酶法降解植物纤维素技术研究

用正交试验法探讨了以麦秸为原料进行纤维素酶降解的工艺条件。正交试验的结果表明,影响麦秸纤维素降解的因素的主次顺序为A（酶添加量）＞B（底物浓度）＞E（时间）＞C（温度）＞D（pH值）,纤维素酶解麦秸纤维素的最佳组合为A3B1E3C3D2,即纤维素酶的添加量为0．2％,底物浓度为5％,反应时间为2h,反应温度50℃,pH5.0时为最佳条件。在比常规酶解法时间缩短12－30倍的条件下,能使纤维素降解葡萄糖的转化率达22．3％。     

基于响应面设计脂肪酶Novo435催化合成甘油二酯的工艺优化

以甘油、油酸为原料,优化在无溶剂体系中以固定化脂肪酶Novo435催化合成甘油二酯（diglyceride,DAG）的工艺。系统考察底物摩尔比（油酸／甘油）、反应温度、时间和加酶量等因素对油酸转化率和甘油二酯含量影响的基础上,利用响应面试验设计优化各主效因子,并经回归分析获得最优的工艺条件。所得最优条件：油酸与甘油底物摩尔比2．27、反应温度48．14℃、反应时间6．3h、加酶量1．68％。在此条件下,实验测得油酸转化率为45．42％,甘油二酯质量分数为70．01％,与响应面模型预测值吻合。     

脂肪酶催化猪油与辛酸酸解制备功能性脂反应条件的优化

目的:探索有机溶剂体系中酶法酸解猪油与辛酸制备减热量型功能性脂的最佳反应条件。方法:采用响应曲面法中的3水平5因子2星点部分因子试验设计,评价酸解反应中的5个关键因素,即酶量、反应时间、反应温度、底物比率和水分添加量及其交互作用对辛酸插入率的影响,确定最佳反应条件。结果:建立了辛酸插入率对5个变量的一个2次多项式数学模型,该模型极显著(P<0.0001),拟合优度良好。通过主效应分析,得出每个因子对模型的贡献程度从大到小依次为反应温度(负效应)>底物比率>反应时间>酶量(在实验范围内,水分不影响辛酸插入率)。借助模型方程产生的等高线图及统计软件,分析得出最大辛酸插入率下各个因子的最适水平分别为酶量16%,反应时间36h,反应温度50℃,底物比率3.8,水分添加量5%。在此条件下辛酸插入率达到了50.5mol%,与模型预测值50.7mol%非常吻合。结论:应用响应曲面法对有机溶剂体系中酶法酸解猪油与辛酸制备减热量性脂的反应条件进行优化是合理可靠,科学迅速的,且有效的。     

响应面分析应用于抗病毒药物香菇多糖酯化工艺的优化

目的:应用响应面分析法(RSM)优化香菇多糖酯化的工艺,确定最佳酯化条件.方法:利用Design Expert软件的中心组合设计法对香菇多糖酯化条件进行了优化,并利用响应面分析法对主要影响因素进行了回归分析,主要考察脂肪酶添加量,反应时间和反应温度对酯化效果的影响.结果:得到了各因素的最佳水平值,即酶加量为0.069g,反应时间为11.92h,反应温度为40.4℃,在模拟优化的条件下,酯化后滴定所消耗NaOH量为36.60ml.结论:将在此条件下酯化的香菇多糖测定红外光谱,证实有酯键生成.     

青牛胆总黄酮的对比提取研究

采用分光光度法对青牛胆块根中总黄酮进行超声波法、浸提法和微波法比较提取研究.以总黄酮提取率为考察对象,研究提取温度、乙醇体积分数、料液比及提取时间等因素对青牛胆块根中总黄酮提取率的影响.结果表明:最佳提取方法为浸提法,最佳提取条件:乙醇体积分数60％,提取温度90℃,料液比1∶30,提取时间4h,总黄酮提取率6.294 mg/g.     

