Expression and secretion of barley α-amylase and A.niger glucoamylase inSaccharomyces cerevisiae

cDNAs of barley α-amylase andA. niger glucoamylase were cloned in oneE. coli-yeast shuttle plasmid resulting in the construction of expression secretion vector pMAG15. pMAG15 was transformed intoS. cerevisiae GRF18 by protoplast transformation. The barley α-amylase andA. niger glucoamylase were efficiently expressed under the control of promoter and terminator of yeast PGK gene and their own signal sequence. Over 99% of the enzyme activity expressed was secreted to the medium. The recombinant yeast strain, S.cerevisiae GRF18 (pMAG15), hydrolyzes 99% of the starch in YPS medium containing 15% starch in 47 h. The glucose produced can be used for the production of ethanol.     

双酶法水解辐照改性马铃薯淀粉动力学研究

为了解辐照改性马铃薯淀粉的酶解特性,用α-淀粉酶和糖化酶同时作用于马铃薯原淀粉和经400 kGy剂量辐照处理后淀粉,考察了pH值、酶解温度、α-淀粉酶用量、糖化酶用量对反应速率的影响.以米氏方程为基础,用Lineweaver-Burk法求解动力学参数.结果表明,辐照后马铃薯淀粉的酶解反应速率明显高于马铃薯原淀粉.在单一水解体系中,α-淀粉酶和糖化酶对辐照前后马铃薯淀粉的降解都遵循Michaelis-Menten方程,α-淀粉酶的Km分别为11.343 mg· mL-1和9.386 mg· mL-1,Vmax分别为0.406 mg（mL·min）-1和1.079 mg（mL·min）-1;糖化酶的Km分别为10.307 mg· mL-1和8.905 mg·mL-1,Vmax分别为0.338 mg（mL·min）-1和0.821mg（mL·min）-1;水解产物葡萄糖对反应体系具有竞争性抑制剂的作用,其抑制常数Ki分别为1.298 mg·mL-1和0.934 mg·mL-1.研究结果表明辐照有效提高了马铃薯淀粉的酶解反应活性.     

Repeated fermentation from raw starch using Saccharomyces cerevisiae displaying both glucoamylase and α-amylase

A diploid yeast strain displaying both α-amylase and glucoamylase was developed for repeated fermentation from raw starch. First, the construct of α-amylase was optimized for cell surface display, as there have been no reports of α-amylase-displaying yeast. The modified yeast displaying both glucoamylase and α-amylase produced 46.5 g/l of ethanol from 200 g/l of raw corn starch after 120 h of fermentation, and this was 1.5-fold higher when compared to native α-amylase-displaying yeast. Using the glucoamylase and modified α-amylase co-displaying diploid strain, we repeated fermentation from 100g/l of raw starch for 23 cycles without the loss of α-amylase or glucoamylase activity. The average ethanol productivity and yield during repeated fermentation were 1.61 g/l/h and 76.6% of the theoretical yield, respectively. This novel yeast may be useful for reducing the cost of bio-ethanol production and may be suitable for industrial-scale bio-ethanol production.     

Purification and Properties of α-Glucosidase and Glucoamylase from Lentinus edodes (Berk.) Sing.

An α-glucosidase and a glucoamylase have been isolated from fruit bodies of Lentinus edodes (Berk.) Sing., by a procedure including fractionation with ammonium sulfate, DEAE-cellulose column chromatography, and preparative gel electrofocusing. Both of them were homogeneous on gel electrofocusing and ultracentrifugation. The molecular weight of α-glucosidase and glucoamylase was 51,000 and 55,000, respectively. The α-glucosidase hydrolyzed maltose, maltotriose, phenyl α-maltoside, amylose, and soluble starch, but did not act on sucrose. The glucoamylase hydrolyzed maltose, maltotriose, phenyl α-maltoside, soluble starch, amylose, amylopectin, and glycogen, glucose being the sole product formed in the digests of these substrates. Both enzymes hydrolyzed phenyl a-maltoside into glucose and phenyl α-glucoside. The glucoamylase hydrolyzed soluble starch, amylose, amylopectin, and glycogen, converting them almost completely into glucose. It was found that β-glucose was liberated from amylose by the action of glucoamylase, while α-glucose was produced by the α-glucosidase.

