Effect of gamma-ray irradiation on alcohol production from corn

Cracked corn was irradiated with gamma rays at 0-100 Mrad and the effects of the irradiation on sugar yield, susceptibility to enzymatic hydrolysis of starch, yeast growth, and alcohol production were studied. Gamma irradiation at 50 Mrad or greater produced a considerable amount of reducing sugar but little glucose. At lower dosages, gamma irradiation significantly increased the susceptibility of corn starch to enzymatic hydrolysis, but dosages of 50 Mrad or greater decomposed the starch molecules as indicated by the reduction in iodine uptake. About 12.5% reducing sugar was produced by amylase treatment of uncooked, irradiated corn. This amount exceeded the level of sugar produced from cooked (gelatinized) corn by the same enzyme treatment. The yeast numbers in submerged cultivation were lower on a corn substrate that was irradiated at 50 Mrad or greater compared to that on an unirradiated control. About the same level of alcohol was produced on uncooked, irradiated (10(5)-10(6) rad) corn as from cooked (121 degrees C for 30 min) corn. Therefore, the conventional cooking process for gelatinization of starch prior to its saccharification can be eliminated by irradiation. Irradiation also eliminated the necessity of sterilization of the medium and reduced the viscosity of high levels of substrate in the fermentation broth.     

Production and Characteristics of Raw Starch-Digesting Glucoamylase O from a Protease-Negative, Glycosidase-Negative Aspergillus awamori var. kawachi Mutant

Production of a raw starch-digesting glucoamylase O (GA O) by protease-negative, glycosidase-negative mutant strain HF-15 of Aspergillus awamori var. kawachi was undertaken under submerged culture conditions. The purified GA O was electrophoretically homogeneous and similar to the parent glucoamylase I (GA I) in the hydrolysis curves toward gelatinized potato starch, raw starch, and glycogen and in its thermostability and pH stability, but it was different in molecular weight and carbohydrate content (250,000 and 24.3% for GA O, 90,000 and ca. 7% for GA I, respectively). The chitin-bound GA O hydrolyzed raw starch but the chitin-bound GA I failed to digest raw starch because chitin was adsorbed at the raw starch affinity site of the GA I molecule. The removal of the raw starch affinity site of GA O with subtilisin led to the formation of a modified GA O (molecular weight, 170,000), which hydrolyzed glycogen 100%, similar to GA O and GA I, and was adsorbed onto chitin and fungal cell wall but not onto raw starch, Avicel, or chitosan. The modified GA I (molecular weight, 83,000) derived by treatment with substilisin hydrolyzed glycogen up to only 80% and failed to be adsorbed onto any of the above polysaccharides. The N-bromosuccinimide-oxidized GA O lost its activity toward gelatinized and raw starches, but the abilities to be adsorbed onto raw starch and chitin were preserved. It was thus suggested that both the raw starch affinity site essential for raw starch digestion and the chitin-binding site specific for the binding with chitin in the cell wall could be different from the active site, located in the three respective positions in the GA O molecule.     

Purification and properties of a novel raw starch degrading-cyclodextrin glycosyltransferase from Klebsiella pneumoniae AS- 22

A novel raw starch degrading α-cyclodextrin glycosyltransferase (CGTase; E.C. 2.4.1.19), produced by Klebsiella pneumoniae AS-22, was purified to homogeneity by ultrafiltration, affinity and gel filtration chromatography. The specific cyclization activity of the pure enzyme preparation was 523 U/mg of protein. No hydrolysis activity was detected when soluble starch was used as the substrate. The molecular weight of the pure protein was estimated to be 75 kDa with SDS-PAGE and gel filtration. The isoelectric point of the pure enzyme was 7.3. The enzyme was most active in the pH range 5.5–9.0 whereas it was most stable in the pH range 6–9. The CGTase was most active in the temperature range 35–50°C. This CGTase is inherently temperature labile and rapidly loses activity above 30°C. However, presence of soluble starch and calcium chloride improved the temperature stability of the enzyme up to 40°C. In presence of 30% (v/v) glycerol, this enzyme was almost 100% stable at 30°C for a month. The K_m and k_cat values for the pure enzyme were 1.35 mg ml⁻¹ and 249 μM mg⁻¹ min⁻¹, respectively, with soluble starch as the substrate. The enzyme predominantly produced α-cyclodextrin without addition of any complexing agents. The conditions employed for maximum α-cyclodextrin production were 100 g l⁻¹ gelatinized soluble starch or 125 g l⁻¹ raw wheat starch at an enzyme concentration of 10 U g⁻¹ of starch. The α:β:γ-cyclodextrins were produced in the ratios of 81:12:7 and 89:9:2 from gelatinized soluble starch and raw wheat starch, respectively.     