复合酶解法提取三七皂苷的实验研究

以三七提取液中总皂苷的含量和提取物得率为指标,考察了乙醇回流法、渗漉法、纤维素酶解法、果胶酶解法、复合酶解法的优劣,并采用单因素法和四因素（纤维素酶用量、果胶酶用量、酶解温度、乙醇浓度）三水平正交设计法对复合酶解法提取工艺条件进行优选,得到如下较理想的提取工艺条件：纤维素酶用量为15U／g（生药）、果胶酶用量为140U／g（生药）,酶解pH值为4．5,酶解温度为50℃,乙醇浓度为80％,提取时间为2．5h。所得三七提取液中总皂苷的含量为12．01％,提取物得率为35．82％。     

季铵型阳离子皂荚胶的合成

本文介绍了以皂荚胶粉,与阳离子试剂3-氯-2-羟丙基三甲基氯化铵(CHPTMA)为原料,制备季铵型阳离子皂荚胶,通过正交试验确定了生产一定取代度胶粉的最佳反应条件：反应温度65℃;反应时间6h;氢氧化钠与阳离子试剂摩尔比为0．8;乙醇质量分数90％。     

荷叶黄酮的溶剂热提取及其抗氧化作用研究

研究利用溶剂热法提取荷叶中黄酮类化合物的最佳工艺条件,考察了提取温度、时间、料液比、乙醇的体积分数及提取级数5个单因素对荷叶黄酮提取率的影响,并在单因素的基础上进行正交实验得到荷叶黄酮提取的最佳工艺条件:料液比1:40、乙醇体积分数为60%、提取2.5 h、提取温度80℃,提取2次。并研究了荷叶提取物在新榨豆油中的抗氧化作用,效果良好。     

木薯生料发酵生产燃料乙醇的工艺优化

为了实现生料发酵更好的应用,考察料水比、发酵温度、氮源及接种量等因素对木薯生料发酵生产燃料乙醇的影响,并通过正交试验分析主要因素之间的相互作用。结果表明:木薯生料发酵产燃料乙醇的最佳条件为料水比1∶2.0,活性干酵母接种量0.15%(质量分数),发酵温度32℃,发酵周期120 h,尿素添加量0.20%(质量分数)。在最佳条件下,发酵得到的燃料乙醇的酒精度可达到15.12%(体积分数)。本实验为高效利用木薯生料发酵生产燃料乙醇的工业化生产提供了重要参数。     

一步法发酵菊芋产乙醇菌种的筛选及产酶条件、酶学性质的研究

从腐烂的菊芋及实验室保存的菌种中,选育到一株发酵菊芋产乙醇的菌株克鲁维酵母Kluyveromyces marxianus Y1。利用正交实验法对克鲁维酵母产菊粉酶的培养基组成及培养条件进行优化,确定培养基组成（g/L）为：菊粉40,酵母粉4,蛋白胨4,尿素1;初始pH5．0,温度30℃,150r／min条件下培养达到最佳产酶效果（57U／mL）。该菌株所产菊粉酶的性质测定结果表明：以菊粉为底物,该菊粉酶最适反应温度为55℃,在60℃以下稳定性很好,高于60℃时酶迅速失活;最适pH为5．0,pH4．6—5．2范围内酶稳定性很好;该酶属于外切型菊粉酶,体积分数为8％的乙醇对酶活力基本没有影响。     

High solid simultaneous saccharification and fermentation of wet oxidized corn stover to ethanol