Maltotriose was the main α-glucosyltransfer product formed from maltose by the α-glucosidase.     

Development of new α-amylases for raw starch hydrolysis

This paper describes the discovery of a new 4 domain α-amylase from Anoxybacillus contaminans which very efficiently hydrolyses raw starch granules. Compared to traditional starch liquefying α-amylases, this new 4 domain α-amylase contains a starch binding domain. The presence of this starch-binding domain enables the enzyme to efficiently hydrolyse starch at a temperature below the gelatinisation temperature. At a reaction temperature of 60°C and in combination with a glucoamylase from Aspergillusniger it was possible to liquefy 99% of the starch obtaining a DX value of 95%.

Furthermore, we describe how the current HFCS process can be turned into a low temperature simultaneous liquefaction and saccharification process by using this new 4 domain α-amylase in combination with a glucoamylase.     

Transient responses of <Emphasis Type="Italic">Wickerhamia</Emphasis> sp. yeast continuous cultures to qualitative changes in carbon source supply: induction and catabolite repression of α-amylase synthesis

The purpose of this study was to evaluate the inductive effect of starch and maltose, and the repressive/inhibitory effect of glucose, on amy-1 gene expression and α-amylase production by Wickerhamia sp., using continuous culture under transient-state conditions at a dilution rate (D) of 0.083 h^?1. Induction and repression kinetics of α-amylase were studied by changing the medium feed from glucose to maltose or starch in the induction experiments and vice versa in the repression experiments. Expression levels of amy-1 gene were measured by RT-qPCR. Results showed that starch was a more efficient inducer of α-amylase synthesis compared to maltose, with maximum accumulation rate constants of 0.424 and 0.191 h^?1, respectively. In contrast, α-amylase synthesis in starch and maltose cultures was partially repressed by glucose as indicated by a specific activity close to basal levels and a decay constant rate (??0.065 and ??0.069 h^?1, respectively) higher than ??D. A linear dependence of the specific rate of α-amylase production on mRNA relative abundance of amy-1 gene was observed. An inhibitory effect of glucose was not observed even at a concentration of 30 g L^?1. In conclusion, the transient continuous culture is a useful tool to determine the qualitative and quantitative effects of maltose and starch on α-amylase induction and of glucose on enzyme repression, as well as to obtain a detailed understanding of the dynamic behavior of the yeast culture. Furthermore, results showed that amylaceous substrates can be very effective carbon sources for the production of α-amylase without being inhibited by glucose.     

Cybernetic modelling of growth and ethanol production in a recombinant Saccharomyces cerevisiae strain secreting a bifunctional fusion protein

Recombinant Saccharomyces cerevisiae YPB-G strain secreting a fusion protein displaying both BsAAase/GAase activities was grown in 1.5 l YPS media containing single (starch) and mixed carbon sources (glucose+starch) using a 2.5 l New Brunswick BiofloIII fermenter. Ethanol and biomass formation, starch utilisation, secretion of the amylolytic enzymes (-amylase and glucoamylase), accumulation of reducing sugars and glucose were followed during the fermentation of YPB-G under different conditions. Moreover, a model has been developed for the growth of recombinant yeast on substitutable substrates using cybernetic framework principles and incorporating product formation. In the present work, both the biphasic and the diauxic growth patterns observed experimentally in batch culture of recombinant yeast cells were simulated successfully by modifying the cybernetic framework to include ethanol formation and the degradation kinetics of starch which is not directly utilised by yeast. The model can further be expanded to fed-batch systems.     