Dependence of alcohol binding from aqueous dispersions on physicochemical properties of starch

Binding of alcohols from aqueous dispersions of native cornstarches differing in amylose content was studied by means of capillary gas chromatography. The efficiency of this process was compared with that of binding to gelatinized starches. Studies of native and gelatinized starches showed that the amount of bound substances depended linearly on their initial concentration. Binding of alcohols did not differ in native and gelatinized normal starch and high amylose starch. The efficiency of binding increased with the length of the alkyl substituent. It should be emphasized that the highest efficiency of binding was observed with native starch. Native amylopectin starch was less potent than gelatinized starch in binding hexanol. The degree of alcohol binding was much lower in cryotextures of gelatinized starch.     

Dependence of alcohol binding from aqueous dispersions on physicochemical properties of starch

Binding of alcohols from aqueous dispersions of native cornstarches differing in amylose content was studied by means of capillary gas chromatography. The efficiency of this process was compared with that of binding to gelatinized starches. Study of native and gelatinized starches showed that the amount of bound substances depends linearly on their initial concentration. Binding of alcohols did not differ in native and gelatinized normal starch and high amylose starch. The efficiency of binding increased with an increase in the length of the alkyl substituent. It should be emphasized that the efficiency of binding was highest in native starch. Native amylopectin starch was less potent than gelatinized starch in binding hexanol. The degree of alcohol binding was much lower in cryotextures of gelatinized starch.     

响应面法优化米糠淀粉酶法水解工艺

以米糠为原料,对米糠淀粉酶法水解生产葡萄糖的液化工艺进行研究和优化,来提高葡萄糖收率。在单因素试验的基础上,用响应面法对液化工艺进行优化。结果表明,液化工艺的最佳条件为酶用量0.11%、醪浓度25%、pH=6.0、温度88℃,在此条件下得到的液化葡萄糖值(即DX值)平均值为6.54%。然后对此液化液进行糖化,最终得到的糖化液DX值为97.07%。     

Continuous butanol fermentation and feed starch retrogradation: butanol fermentation sustainability using Clostridium beijerinckii BA101

Use of starch solution as feed for butanol bioconversion processes employing Clostridium beijerinckii BA101 may have added economic advantage over the use of glucose. Acetone butanol ethanol (ABE) was produced from 30 gL(-1) starch solution using a continuous process. The bioreactor was fed at a dilution rate of 0.02 h(-1) and starch solution/feed volume (3 L) was replaced every 72 h. The continuous reactor fed with cornstarch solution (feed temperature 19 degrees C) produced approximately 6.0 gL(-1) total ABE. Increasing the feed storage temperature to 37 degrees C improved ABE production to 7.2 gL(-1) suggesting that retrogradation was occurring more rapidly at 19 degrees C. In both these cases the fermentation drifted toward acid production after approximately 260 h, consistent with the retrogradation of starch overtime. The use of soluble starch, which is less prone to retrogradation, resulted in the production of 9.9 gL(-1) ABE at 37 degrees C feed storage temperature, as compared to 7.2 gL(-1) ABE when cornstarch was used. It should be noted that gelatinized starch retrogradation takes place after sterilization and prior to use of the feed medium, and does not occur during long-term storage of the raw corn material in the months leading up to processing. The degree of hydrolysis of gelatinized starch decreased from 68.8 to 56.2% in 3 days when stored at 37 degrees C. Soluble starch which does not retrograde demonstrated no change in the degree of hydrolysis.     

