木质纤维素的预处理及其酶解

从木质纤维素制取燃料乙醇,主要包括原料预处理、酶水解糖化及酒精发酵三个部分.通过前二步获得较高还原糖总量是提高乙醇得率的关键.预处理技术及工艺直接影响酶解效果,而酶水解是一个涉及多因素变化的复杂异相动力学过程.本文主要针对这两部分的国内外研究现状作一论述,并提出该领域目前所面临的问题及发展前景.     

植物细胞壁蛋白与木质纤维素酶解

木质纤维素是生产生物能源和材料的重要原料。木质纤维素具有高度复杂的结构,其酶解效率除了受自身的凝聚态结构影响外,还受到细胞壁自身组分的影响。本文综述了植物细胞壁中主要蛋白的特征及其与木质纤维素酶解的关系。从植物自身细胞壁蛋白活性出发来研究木质纤维素的酶解,为研究其酶解机制和高效酶解方法提供了新思路。     

Kinetic Studies on the Product Inhibition of Enzymatic Lignocellulose Hydrolysis

In order to understand the product inhibition of enzymatic lignocellulose hydrolysis, the enzymatic hydrolysis of pretreated rice straw was carried out over an enzyme loading range of 2 to 30 FPU/g substrate, and the inhibition of enzymatic hydrolysis was analyzed kinetically based on the reducing sugars produced. It was shown that glucose, xylose, and arabinose were the main reducing sugar components contained in the hydrolysate. The mass ratio of glucose, xylose, and arabinose to the total reducing sugars was almost constant at 52.0?%, 29.7?% and 18.8?%, respectively, in the enzyme loading range. The reducing sugars exerted competitive inhibitory interferences to the enzymatic hydrolysis. Glucose, xylose, and arabinose had a dissociation constant of 1.24, 0.54 and 0.33?g/l, respectively. The inhibitory interferences by reducing sugars were superimposed on the enzymatic hydrolysis. The enzymatic hydrolysis could be improved by the removal of the produced reducing sugars from hydrolysate.     

非离子型表面活性剂对木质纤维素酶催化水解的影响及机理

木质纤维素的酶解糖化过程是纤维素生物质转化中的关键步骤,也是限制纤维素生物转化生产燃料和化学品的主要瓶颈。大量的研究表明,非离子型表面活性剂能够强化木质纤维素酶解过程,显著提高纤维素的酶催化水解效率。本文综述了非离子型表面活性剂对纯纤维素和木质纤维素底物酶解的影响,分析了底物结构特性、水解条件、纤维素酶组成等诸多因素与表面活性剂作用效果之间的关联,并从纤维素酶的吸附特性、纤维素酶组分间的协同作用等方面对非离子表面活性剂的作用机理进行了总结。结合已有的研究进展和存在的问题,提出了今后表面活性剂对于木质纤维素酶催化水解影响的研究重点方向,即系统分析底物结构、水解条件等因素对表面活性剂作用的宏观影响,以及分析这种作用的热力学和动力学特性,而微观上需要从原子和分子层面上解析表面活性剂与底物和纤维素酶之间的相互作用特性。     

Enhanced Enzymatic Hydrolysis of Sorghum Stalk by Supercritical Carbon Dioxide and Ultrasonic Pretreatment

Applied Biochemistry and Biotechnology - Sorghum was pretreated by sole ultrasound or supercritical carbon dioxide (scCO2), as well as the method combining both to intensify enzymatic hydrolysis....     

木质纤维素酶解糖化*

纤维素水解转化为可发酵糖工艺是纤维素乙醇炼制过程中至关重要的环节。酶法水解工艺具有条件温和、副产物少、环境友好等特点,因而受到广泛重视。目前许多学者已针对如何提高木质纤维素酶解效率、降低纤维素酶成本等问题,开展了多种化学、生物技术及工艺耦合的研究。本文综述了近几年木质纤维素酶解领域取得的最新工艺进展和理论研究成果,对原料预处理、多酶复配优化、酶脱附与重复利用、工艺耦合、高固液比反应等方面的研究情况进行了总结,同时展望了木质纤维素酶解工艺的未来发展方向。     

Continuous Enzymatic Hydrolysis of Lignocellulosic Biomass with Simultaneous Detoxification and Enzyme Recovery

