α淀粉酶和糖化酶在酿酒酵母中的表达和分泌

将地衣芽孢杆菌α-淀粉酶基因及黑曲霉糖化酶cDNA重组进大肠杆菌-酵母穿梭质粒,转化酿酒酵母,构建能分解淀粉的酵母工程菌。酶活力测定和酶学性质分析的结果显示:在酵母MF-α1因子及磷酸甘油酸激酶基因的启动子和终止信号的调控下,α-淀粉酶和糖化酶基因在酵母中获得高表达并向胞外分泌这两种酶。构建的酵母工程菌在含10％淀粉的培养基中6天内能水解97％的淀粉,重组质粒能在酵母中较稳定地存在。     

The relationship of structure of glucoamylase and glucose oxidase to antigenicity

Glucoamylase and glucose oxidase fromAspergillus niger have been purified to homogeneity by chromatography on DEAE-cellulose and the purified enzymes have been used to investigate structural and antigenicity relationships. In structure, glucoamylase and glucose oxidase are glycoproteins containing 14% and 16% carbohydrate. Earlier methylation and reductive -elimination results have shown that glucoamylase has an unusual arrangement of carbohydrate residues, with 20 single mannose units and 25 di-, tri-, or tetrasaccharide chains of mannose, glucose, and galactose, all attached O-glycosidically to serine and threonine residues of the protein moiety. The antigenicity of the glucoamylase has now been found to reside predominantly in the types and arrangement of the carbohydrate chains. Glucose oxidase contains mannose, galactose, and glucosamine in the N-acetyl form in the native enzyme, but the complete structure of the carbohydrate chains has not yet been determined. The antigenicity of this enzyme does not reside in the carbohydrate units, but rather in the polypeptide chains of the two subunits of the enzyme. Glucose oxidase can be dissociated into subunits by mercaptoethanol and sodium dodecyl sulfate treatment, while glucoamylase cannot be dissociated, but undergoes only an unfolding of the polypeptide chain under these conditions. The subunits of glucose oxidase do not react with the anti-glucose oxidase antibodies, but the unfolded molecule and peptide fragments produced from glucoamylase by cyanogen bromide cleavage do react with antiglucoamylase antibodies.     

Thyroxine-stimulated synthesis of microvillus membrane glycoproteins during culture of chick embryonic duodenum

The effect of thyroxine on biosynthesis of microvillus membrane glycoproteins has been investigated in organ culture of 18-day-old chick embryonic duodenum. Explants incorporate [³H]leucine and [³H]glucosamine continuously, and overall incorporation is enhanced by 10 nM thyroxine during 48 h of labeling; this increase in radioactivity is associated with vesicles released from the microvilli. Light microscope autoradiography, pulse labeling of brush border fragments, and pulse chase experiments reveal that [³H]glucosamine is incorporated into brush border at an increasing rate during culture, and that newly synthesized glycoproteins are discharged into the medium along with brush border enzymes (alkaline phosphatase and maltase). These results suggest that thyroxine stimulates biosynthesis of microvillus membrane glycoproteins, in addition to stimulating vesiculation of the membrane. Sodium dodecyl sulfate-polyacrylamide gel electrophoresis of ³H-labeled vesicles and brush border fragments show that [³H]leucine and [³H]glucosamine are incorporated into proteins of high molecular weight. Two protein bands are identified as alkaline phosphatase and maltase. Thyroxine stimulates glycosylation of these enzymes, but does not change protein patterns. Radioactivity assay of alkaline phosphatase- and maltase-active gel slices suggests that thyroxine stimulation of these enzyme activities during culture is not correlated with de novo synthesis of these proteins.     