σ-Amylase inactivation during corn starch hydrolysis process

The effects of operating conditions on the enzymatic hydrolysis of corn starch were investigated. A commercial α-amylase produced by Bacillus sp. was used for the hydrolysis experiments. The degree of starch hydrolysis (%) and residual α-amylase activity (%) was investigated versus process variables, including pH, temperature, viscosity, impeller speed, processing time and some materials added such as hydrolysate, maltose, glucose, ethanol and CaCl₂ using a stirred batch reactor. The mathematical models depending on the operating conditions were also derived using the experimental data of residual starch concentration. Some inactivation models were tested to determine the relationship between process variables and enzyme stability during the hydrolysis process.     

Physicochemical characterisation of enzymatically hydrolysed derivatives of acetylated starch

Potato starch modified to different degrees by substitution with acetyl groups was the subject of this study undertaken to determine the influence of conditions of enzymatic hydrolysis on the surface-active properties of hydrolysates of acetylated starch. The effect of acetylation of starch preparation on its susceptibility to enzymatic hydrolysis in the membrane reactor was also considered. All hydrolysates of acetylated starch samples investigated were found to bring a decrease in the surface/interfacial tension, both at the air/water and the toluene/water interfaces. For binary hydrolysate-surfactant systems, the surface mole fractions in the mixed adsorbed monolayer at the air/water interface were estimated. For mixed systems, the synergism in reducing the surface tension at the air/water interface was observed. The experimentally obtained dynamic surface tension data for the aqueous solution of acetylated starch hydrolysates were used to estimate the diffusion coefficients. Particle size distributions of the hydrolysates formed in the aqueous solutions were compared to those of commercial maltodextrin.     

Glucoamylase production by the marine yeast Aureobasidium pullulans N13d and hydrolysis of potato starch granules by the enzyme

Under the optimal conditions, 10 U/ml of glucoamylase was produced by the marine yeast Aureobasidium pullulans N13d. It was noticed that the crude glucoamylase actively hydrolyzed potato starch granules, but poorly digested raw corn starch and sweet potato starch, resulting in conversion of 68.5, 19 and 22% of them into glucose within 6 h of incubation in the presence of 40 g/l of potato starch granules and 20 U/ml of the crude enzyme. When potato starch granules concentration was increased from 10 to 80 g/l, hydrolysis extent was decreased from 85.6 to 60%, while potato starch granules concentration was increased from 80 to 360 g/l, hydrolysis extent was decreased from 60 to 56%. Ratio of hydrolysis extent of potato starch granules to hydrolysis extent of gelatinized potato starch was 86.0% and the hydrolysis extent of potato starch granules by action of the crude glucoamylase (1.0 U/ml) was 18.5% within 30 min at 60 °C. Only glucose was detected during the hydrolysis, indicating that the crude enzyme could hydrolyze both α-1,4 and α-1,6 linkages of starch molecule in the potato starch.     

Investigating the role of mechanics in lignocellulosic biomass degradation during hydrolysis: Part II

Lignocellulose breakdown in biorefineries is facilitated by enzymes and physical forces. Enzymes degrade and solubilize accessible lignocellulosic polymers, primarily on fiber surfaces, and make fibers physically weaker. Meanwhile physical forces acting during mechanical agitation induce tearing and cause rupture and attrition of the fibers, leading to liquefaction, that is, a less viscous hydrolysate that can be further processed in industrial settings. This study aims at understanding how mechanical agitation during enzymatic saccharification can be used to promote fiber attrition. The effects of reaction conditions, such as substrate and enzyme concentration on fiber attrition rate and hydrolysis yield were investigated. To gain insight into the fiber attrition mechanism, enzymatic hydrolysis was compared to hydrolysis by use of hydrochloric acid. Results show that fiber attrition depends on several factors concerning reactor design and operation including drum diameter, rotational speed, mixing schedule, and concentrations of fibers and enzymes. Surprisingly, different fiber attrition patterns during enzymatic and acid hydrolysis were found for similar mixing schedules. Specifically, for tumbling mixing, slow continuous mixing appears to function better than faster, intermittent mixing even for the same total number of drum revolutions. The findings indicate that reactor design and operation as well as hydrolysis conditions are key to process optimization and that detailed insights are needed to obtain fast liquefaction without sacrificing saccharification yields.     