Recovering hydrolysis enzymes and/or alternative enzyme addition strategies are two potential mechanisms for reducing the cost during the biochemical conversion of lignocellulosic materials into renewable biofuels and biochemicals. Here, we show that enzymatic hydrolysis of acid-pretreated pine wood with continuous and/or fed-batch enzyme addition improved sugar conversion efficiencies by over sixfold. In addition, specific activity of the hydrolysis enzymes (cellulases, hemicellulases, etc.) increased as a result of continuously washing the residual solids with removal of glucose (avoiding the end product inhibition) and other enzymatic inhibitory compounds (e.g., furfural, hydroxymethyl furfural, organic acids, and phenolics). As part of the continuous hydrolysis, anion exchange resin was tested for its dual application of simultaneous enzyme recovery and removal of potential enzymatic and fermentation inhibitors. Amberlite IRA-96 showed favorable adsorption profiles of inhibitors, especially furfural, hydroxymethyl furfural, and acetic acid with low affinity toward sugars. Affinity of hydrolysis enzymes to adsorb onto the resin allowed for up to 92 % of the enzymatic activity to be recovered using a relatively low-molar NaCl wash solution. Integration of an ion exchange column with enzyme recovery into the proposed fed-batch hydrolysis process can improve the overall biorefinery efficiency and can greatly reduce the production costs of lignocellulosic biorenewable products.

壳寡糖的酶法制备

通过还原端基、酶解产物聚合度、水解液调碱性后透光率的测定以及酶解产物的TLC、HPLC分析,研究了壳聚糖酶降解壳聚糖过程中壳聚糖浓度、酶用量、反应时间和pH对酶促反应速率和产物聚合度的影响。结果表明:壳聚糖酶在底物浓度0.03 g/mL、壳聚糖酶用量4~6 u/g、pH=5.8和水解200 min时,可得到以聚合度3~7为主的壳寡糖。     

Reduction of Enzyme Dosage by Oxygen Delignification and Mechanical Refining for Enzymatic Hydrolysis of Green Liquor-Pretreated Hardwood

In this study, a strategy to reduce enzyme dosage is evaluated by applying two post-treatments, oxygen delignification and mechanical refining. The sugar conversion for GL12 substrates was increased from 51.5% to 77.9% with post-treatments at the enzyme dosage of 10 FPU. When the amount of enzyme was reduced to 5 FPU with post-treatments, the conversion of 71.8% was obtained, which was significant higher than the conversion without any post-treatment using 10 FPU (51.5%). This clearly demonstrates the benefit of post-treatments that allows more than 50% of enzyme reduction at the same level of enzymatic conversion. Enzyme-accessible surface area and pore volume were evaluated by Simons' staining and DSC thermoporometry methods, and strong correlations were found with the sugar conversion.     

Preparation of Hepta-O-Acetylsucroses and Hexa-O-Acetylsucroses by Enzymatic Hydrolysis

ABSTRACT

Octa-O-acetylsucrose (1) was regioselectively hydrolyzed by the lipase AK from Pseudomonas sp. in aqueous buffer and two hepta-O-acetylsucroses and two hexa-O-acetylsucroses were obtained by column purification. After analysis by NMR methods, four products were shown to be 3,4,6,1′,3′,4′,6′-hepta-O-acetylsucrose (2), 2,3,4,6,1′,3′,6′-hepta-O-acetylsucrose (3), 3,4,6,1′,3′,6′-hexa-O-acetylsucrose (4) and 2,3,4,6,3′,6′-hexa-O-acetylsucrose (5).     

Enzymatic Reactions in Organic Synthesis 3-Separations of Esters by Enzymatic Hydrolysis

Enzymatic hydrolyses were used to separate mixtures of esters.     