In this study ethanol was produced from corn stover pretreated by alkaline and acidic wet oxidation (WO) (195 degrees C, 15 min, 12 bar oxygen) followed by nonisothermal simultaneous saccharification and fermentation (SSF). In the first step of the SSF, small amounts of cellulases were added at 50 degrees C, the optimal temperature of enzymes, in order to obtain better mixing condition due to some liquefaction. In the second step more cellulases were added in combination with dried baker's yeast (Saccharomyces cerevisiae) at 30 degrees C. The phenols (0.4-0.5 g/L) and carboxylic acids (4.6-5.9 g/L) were present in the hemicellulose rich hydrolyzate at subinhibitory levels, thus no detoxification was needed prior to SSF of the whole slurry. Based on the cellulose available in the WO corn stover 83% of the theoretical ethanol yield was obtained under optimized SSF conditions. This was achieved with a substrate concentration of 12% dry matter (DM) acidic WO corn stover at 30 FPU/g DM (43.5 FPU/g cellulose) enzyme loading. Even with 20 and 15 FPU/g DM (corresponding to 29 and 22 FPU/g cellulose) enzyme loading, ethanol yields of 76 and 73%, respectively, were obtained. After 120 h of SSF the highest ethanol concentration of 52 g/L (6 vol.%) was achieved, which exceeds the technical and economical limit of the industrial-scale alcohol distillation. The SSF results showed that the cellulose in pretreated corn stover can be efficiently fermented to ethanol with up to 15% DM concentration. A further increase of substrate concentration reduced the ethanol yield significant as a result of insufficient mass transfer. It was also shown that the fermentation could be followed with an easy monitoring system based on the weight loss of the produced CO2.     

Optimization of fermentation conditions for the production of ethanol from sago starch using response surface methodology

The quantitative effects of temperature, pH and time of fermentation were investigated on simultaneous saccharification and fermentation (SSF) of ethanol from sago starch with glucoamylase (AMG) and Zymomonas mobilis ZM4 using a Box–Wilson central composite design protocol. The SSF process was studied using free enzyme and free cells and it was found that with sago starch, maximum ethanol concentration of 70.68 g/l was obtained using a starch concentration of 140 g/l, which represents an ethanol yield of 97.08%. The optimum conditions for the above yield were found to be a temperature of 36.74 °C, pH of 5.02 and time of fermentation of 17 h. Thus by using the central composite design, it is possible to determine the accurate values of the fermentation parameters where maximum production of ethanol occurs.     

The enzymatic hydrolysis and fermentation of pretreated wheat straw to ethanol

Autohydrolysis and ethanol-alkali pulping were used as pretreatment methods of wheat straw for its subsequent saccharification by Trichoderma reesei cellulase. The basic hydrolysis parameters, i.e., reaction time, pH, temperature, and enzyme and substrate concentration, were optimized to maximize sugar yields from ethanol-alkali modified straw. Thus, a 93% conversion of 2.5% straw material to sugar syrup containing 73% glucose was reached in 48 h using 40 filter paper units/g hydrolyzed substrate. The pretreated wheat straw was then fermented to ethanol at 43 degrees C in the simultaneous saccharification and fermentation (SSF) process using T. reesei cellulase and Kluyveromyces fragilis cells. From 10% (w/v) of chemically treated straw (dry matter), 2.4% (w/v) ethanol was obtained after 48 h. When the T. reesei cellulase system was supplemented with beta-glucosidase from Aspergillus niger, the ethanol yield in the SSF process increased to 3% (w/v) and the reaction time was shortened to 24 h.     

Fungal pretreatment of lignocellulose by Phanerochaete chrysosporium to produce ethanol from rice straw

Phanerochaete chrysosporium is a wood‐rot fungus that is capable of degrading lignin via its lignolytic system. In this study, an environmentally friendly fungal pretreatment process that produces less inhibitory substances than conventional methods was developed using P. chrysosporium and then evaluated by various analytical methods. To maximize the production of manganese peroxidase, which is the primary lignin‐degrading enzyme, culture medium was optimized using response surface methodologies including the Plackett–Burman design and the Box–Behnken design. Fermentation of 100 g of rice straw feedstock containing 35.7 g of glucan (mainly in the form of cellulose) by cultivation with P. chrysosporium for 15 days in the media optimized by response surface methodology was resulted in a yield of 29.0 g of glucan that had an enzymatic digestibility of 64.9% of the theoretical maximum glucose yield. In addition, scanning electronic microscopy, confocal laser scanning microscopy, and X‐ray diffractometry revealed significant microstructural changes, fungal growth, and a reduction of the crystallinity index in the pretreated rice straw, respectively. When the fungal‐pretreated rice straw was used as a substrate for ethanol production in simultaneous saccharification and fermentation (SSF) for 24 h, the ethanol concentration, production yield and the productivity were 9.49 g/L, 58.2% of the theoretical maximum, and 0.40 g/L/h, respectively. Based on these experimental data, if 100 g of rice straw are subjected to fungal pretreatment and SSF, 9.9 g of ethanol can be produced after 96 h, which is 62.7% of the theoretical maximum ethanol yield. Biotechnol. Bioeng. 2009; 104: 471–482 © 2009 Wiley Periodicals, Inc.     