Investigation of the binding mechanism of glucoamylase to alkylamine derivatives of titanium(IV)-activated porous inorganic supports

Glucoamylase (exo-1,4-α-d-glucosidase, EC 3.2.1.3) has been coupled to several porous silica matrices by a new covalent process using alkylamine derivatives of titanium(IV)-activated supports. In order to investigate the interaction of the titanium element with the silanol groups of the inorganic matrices, activation was performed at different times, using titanium(IV) chloride, either pure or as a 15% w/v solution, in 15% w/v hydrochloric acid at 25, 45 and 80°C, followed by washing with sodium acetate buffer (0.02m, pH 4.5) or chloroform. Using pure TiCl₄, the highest activities of all preparations were obtained at 80°C and with acetate buffer washing, resulting from a higher content of titanium coating of the carrier. When activation was performed in aqueous TiCl₄ solution, followed by a drying step, the highest activity was obtained with preparations washed with chloroform, with or without amination. When reacting pure TiCl₄ with controlled pore glass (CPG) and with porous silica (Spherosil), colour formation was observed after reaction of glutaraldehyde with the aminated support. This did not happen when Celite was used as the support. As a criterion for comparison of the different immobilized enzyme preparations, the concept of an ‘instability factor’, which measures the percentage of immobilized enzyme activity due to release of enzyme into solution, is introduced. Instability factors of immobilized enzyme preparations on Celite were always higher than those obtained with the other matrices, confirming that there was no covalent coupling of the enzyme to Celite. However, when the activation was performed with aqueous TiCl₄ solution with drying, Schiff's base formation was observed in all preparations and very stable immobilized enzyme preparations were obtained. The results of the activation of controlled pore glass and porous silica with pure titanium(IV) chloride suggest the existence of a true reaction between the titanium element and the silanol groups of these carriers by formation of a bridge, Si-O-Ti, while with the titanium(IV) chloride solution in hydrochloric acid, a coating of hydrous titanium(IV) oxide is obtained.     

Modeling protein recognition of carbohydrates

We have a limited understanding of the details of molecular recognition of carbohydrates by proteins, which is critical to a multitude of biological processes. Furthermore, carbohydrate-modifying proteins such as glycosyl hydrolases and phosphorylases are of growing importance as potential drug targets. Interactions between proteins and carbohydrates have complex thermodynamics, and in general the specific positioning of only a few hydroxyl groups determines their binding affinities. A thorough understanding of both carbohydrate and protein structures is thus essential to predict these interactions. An atomic-level view of carbohydrate recognition through structures of carbohydrate-active enzymes complexed with transition-state inhibitors reveals some of the distinctive molecular features unique to protein-carbohydrate complexes. However, the inherent flexibility of carbohydrates and their often water-mediated hydrogen bonding to proteins makes simulation of their complexes difficult. Nonetheless, recent developments such as the parameterization of specific force fields and docking scoring functions have greatly improved our ability to predict protein-carbohydrate interactions. We review protein-carbohydrate complexes having defined molecular requirements for specific carbohydrate recognition by proteins, providing an overview of the different computational techniques available to model them.     

Ethanol production and fermentation characteristics of recombinant saccharomyces cerevisiae strains grown on starch

The production of ethanol from starch has been investigated in three genetically modified Saccharomyces cerevisiae strains (YPG/AB, YPG/MM, and YPB-G). Two of the three strains produce the Aspergillus awamori glucoamylase together with either the Bacillus subtilis (YPG/AB) or the mouse (YPG/MM) α-amylase as separately secreted polypeptides. YPB-G, on the other hand, secretes a bifunctional fusion protein that contains both the B. subtilis α-amylase and the A. awamori glucoamylase activities. Substrate utilization, biomass growth, and ethanol production were all studied in both starch- and glucose-containing media. Much higher growth rates were found when any of the three strains were grown on glucose. YPG/AB showed the most efficient utilization of starch for ethanol production with the lowest levels of reducing sugars accumulating in the medium. The superior performance of YPG/AB as compared to YPB-G was found to correlate with its higher level of α-amylase activity. The ethanol production levels of YPG/AB in starch- and glucose-containing media were found to be comparable. YPB-G, which secretes the bifunctional fusion protein, could produce ethanol in media with starch concentrations above 100 g l⁻¹ while YPG/MM did not produce ethanol from starch because of its negligible secretion of glucoamylase.     