Enzymatic Hydrolysis of Recovered Office Printing Paper with Low Enzyme Dosages to Produce Fermentable Sugars

The use of recovered paper and paper manufacturing wastes are a potentially large, concentrated, and convenient raw material for ethanol production via enzyme hydrolysis and fermentation. However, many previous studies in the area have investigated impractically high enzyme charges. In this research, low dosages of enzymes on copy paper (CP) were investigated for the conditions of 5% consistency (w/v) and 50 °C for 48 h. The removal of inorganic filler (mainly calcium carbonate) by washing prior to hydrolysis led to higher sugar yields than the unwashed CP as well as CP acidified to remove the ash. Enzyme adsorption measurement showed that both acid-soluble ash and acid-insoluble ash adsorb enzymes with a greater affinity than fibers. Drying of the fibers (termed hornification) decreased the efficiency of enzyme hydrolysis, confirming previous results. The mechanical refining at 10% consistency in a laboratory refining mill of previously dried fibers improved the sugar recovery to similar or higher levels as never-dried fibers. By plotting water retention value (WRV) versus corresponding sugar recovery, it was shown that WRV is more useful at low enzyme charges reflecting the use of refining and the reversal of hornification. For de-ashed and refined copy paper, the sugar recovery was determined to be 82% and 97% with enzyme dosages of 4 and 8 Filter Paper Unit (FPU)/g oven-dried (OD) substrate.     

β—环糊精衍生物的金属配合物催化RNA的水解

用 β-环糊精 (β- CD)与马来酸酐合成了双 (6 -氧 -丁烯二酸单脂 ) - β- CD(简称 E1 ) ,用 KI对 E1 进行取代 ,生成了双 (6 -碘 ) - β- CD,其与组氨酸在 Na OH溶液中反应 ,生成双 (6 -氮 -组胺酸 ) - β- CD(简称 E2 ) ,E2 分别与 Mg( )、Zn( )、Fe( )和 Fe( )形成配合物 .研究了这 4种金属配合物对 RNA的水解 ,并与 Na OH水解 RNA进行了比较 ,发现 E2 · Fe( )对 RNA的水解能力可达到 Na OH水解 RNA能力的 96 .9% .     

Enzymatic Hydrolysis and Ethanol Fermentation of High Dry Matter Wet-Exploded Wheat Straw at Low Enzyme Loading

Wheat straw was pretreated by wet explosion using three different oxidizing agents (H₂O₂, O₂, and air). The effect of the pretreatment was evaluated based on glucose and xylose liberated during enzymatic hydrolysis. The results showed that pretreatment with the use of O₂ as oxidizing agent was the most efficient in enhancing overall convertibility of the raw material to sugars and minimizing generation of furfural as a by-product. For scale-up of the process, high dry matter (DM) concentrations of 15–20% will be necessary. However, high DM hydrolysis and fermentation are limited by high viscosity of the material, higher inhibition of the enzymes, and fermenting microorganism. The wet-explosion pretreatment method enabled relatively high yields from both enzymatic hydrolysis and simultaneous saccharification and fermentation (SSF) to be obtained when performed on unwashed slurry with 14% DM and a low enzyme loading of 10 FPU/g cellulose in an industrial acceptable time frame of 96 h. Cellulose and hemicellulose conversion from enzymatic hydrolysis were 70 and 68%, respectively, and an overall ethanol yield from SSF was 68%.     

Enzymatic Hydrolysis of Spent Coffee Ground

Spent coffee ground (SCG) is the main residue generated during the production of instant coffee by thermal water extraction from roasted coffee beans. This waste is composed mainly of polysaccharides such as cellulose and galactomannans that are not solubilised during the extraction process, thus remaining as unextractable, insoluble solids. In this context, the application of an enzyme cocktail (mannanase, endoglucanase, exoglucanase, xylanase and pectinase) with more than one component that acts synergistically with each other is regarded as a promising strategy to solubilise/hydrolyse remaining solids, either to increase the soluble solids yield of instant coffee or for use as raw material in the production of bioethanol and food additives (mannitol). Wild fungi were isolated from both SCG and coffee beans and screened for enzyme production. The enzymes produced from the selected wild fungi and recombinant fungi were then evaluated for enzymatic hydrolysis of SCG, in comparison to commercial enzyme preparations. Out of the enzymes evaluated on SCG, the application of mannanase enzymes gave better yields than when only cellulase or xylanase was utilised for hydrolysis. The recombinant mannanase (Man1) provided the highest increments in soluble solids yield (17 %), even when compared with commercial preparations at the same protein concentration (0.5 mg/g SCG). The combination of Man1 with other enzyme activities revealed an additive effect on the hydrolysis yield, but not synergistic interaction, suggesting that the highest soluble solid yields was mainly due to the hydrolysis action of mannanase.     