Measurement of α-amylase and glucoamylase activities produced during fermentation

A method for the automatic measurement of α-amylase and glucoamylase activities during fermentation has been developed. Soluble starch dyed with Remazol Brilliant Orange was used as the substrate for α-amylase and 4-nitrophenyl α-d-glucopyranoside for glucoamylase. The same automatic analysis system could be used for both of these enzymes because the reaction products were measured at the same wavelength. Simultaneous pick-up of enzyme and the respective substrate was enabled by using two samplers. The presence of α-amylase did not interfere with the glucoamylase determination. Absolute values for α-amylase activity were obtained using a mathematical correction. Monitoring of these enzymes was accomplished during microbial fermentation.     

Hydrolysis of wheat flour with amylase preparations and individual enzymes

Rheological properties of wheat flour were studied in the course of its processing (cooking and saccharification). The effects of commercial α-amylase preparations were compared during flour preparation. Test preparations were equally potent in decreasing the viscosity of an all-grain batch. Homogenous glucoamylases isolated from Aspergillus differed in the presence or absence of the starch-binding domain. The starch-binding domain provided for the high activity of glucoamylase on insoluble starch, but gave no advantages in saccharification of pretreated wheat flour.     

Production and Characteristics of Raw-Potato-Starch-Digesting α-Amylase from Bacillus subtilis 65

A newly isolated bacterium, identified as Bacillus subtilis 65, was found to produce raw-starch-digesting α-amylase. The electrophoretically homogeneous preparation of enzyme (molecular weight, 68,000) digested and solubilized raw corn starch to glucose and maltose with small amounts of maltooligosaccharides ranging from maltotriose to maltoheptaose. This enzyme was different from other amylases and could digest raw potato starch almost as fast as it could corn starch, but it showed no adsorbability onto any kind of raw starch at any pH. The mixed preparation with Endomycopsis glucoamylase synergistically digested raw potato starch to glucose at 30°C. The raw-potato-starch-digesting α-amylase showed strong digestibility to small substrates, which hydrolyzed maltotriose to maltose and glucose, and hydrolyzed p-nitrophenyl maltoside to p-nitrophenol and maltose, which is different from the capability of bacterial liquefying α-amylase.     

Purification and characterization of an extracellular glucoamylase from the yeastCandida tsukubaensis CBS 6389

The starch-degrading yeastCandida tsukubaensis CBS 6389 secreted amylase at high activity when grown in a medium containing soluble starch. The extracellular α-amylase activity was very low. The major amylase component was purified by DEAE-Sephadex A-50 chromatography and Ultrogel AcA 44 gel filtration and characterized as a glucoamylase. The enzyme proved to be a glycoprotein with a molecular weight of 56000. The glucoamylase had a temperature optimum at 55°C and displayed highest activity in a pH range of 2.4–4.8. Acarbose strongly inhibited the purified glucoamylase. Debranching activity was present as demonstrated by the release of glucose from pullulan.     

Fast and reliable method for simultaneous zymographic detection of glucoamylase and α-amylase in fungal fermentation

Detection of α-amylase and glucoamylase in crude fermentation extracts using a single native electrophoresis gel and zymogram is described in this article. Proteins were printed on substrate gel and simultaneously onto a membrane in a three-sandwich gel. α-Amylase was detected on the substrate gel with copolymerized β-limit dextrins and iodine reagent. Glucoamylases were detected on the membrane using a coupled assay for glucose detection. Both amylases were detected in native gel using starch and iodine reagent. The described technique can be a helpful tool for monitoring and control of fermentation processes because fungal amylase producers almost always synthesize both amylases.     

Expression and secretion of barley α-amylase and A.niger glucoamylase in Saccharomyces cerevisiae

cDNAs of barley α-amylase andA. niger glucoamylase were cloned in oneE. coli-yeast shuttle plasmid resulting in the construction of expression secretion vector pMAG15. pMAG15 was transformed intoS. cerevisiae GRF18 by protoplast transformation. The barley α-amylase andA. niger glucoamylase were efficiently expressed under the control of promoter and terminator of yeast PGK gene and their own signal sequence. Over 99% of the enzyme activity expressed was secreted to the medium. The recombinant yeast strain, S.cerevisiae GRF18 (pMAG15), hydrolyzes 99% of the starch in YPS medium containing 15% starch in 47 h. The glucose produced can be used for the production of ethanol. Project supported by the Guangdong Natural Science Foundation.     

