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Experimental study on ethanol production from hydrothermal pretreated rapeseed straw by simultaneous saccharification and fermentation 下载免费PDF全文
Juan C. López‐Linares Inmaculada Romero Cristóbal Cara Encarnación Ruiz Eulogio Castro Manuel Moya 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2014,89(1):104-110
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木薯酒精渣的处置是制约木薯燃料乙醇大规模产业化的问题之一。本文立足于探索木薯酒精渣利用途径,分析了木薯酒精渣的主要成分,对比了氨水、氢氧化钠、氨水组合稀硫酸3种预处理方式对于木薯酒精渣纤维素和木素含量及纤维素酶水解效率的影响,分析了处理前后木薯酒精渣的表面结构及纤维素结晶度,并以氨水处理后的木薯酒精渣为底物,进行了同步糖化发酵。结果表明,3种预处理方法中组合预处理能更好地增加纤维素含量和提高纤维素酶水解效率,与未处理原料相比,组合预处理后纤维素含量增加了111.26%,木素下降了35.05%,酶水解72h纤维素转化率从42.10%增加到61.71%。氨水预处理后,原料的木素含量降低,处理后木薯酒精渣的表面变得更加粗糙,纤维素结晶度有所增加,以氨水处理后的木薯酒精渣为底物进行分批补料同步糖化发酵,当初始底物浓度为100.0g/L,分别在20h、40h、60h进行补料至最终底物浓度为400.0g/L时,发酵120h乙醇浓度达到51.0g/L。 相似文献
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蒸汽爆破麦草同步糖化发酵转化乙醇的研究 总被引:4,自引:0,他引:4
近年来对木质生物资源同步糖化发酵转化乙醇的研究较多,但是,麦草同步糖化发酵转化乙醇的最佳工艺条件还未确定。文中采用正交试验设计的方法,对在混合酶(纤维素酶Celluclast 1.5 1,β-葡萄糖苷酶Novozym 188)与酿酒酵母菌作用下,稀硫酸催化的蒸汽爆破麦草原料同步糖化发酵转化乙醇的工艺条件进行研究,详细讨论了反应温度、底物质量浓度、发酵液pH值、纤维素酶浓度对乙醇质量浓度和得率的影响。结果表明,工艺条件对乙醇质量浓度和得率的影响程度由高到低依次为:底物质量浓度、纤维素酶浓度、发酵液pH值、反应温度。最佳工艺条件为反应温度35℃,底物质量浓度100 g/L,发酵液pH值5.0,纤维素酶浓度30 FPU/g。在此条件下,随着反应时间的延长,乙醇质量浓度持续上升。反应72 h后,乙醇质量浓度和得率分别达到22.7 g/L和65.8%。 相似文献
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Peng LUO Zhong LIU Chuanmin YANG Gaosheng WANG 《Frontiers of Chemical Engineering in China》2008,2(4):447-451
Although simultaneous saccharification and fermentation (SSF) has been investigated extensively, the optimum condition for
SSF of wheat straw has not yet been determined. Dilute sulfuric acid impregnated and steam explosion pretreated wheat straw
was used as a substrate for the production of ethanol by SSF through orthogonal experiment design in this study. Cellulase
mixture (Celluclast 1.5 l and β-glucosidase Novozym 188) were adopted in combination with the yeast Saccharomyces cerevisiae AS2.1. The effects of reaction temperature, substrate concentration, initial fermentation liquid pH value and enzyme loading
were evaluated and the SSF conditions were optimized. The ranking, from high to low, of influential extent of the SSF affecting
factors to ethanol concentration and yield was substrate concentration, enzyme loading, initial fermentation liquid pH value
and reaction temperature, respectively. The optimal SSF conditions were: reaction temperature, 35°C; substrate concentration,
100 g·L−1; initial fermentation liquid pH, 5.0; enzyme loading, 30 FPU·g−1. Under these conditions, the ethanol concentration increased with reaction time, and after 72 h, ethanol was obtained in
65.8% yield with a concentration of 22.7 g·L−1.