Acetic acid-catalyzed hydrothermal pretreatment of corn stover for the production of bioethanol at high-solids content

Corn stover (CS) was hydrothermally pretreated using CH₃COOH (0.3 %, v/v), and subsequently its ability to be utilized for conversion to ethanol at high-solids content was investigated. Pretreatment conditions were optimized employing a response surface methodology (RSM) with temperature and duration as independent variables. Pretreated CS underwent a liquefaction/saccharification step at a custom designed free-fall mixer at 50 °C for either 12 or 24 h using an enzyme loading of 9 mg/g dry matter (DM) at 24 % (w/w) DM. Simultaneous enzymatic saccharification and fermentation (SSF) of liquefacted corn stover resulted in high ethanol concentration (up to 36.8 g/L), with liquefaction duration having a negligible effect. The threshold of ethanol concentration of 4 % (w/w), which is required to reduce the cost of ethanol distillation, was surpassed by the addition of extra enzymes at the start up of SSF achieving this way ethanol titer of 41.5 g/L.     

Optimization of bioethanol production during simultaneous saccharification and fermentation in very high-gravity cassava mash

Hydrolysis and fermentation conditions for production of ethanol from very high-gravity cassava mash by Saccharomyces cerevisiae during simultaneous saccharification and fermentation (SSF) processing were optimized using a statistical methodology. During the first part of the study, Placket–Burman design (PBD) was used to study 19 factors that could potentially influence ethanol production. Gravity, particle size, initial pH, and fermentation temperature were identified as key factors that significantly increased final ethanol concentration. The main and interaction effects of these factors were subsequently evaluated based on a quadratic equation generated by central composite design (CCD) using response-surface methodology (RSM). Under the optimized very high-gravity conditions, the final ethanol concentration obtained from experiment increased from 8.21% (wt.%) to 15.03% (wt.%) and was in good agreement with model prediction. By employing two other commercial Saccharomyces strains, similar results were obtained under the same optimized condition. Therefore, we conclude that final ethanol concentration, ethanol productivity (V _P/max), glucose utilization (Y _G/s, Y _P/s), and fermentation efficiency (η _f) were enhanced or maintained under the optimized condition of 40% gravity, 390 μm particle size, initial pH 5.5, and 27°C fermentation temperature.     

Statistical optimization of sulfite pretreatment of corncob residues for high concentration ethanol production

In this study, a central composite design of response surface method was used to optimize sulfite pretreatment of corncob residues, in respect to sulfite charge (5-10%), treatment time (1-2h), liquid/solid (l/s) ratio (6:1-10:1) and temperature (150-180°C) for maximizing glucose production in enzymatic hydrolysis process. The relative optimum condition was obtained as follows: sulfite charge 7.1%, l/s ratio 7.6:1, temperature 156°C for 1.4h, corresponding to 79.3% total glucan converted to glucose+cellobiose. In the subsequent simultaneous saccharification and fermentation (SSF) experiments using 15% glucan substrates pretreated under this kind of conditions, 60.8 g ethanol l(-1) with 72.2% theoretical yield was obtained.     