Corn porous starch: preparation, characterization and adsorption property

This study was carried out to develop a new type of modified starch based on α-amylase and glucoamylase. The structural and chemical characteristics of the porous starch were determined by Fourier-transform infrared (FTIR) spectroscopy, scanning electron microscopy (SEM), X-ray diffraction (XRD) and differential scanning calorimetry (DSC). The potential application of the porous starch as an adsorbent was evaluated using methyl violet as an adsorbed model. The adsorption capacity was optimized by investigating the reaction factors, including the mass ratio of α-amylase to glucoamylase (m_α-amylase/m_glucoamylase), the mass ratio of total amount of enzymes to starch (m_enzyme/m_St), the ratio of liquid volume to starch mass (VH₂O/mSt), pH value of the reaction solution, enzymatic reaction temperature, and enzymatic reaction time. The hydrolysis ratio of each sample was also determined to investigate the effect of different reaction conditions on the hydrolysis degree. The results suggest that the porous starch has a more excellent adsorption capacity than the native starch, and may be expected to have wide potential applications in many fields.     

Application of ultrafiltration for enzyme retention during continuous enzymatic reaction

In most enzymatic reactions, batch or continuous, separation of the enzyme for reuse is difficult if not impossible. A process will be presented in which an Ultrafiltration membrane serves to separate the reaction products from the enzyme and the substrate. In this manner the enzyme may be retained and re-used. Furthermore, under these conditions, the enzyme need only be present in catalytic amounts regardless of the amount of product produced. Under proper operating conditions and proper ultrafiltration membrane selection, a pure solution of α-amylase from Bacillus subtilis may be retained with no loss in enzyme activity over a test period of 30 hr after steadystate has been achieved. In the presence of substrate, the membrane support and ultrafiltration cell serve as the reaction vessel for the hydrolysis of starch. The substrate is continuously pumped into the cell under constant ultrafiltration pressure. The di-, oligo-, and polysaccharides formed from the enzyme reaction then either pass through the membrane as products or are retained. The molecular weight distribution of the products is dependent on the nominal molecular weight cut-off of the membrane, absolute ultrafiltration pressure, enzyme-to-substrate ratio, temperature, and residence time of the substrate in the reactor. In addition to the partial hydrolysis of starch by α-amylase, some preliminary findings on the complete hydrolysis of starch by glucoamylase will also be presented. In these latter studies, the substrate may be completely hydrolyzed to glucose units.     

Simultaneous and Enhanced Production of Thermostable Amylases and Ethanol from Starch by Cocultures of Clostridium thermosulfurogenes and Clostridium thermohydrosulfuricum

Clostridium thermohydrosulfuricum and Clostridium thermosulfurogenes produced ethanol and amylases with different components as primary metabolites of starch fermentation. Starch fermentation parameters were compared in mono- and cocultures of these two thermoanaerobes to show that the fermentation was dramatically improved as a consequence of coordinate action of amylolytic enzymes and synergistic metabolic interactions between the two species. Under given monoculture fermentation conditions, neither species completely degraded starch during the time course of the study, whereas in coculture, starch was completely degraded. In monoculture starch fermentation, C. thermohydrosulfuricum produced lower levels of pullulanase and glucoamylase, whereas C. thermosulfurogenes produced lower levels of β-amylase and glucoamylase. In coculture fermentation, improvement of starch metabolism by each species was noted in terms of increased amounts and rates of increased starch consumption, amylase production, and ethanol formation. The single-step coculture fermentation completely degraded 2.5% starch in 30 h at 60°C and produced 9 U of β-amylase per ml, 1.3 U of pullulanase per ml, 0.3 U of glucoamylase per ml, and >120 mM ethanol with a yield of 1.7 mol/mol of glucose in starch. The potential industrial applications of the coculture fermentation and the physiological basis for the interspecies metabolic interactions are discussed.     