Debranching enzyme concentration effected on physicochemical properties and α-amylase hydrolysis rate of resistant starch type III from amylose rice starch

The effect of debranching enzyme concentration on physicochemical properties and α-amylase hydrolysis rate of resistant starch type III from high amylose rice starch were studied. The pullulanase enzyme (8, 10, 12, 14 and 16 U/g starch) was introduced to modify amylopectin molecules of 15% (w/w) gelatinized rice starches at 55 °C for 16 h. The debranched starches with different degrees of hydrolysis (0.14–5.27%), and having 66.60–98.82% β-amylolysis limit were then induced at 4 °C for 16 h, afterward a one cycle of freeze–thaw process (?10/30 °C) was applied. The results showed that a pullulanase hydrolysis improved the degree of syneresis (51.64–54.85% from 8 to 16 U/g starch). Resistant starch content increased sharply as the amount of the enzyme increased, reaching the highest (19.81%) for a 12 U/g starch and decreased to 13.16% by 16 U/g starch. α-Amylase hydrolysis rate showed that incompletely-debranched had a lower estimated glycemic index than completely debranched rice starches. Microstructure of the selected RS III samples using X-ray diffraction and scanning electron microscopy revealed a crystal pattern change from A- to V-type pattern and formed a coarse honeycomb-like and a filamentous network structure.     

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.     

响应曲面法制备蛹虫草子实体酶解液的研究

为了将蛹虫草开发成为便于人们食用的产品形式,本实验以不同的酶对蛹虫草进行水解得到蛹虫草酶解液.以水解度和酶解液中腺苷含量为目标,确定选用木瓜蛋白酶.以水解度为响应指标,应用响应曲面法对蛹虫草酶解条件进行优化,根据Box-Behnken中心组合实验设计原理,选取酶解温度、酶解时间、加酶量三因素三水平进行中心组合实验,响应曲面分析结果表明水解最佳条件为:酶解温度60.92℃,酶解时间11.85 h,加酶量1.02％,此条件下蛹虫草的水解度达到最大.水解度验证值61.27％与预测值60.76％接近,说明建立模型正确.     

Selective suppression of bacterial contaminants by process conditions during lignocellulose based yeast fermentations

Background

When scaling up lignocellulose-based ethanol production, the desire to increase the final ethanol titer after fermentation can introduce problems. A high concentration of water-insoluble solids (WIS) is needed in the enzymatic hydrolysis step, resulting in increased viscosity, which can cause mass and heat transfer problems because of poor mixing of the material. In the present study, the effects of mixing on the enzymatic hydrolysis of steam-pretreated spruce were investigated using a stirred tank reactor operated with different impeller speeds and enzyme loadings. In addition, the results were related to the power input needed to operate the impeller at different speeds, taking into account the changes in rheology throughout the process.

Results

A marked difference in hydrolysis rate at different impeller speeds was found. For example, the conversion was twice as high after 48 hours at 500 rpm compared with 25 rpm. This difference remained throughout the 96 hours of hydrolysis. Substantial amounts of energy were required to achieve only minor increases in conversion during the later stages of the process.

Conclusions

Impeller speed strongly affected both the hydrolysis rate of the pretreated spruce and needed power input. Similar conversions could be obtained at different energy input by altering the mixing (that is, energy input), enzyme load and residence time, an important issue to consider when designing large-scale plants.     

Production of maltooligosaccharides from starch and separation of maltopentaose by adsorption of them on activated carbon (I)

For the selective production of maltopentaose (G₅) over other oligosaccharides, enzymatic hydrolysis conditions of starch by commercial α-amylase (Termamyl^®) were investigated. The determined optimum condition was 29.6 KNU (Kilo Novo α-amylase Unit) enzyme loading in 150 mL of 0.3% starch solution under pH level of 5 at 40°C for 30 min. About 40% of G₅ selectivity can be attained using the determined optimum condition. For further enhancing G₅ selectivity, an activated carbon adsorption process has been attached after the enzymatic hydrolysis. From the adsorption process, G₅ can be enriched up to 72% in the solution.     

