurans LBK 261 were used as a source of catalase for degradation of hydrogen peroxide. The organism, B. halodurans grown at 55°C and pH 10, yielded a maximum catalase activity of 275 U g^-1 (wet wt.) cells. The catalase in the whole cells was active over a broad range of pH with a maximum at pH 8-9. The enzyme was optimally active at 55°C, but had low stability above 40°C. The whole cell biocatalyst exhibited a K_m of 6.6 mM for H₂O₂ and V_max of 707 mM H₂O₂ min^-1 g^-1 wet wt. cells, and showed saturation kinetics at 50 mM H₂O₂. The cells were entrapped in calcium alginate and used for H₂O₂ degradation at pH 9 in batch and continuous mode. In the batch process, the immobilized preparation containing 1.5 g (wet wt.) cells could be recycled at least four times for complete degradation of the peroxide in 50 mL solution at 25°C. An excess of immobilized biocatalyst could be used in a continuous stirred tank reactor for an average of 9 days at temperatures upto 55°C, and in a packed bed reactor (PBR) for 5 days before the beads started to deform.     

Immobilization of thermostable β-glucosidase from Sulfolobus shibatae by cross-linking with transglutaminase

Thermostable β-glucosidase from Sulfolobus shibatae was immobilized on silica gel modified or not modified with 3-aminopropyl-triethoxysilane using transglutaminase as a cross-linking factor. Obtained preparations had specific activity of 3883 U/g of the support, when measured at 70 °C using o-nitrophenyl β-d-galactopyranoside (GalβoNp) as substrate. The highest immobilization yield of the enzyme was achieved at pH 5.0 in reaction media. The most active preparations of immobilized β-glucosidase were obtained at a transglutaminase concentration of 40 mg/ml at 50 °C. The immobilization was almost completely terminated after 100 min of the reaction and prolonged time of this process did not cause considerable changes of the activity of the preparations. The immobilization did not influence considerably on optimum pH and temperature of GalβoNp hydrolysis catalyzed by the investigated enzyme (98 °C, pH 5.5). The broad substrate specifity and properties of the thermostable β-glucosidase from S. shibatae immobilized on silica-gel indicate its suitability for hydrolysis of lactose during whey processing.