酶催化水解法快速测定牛奶中蛋白质含量

以酪蛋白水解度为指标,采用pH-stat法优化了胰蛋白酶催化酪蛋白水解的反应条件,并以该酶为检测用酶,分析了酪蛋白浓度与酶解反应初速度的关系,并建立了一种快速检测牛奶中蛋白质含量的方法.在pH=7.5,温度55℃的条件下,用pH-stat法测得酪蛋白浓度与酶促蛋白质水解反应初速度呈良好线性关系.最后采用该酶催化水解法测...     

Enzymatic Hydrolysis of Polylactic Acid Fiber

This study investigated the optimization of the enzymatic processing conditions for polylactic acid (PLA) fibers using enzymes consisting of lipases originating from different sources. The hydrolytic activity was evaluated taking into consideration the pH, temperature, enzyme concentration, and treatment time. The structural change of the PLA fibers was measured in the optimal treatment conditions. PLA fiber hydrolysis by lipases was maximized for lipase from Aspergillus niger at 40 °C for 60 min at pH 7.5 with 60% (owf) concentration, for lipase from Candida cylindracea at 40 °C for 120 min at pH 8.0 with 70% (owf) concentration, and for lipase from Candida rugosa at 45 °C for 120 min at pH 8.0 with 70% (owf) concentration. There was a change in protein absorbance of the treatment solution before and after all lipase treatments. The analyses of the chemical structure change and structural properties of the PLA due to lipase treatment was confirmed by tensile strength, differential scanning calorimetry, wide-angle X-ray scattering diffractometry, Fourier transform infrared spectroscopy, and scanning electron microscopy.     

大豆分离蛋白的酶水解

大豆分离蛋白的酶水解;大豆分离蛋白;水解作用;光散射     

2-氨基吡啶金属配合物对羧酸酯水解的催化作用

 合成了2-氨基吡啶(2-AP)为配体的Zn(2-AP)2(OAc)2,Ni(2-AP)2(OAc)2和Cu(2-AP)2(OAc)2三种金属配合物,并将其用于催化2-吡啶甲酸对硝基苯酚酯(PNPP)和乙酸对硝基苯酚酯(PNPA)的水解反应. 研究了金属配合物催化PNPP水解的动力学,提出了可能的催化机理. 结果表明,Zn(2-AP)2(OAc)2和Ni(2-AP)2(OAc)2金属配合物对PNPP水解反应有显著的催化作用,且Ni(2-AP)2(OAc)2的催化活性大于Zn(2-AP)2(OAc)2,而对PNPA无催化活性. Cu(2-AP)2(OAc)2对PNPP和PNPA均无催化活性. 这可能源自底物本身的特性以及配合物结构的差异. 同时,实验结果也说明合成的Zn(2-AP)2-(OAc)2和Ni(2-AP)2(OAc)2是水解金属酶的良好模型.     

Kinetics of Enzymatic High-Solid Hydrolysis of Lignocellulosic Biomass Studied by Calorimetry

Enzymatic hydrolysis of high-solid biomass (>10% w/w dry mass) has become increasingly important as a key step in the production of second-generation bioethanol. To this end, development of quantitative real-time assays is desirable both for empirical optimization and for detailed kinetic analysis. In the current work, we have investigated the application of isothermal calorimetry to study the kinetics of enzymatic hydrolysis of two substrates (pretreated corn stover and Avicel) at high-solid contents (up to 29% w/w). It was found that the calorimetric heat flow provided a true measure of the hydrolysis rate with a detection limit of about 500 pmol glucose s⁻¹. Hence, calorimetry is shown to be a highly sensitive real-time method, applicable for high solids, and independent on the complexity of the substrate. Dose–response experiments with a typical cellulase cocktail enabled a multidimensional analysis of the interrelationships of enzyme load and the rate, time, and extent of the reaction. The results suggest that the hydrolysis rate of pretreated corn stover is limited initially by available attack points on the substrate surface (<10% conversion) but becomes proportional to enzyme dosage (excess of attack points) at later stages (>10% conversion). This kinetic profile is interpreted as an increase in polymer end concentration (substrate for CBH) as the hydrolysis progresses, probably due to EG activity in the enzyme cocktail. Finally, irreversible enzyme inactivation did not appear to be the source of reduced hydrolysis rate over time.