Immobilization of enzymes on crosslinked gelatin particles activated with various forms and complexes of titanium(IV) species

A number of methods of activating the surface of glutaraldehyde crosslinked gelatin beads with titanium(IV) compounds, for subsequent enzyme coupling, have been investigated. Glucoamylase (exo-1,4-α-d-glucosidase, EC 3.2.1.3) was so immobilized using titanium(IV)-urea, -acrylamide, -citric acid and -lactose complexes; however, immobilized enzyme preparations with low activities were obtained (0.36–1.28 U g^?1). Activation with uncomplexed titanium(IV) chloride, however, of both moist and freeze-dried crosslinked gelatin particles resulted in highly active immobilized glucoamylase preparations (1.74–26.6 U g^?1). Dual immobilized enzyme conjugates of glucoamylase and invertase (β-d-fructofuranosidase, EC 3.2.1.26) were also prepared using this method. Invertase was served on the entrapped enzyme while glucoamylase was coupled on the surface of titanium(IV)-activated gelatin pre-entrapped invertase particles. A dual gelatin coupled glucoamylase/gelatin entrapped glucoamylase was prepared (3.8 U g^?1) and ～72.5% of the total combined activity was due to the surface bound enzyme.     

A simple kinetic model for the hydrolysis of α-d-glucans using glucoamylase immobilized on titanium (IV) activated porous silica

A simple kinetic model which describes the hydrolysis of α-d-glucans by immobilized glucoamylase (exo-1,4-d-glucosidase, EC 3.2.1.3) is reported. The hydrolysis of starch, amylose, amylopectin, maltose and 40DE starch hydrolysates using glucoamylase immobilized on alkylamine derivatives of titanium(IV) activated porous silica are described by a kinetic model based on Langmuir-Hinshelwood kinetics. This model involves enzyme kinetics with or without product inhibition and reverse reactions as well as mass transfer and diffusion effects in immobilized enzyme reactors. The results of other authors are also interpreted by the model developed in this article.     

Characterization of nimbidiol as a potent intestinal disaccharidase and glucoamylase inhibitor present in Azadirachta indica (neem) useful for the treatment of diabetes

Azadirachta indica, used in antidiabetic herbal drugs, was reported to contain α-glucosidase inhibitor. Bioassay guided purification characterized the inhibitor as nimbidiol (a diterpenoid), present in root and stem-bark of the tree. Nimbidiol inhibited intestinal (mammalian) maltase-glucoamylase, sucrase-isomaltase, lactase, trehalase and fungal α-glucosidases. Nimbidiol showed a mixed competitive inhibition on intestinal carbohydrases. IC₅₀, Ki and Ki′ (µM) were 1.35 ± 0.12, 0.08 ± 0.01, 0.25 ± 0.11, respectively, for maltase-glucoamylase (maltotetraose as substrate). Nimbidiol was more potent inhibitor of isomaltase (IC₅₀ 0.85 ± 0.035 µM), lactase (IC₅₀ 20 ± 1.33 µM) and trehalase (IC₅₀ 30 ± 1.75 µM) than acarbose, voglibose, salacinol, kotalanol and mangiferin. Ki and Ki′ values (µM) for intestinal sucrase were 0.7 ± 0.12 and 1.44 ± 0.65, respectively. Development of nimbidiol as an antidiabetic drug appears to be promising because of broad inhibition spectrum of intestinal glucosidases and easy synthesis of the molecule.     

Purification of amyloglucosidase

Amyloglucosidase (glucoamylase; EC 3.2.1.3) has been purified from the culture filtrates of Aspergillus candidus Link var. aureus using hydrophobic interaction chromatography and DEAE-cellulose treatment. The enzyme thus obtained has a specific activity of 329 units/mg protein with the overall recoveries between 70 and 75%. The process appears to be of industrial promise.