Multi-objective optimization of bioethanol production during cold enzyme starch hydrolysis in very high gravity cassava mash

Cold enzymatic hydrolysis conditions for bioethanol production were optimized using multi-objective optimization. Response surface methodology was used to optimize the effects of α-amylase, glucoamylase, liquefaction temperature and liquefaction time on S. cerevisiae biomass, ethanol concentration and starch utilization ratio. The optimum hydrolysis conditions were: 224 IU/g_starch α-amylase, 694 IU/g_starch glucoamylase, 77 °C and 104 min for biomass; 264 IU/g_starch α-amylase, 392 IU/g_starch glucoamylase, 60 °C and 85 min for ethanol concentration; 214 IU/g_starch α-amylase, 398 IU/g_starch glucoamylase, 79 °C and 117 min for starch utilization ratio. The hydrolysis conditions were subsequently evaluated by multi-objectives optimization utilizing the weighted coefficient methods. The Pareto solutions for biomass (3.655-4.380 × 10⁸ cells/ml), ethanol concentration (15.96-18.25 wt.%) and starch utilization ratio (92.50-94.64%) were obtained. The optimized conditions were shown to be feasible and reliable through verification tests. This kind of multi-objective optimization is of potential importance in industrial bioethanol production.     

Polysaccharide-hydrolyzing enzymes in the GenusBacillus

The production of α-amylase, glucoamylase, C_x- and C₁-cellulase, lichenase, xylanase and mannanase was followed in 118 strains of 25 species of the genusBacillus using specific substrates obtained by crosslinking of polysaccharides with 2-chloromethyloxiran. The α-amylase production was also followed using a chromolytic substrate.     

Amylases of the thermophilic fungusThermomyces lanuginosus: Their purification,properties, action on starch and response to heat

A thermophilic fungus Thermomyces lanuginous strain IISc 91, secreted one form each of α-amylase and glucoamylase during growth. Both enzymes were purified to homogeneity by ion-exchange and gel-filtration chromatography and obtained in mg quantities. α-Amylase was considered to be a dimeric protein of ∼ 42 kDa and contained 5% (by mass) carbohydrate. It was maximally active at pH 5.6 and at 65°C. It had an activation energy of 44 kJ mol^-1. The apparent K_m for soluble starch was 2.5 mg ml^-1. The enzyme produced exceptionally high levels of maltose from raw potato starch. At 50°C, the enzyme was stable for > 7h. At 65°C, α-amylase was nearly 8-times more stable in the presence of calcium. Addition of calcium increaed the melting temperature of α-amylase from 66°C to 73°C. Upon incubation at 94°C, α-amylase was progressively and irreversibly inactivated, and converted into an inactive 72 kDa trimeric species. Glucoamylase was a monomeric glycoprotein of ∼ 45 kDa with a carbohydrate content of 11% (by mass). It effected up to 76% conversion of starch in 24 h producing glucose as the sole product. Its apparent K_m for soluble starch was 0.04 mg ml^-1 and V_max was 660 Mmol glucose min^-1 mg protein^-1. It also hydrolyzed maltose. Its activity on maltooligosaccharides increased with the chain length of the substrates. Glucoamylase was stable at 60°C for over 7h. Its activation energy was 61 kJ mol^-1 Glucoamylase did not show synergistic effect with α-amylase. The properties of α-amylase and glucoamylase of Thermomyces lanuginosus strain IISc 91 suggest their usefulness in the commercial production of maltose and glucose syrups.     

α- and β-Amylases in seed germination

During the first 24 h of germination of wheat seeds, starch is hydrolysed by free β-amylase. In the next 24 h, some amount of inactive form of β-amylase is converted into active form and this together with α-amylase synthesizedde novo brings about the hydrolysis of starch. The amount of α-amylase is greater in seeds with embryo intact than with embryo excised after 24 h hydration. However, at later stages of seed germination α-amylase becomes predominant and the activity of β-amylase steadily diminishes.