Simultaneous saccharification and ethanol fermentation of oxalic acid pretreated corncob assessed with response surface methodology

Response surface methodology was used to evaluate optimal time, temperature and oxalic acid concentration for simultaneous saccharification and fermentation (SSF) of corncob particles by Pichia stipitis CBS 6054. Fifteen different conditions for pretreatment were examined in a 2³ full factorial design with six axial points. Temperatures ranged from 132 to 180 °C, time from 10 to 90 min and oxalic acid loadings from 0.01 to 0.038 g/g solids. Separate maxima were found for enzymatic saccharification and hemicellulose fermentation, respectively, with the condition for maximum saccharification being significantly more severe. Ethanol production was affected by reaction temperature more than by oxalic acid and reaction time over the ranges examined. The effect of reaction temperature was significant at a 95% confidence level in its effect on ethanol production. Oxalic acid and reaction time were statistically significant at the 90% level. The highest ethanol concentration (20 g/l) was obtained after 48 h with an ethanol volumetric production rate of 0.42 g ethanol l⁻¹ h⁻¹. The ethanol yield after SSF with P. stipitis was significantly higher than predicted by sequential saccharification and fermentation of substrate pretreated under the same condition. This was attributed to the secretion of β-glucosidase by P. stipitis. During SSF, free extracellular β-glucosidase activity was 1.30 pNPG U/g with P. stipitis, while saccharification without the yeast was 0.66 pNPG U/g.     

Optimization of NaOH-catalyzed steam pretreatment of empty fruit bunch

Background

Empty fruit bunch (EFB) has many advantages, including its abundance, the fact that it does not require collection, and its year-round availability as a feedstock for bioethanol production. But before the significant costs incurred in ethanol production from lignocellulosic biomass can be reduced, an efficient sugar fractionation technology has to be developed. To that end, in the present study, an NaOH-catalyzed steam pretreatment process was applied in order to produce ethanol from EFB more efficiently.

Results

The EFB pretreatment conditions were optimized by application of certain pretreatment variables such as, the NaOH concentrations in the soaking step and, in the steam step, the temperature and time. The optimal conditions were determined by response surface methodology (RSM) to be 3% NaOH for soaking and 160°C, 11 min 20 sec for steam pretreatment. Under these conditions, the overall glucan recovery and enzymatic digestibility were both high: the glucan and xylan yields were 93% and 78%, respectively, and the enzymatic digestibility was 88.8% for 72 h using 40 FPU/g glucan. After simultaneous saccharification and fermentation (SSF), the maximum ethanol yield and concentration were 0.88 and 29.4 g/l respectively.

Conclusions

Delignification (>85%) of EFB was an important factor in enzymatic hydrolysis using CTec2. NaOH-catalyzed steam pretreatment, which can remove lignin efficiently and requires only a short reaction time, was proven to be an effective pretreatment technology for EFB. The ethanol yield obtained by SSF, the key parameter determining the economics of ethanol, was 18% (w/w), equivalent to 88% of the theoretical maximum yield, which is a better result than have been reported in the relevant previous studies.

     

Cellulosic ethanol production on temperature-shift simultaneous saccharification and fermentation using the thermostable yeast Kluyveromyces marxianus CHY1612

In cellulosic ethanol production, use of simultaneous saccharification and fermentation (SSF) has been suggested as the favorable strategy to reduce process costs. Although SSF has many advantages, a significant discrepancy still exists between the appropriate temperature for saccharification (45-50 °C) and fermentation (30-35 °C). In the present study, the potential of temperature-shift as a tool for SSF optimization for bioethanol production from cellulosic biomass was examined. Cellulosic ethanol production of the temperature-shift SSF (TS-SSF) from 16 w/v% biomass increased from 22.2 g/L to 34.3 g/L following a temperature shift from 45 to 35 °C compared with the constant temperature of 45 °C. The glucose conversion yield and ethanol production yield in the TS-SSF were 89.3% and 90.6%, respectively. At higher biomass loading (18 w/v%), ethanol production increased to 40.2 g/L with temperature-shift time within 24 h. These results demonstrated that the temperature-shift process enhances the saccharification ratio and the ethanol production yield in SSF, and the temperature-shift time for TS-SSF process can be changed according to the fermentation condition within 24 h.