Enzymatic production of cyclodextrins from unliquefied corn starch in an attrition bioreactor

A novel enzymatic process for the production of cyclodextrins from unliquefied starch was developed. Cyclodextrins were produced in an attrition bioreactor in which simultaneous hydrolysis of starch and synthesis of cyclodextrins by cyclodextrin glycosyltransferase (CGTase) occur. The CGTase was obtained from isolated Bacillus sp. BE101, and maximum activity of the enzyme was observed at pH 6.0 and a temperature of 45 degrees C. The effect of milling media size and material on the performance of the attrition bioreactor was investigated, and operational parameters such as agitation speed, volume of milling media, ratio of enzyme to starch, and starch concentration were optimized. The production yield of cyclodextrins from unliquefied corn starch of 15% reached 35% at 24 h under optimized conditions. Energy consumption for the production of cyclodextrins in the attrition bioreactor system was estimated to be about 25% of that required for the liquefaction of starch in the conventional process.     

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.     

Purification and properties of a novel raw starch degrading cyclomaltodextrin glucanotransferase from Bacillus firmus

A novel raw starch degrading cyclomaltodextrin glucanotransferase (CGTase; E.C. 2.4.1.19), produced by Bacillus firmus, was purified to homogeneity by ultrafiltration, affinity and gel filtration chromatography. The molecular weight of the pure protein was estimated to be 78 000 and 82 000 Da, by SDS-PAGE and gel filtration, respectively. The pure enzyme had a pH optimum in the range 5.5–8.5. It was stable over the pH range 7–11 at 10 °C, and at pH 7.0 at 60 °C. The optimum temperature for enzyme activity was 65 °C. In the absence of substrate, the enzyme rapidly lost its activity above 30 °C. K _m and k _cat for the pure enzyme were 1.21 mg/ml and 145.17 μM/mg per minute respectively, with soluble starch as the substrate. For cyclodextrin production, tapioca starch was the best substrate used when gelatinized, while wheat starch was the best substrate used when raw. This CGTase could degrade raw wheat starch very efficiently; up to 50% conversion to cyclodextrins was obtained from 150 g/l starch without using any additives. The enzyme produced α-, β- and γ-cyclodextrins in the ratio of 0.2:9.2:0.6 and 0.2:8.6:1.2 from gelatinized tapioca starch and raw wheat starch with 150 g/l concentration respectively, after 18 h incubation. Received: 25 September 1998 / Received revision: 15 December 1998 / Accepted: 21 December 1998     

Enhanced production of raw starch degrading enzyme using agro-industrial waste mixtures by thermotolerant Rhizopus microsporus for raw cassava chip saccharification in ethanol production

In the present study, solid-state fermentation for the production of raw starch degrading enzyme was investigated by thermotolerant Rhizopus microsporus TISTR 3531 using a combination of agro-industrial wastes as substrates. The obtained crude enzyme was applied for hydrolysis of raw cassava starch and chips at low temperature and subjected to nonsterile ethanol production using raw cassava chips. The agro-industrial waste ratio was optimized using a simplex axial mixture design. The results showed that the substrate mixture consisting of rice bran:corncob:cassava bagasse at 8?g:10?g:2?g yielded the highest enzyme production of 201.6?U/g dry solid. The optimized condition for solid-state fermentation was found as 65% initial moisture content, 35°C, initial pH of 6.0, and 5?×?10⁶ spores/mL inoculum, which gave the highest enzyme activity of 389.5?U/g dry solid. The enzyme showed high efficiency on saccharification of raw cassava starch and chips with synergistic activities of commercial α-amylase at 50°C, which promotes low-temperature bioethanol production. A high ethanol concentration of 102.2?g/L with 78% fermentation efficiency was achieved from modified simultaneous saccharification and fermentation using cofermentation of the enzymatic hydrolysate of 300?g raw cassava chips/L with cane molasses.