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Translated from Chemical Engineering (China), 2007, 35(12): 42–45 [译自: 化学工程] 相似文献
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Gyun Min Lee Chul Ho Kim Zainal Abidin Mohammed Yusof Moon Hi Han Sang Ki Rhee 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》1987,38(4):235-242
Simultaneous saccharification and ethanol fermentation (SSF) of sago starch was studied using amyloglucosidase (AMG) and Zymomonas mobilis. The optimal concentration of AMG and operating temperature for the SSF process were found to be 0.5% (v/w) and 35°C, respectively. Under these conditions with 150 g dm?3 sago starch as a substrate, the final ethanol concentration obtained was 69.2 g dm?3 and ethanol yield, YP/S, 0.50 g g?1 (97% of theoretical yield). Sago starch in the concentration range of 100–200 g dm?3 was efficiently converted into ethanol. When compared to a two-step process involving separate saccharification and fermentation stages, the SSF reduced the total process time by half. 相似文献
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S Hari Krishna G
V Chowdary D Srirami Reddy C Ayyanna 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》1999,74(11):1055-1060
Simultaneous saccharification and fermentation (SSF) of alkaline hydrogen peroxide pretreated Antigonum leptopus (Linn) leaves to ethanol was optimized using cellulase from Trichoderma reesei QM‐9414 (Celluclast® from Novo) and Saccharomyces cerevisiae NRRL‐Y‐132 cells. Contrary to the saccharification optima (2.5% w/v substrate concentration, 50 °C, 4.5 pH, 40 FPU cellulase g−1 substrate and 24 h reaction time), the SSF optima was found to be somewhat different (10% w/v substrate, 40 °C, 100 FPU cellulase g−1 substrate and 72 h). Better ethanol yields were obtained with SSF compared with the traditional saccharification and subsequent fermentation (S&F) and when the cellulase was supplemented with β‐glucosidase. © 1999 Society of Chemical Industry 相似文献
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为了解氧气(O2)在玉米秸秆湿热预处理中的作用,优化玉米秸秆酒精生产工艺,本文采用三种不同湿热预处理条件处理玉米秸秆,即条件1(195℃,15min)、条件2(195℃,15min,12bar O2)和条件3(195℃,15min,12bar O2,2g/L Na2CO3),并利用酿酒酵母对预处理后的玉米秸秆同步糖化发酵酒精工艺(SSF)进行了研究。实验结果表明:经过预处理,玉米秸秆分为固体滤饼与水解液两部分,其中绝大部分纤维素以固体形式保留在滤饼中,而半纤维素和木质素由于不稳定则发生了部分水解或降解。三种预处理条件下纤维素总体收率分别为91.2%、94.6%和95.9%,半纤维素总体收率分别为74.5%、50.3%和68.2%,固体滤饼中木质素质量分数分别为25.2%、17.5%和13.7%,纤维素酶解葡萄糖率分别为64.8%、65.8%和67.6%。表明氧气对纤维素收率影响不大,能够促进半纤维素的溶出。氧气主要与木质素发生反应,尤其与碱性物质碳酸钠(Na2CO3)结合,能够促进木质素降解,从而获得了较高的纤维素收率和纤维素酶解葡萄糖率。因此在底物质量分数8%,经过酿酒酵母142h发酵,经条件3处理的玉米秸秆获得的酒精浓度最高,最终酒精浓度达到25.0g/L,并且整个发酵过程没有明显的抑制作用产生。 相似文献
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Ana B Moldes Jos L Alonso Juan C Paraj 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2001,76(3):279-284
In the one‐step conversion of wood into lactic acid by Simultaneous Saccharification and Fermentation (SSF), inhibition effects caused by hydrolysis‐ and fermentation‐derived compounds on both enzymatic activity and fermentative ability of microorganisms appear when the operation is carried out under conditions leading to high productivities. The main effects inhibiting SSF have been assessed, and the results obtained in fed‐batch experiments allowed the definition of strategies for improving the overall bioconversion process. As cellobiose caused significant inhibition of cellulases, the supplementation of media with β‐glucosidase resulted in improved kinetics and yields. The inhibition of both enzymatic activity and microbial metabolism by lactic acid was confirmed. Intermittent removal of lactic acid by passing the fermentation media through an anion‐exchange resin column resulted in increased productivities and yields. Improved conversion of pretreated wood into lactic acid (67% conversion of cellulose into lactic acid, with maximum lactic acid concentration of 108 g dm?3 and a productivity of 0.94 g dm?3 h?1) was achieved combining multiple substrate addition, supplementation with fresh nutrients and enzymes and removal of lactic acid. © 2001 Society of Chemical Industry 相似文献
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Some of the most recent, relevant, industrial and academic contributions made in the field of butanol production are reviewed here. The focus on butanol is due to the growing demand for non‐fossil biofuels. In addition, butanol can be mixed with fossil fuels or can be used alone, allowing an alternative to gasoline. Butanol can be synthesised biologically using sugars extracted from biomass such as agricultural waste. This agricultural waste must be pretreated before it is suitable for sugar extraction. Following this stage, enzymatic hydrolysis is employed, before performing fermentation using microorganisms. This article summarises some of the economical methods such as simultaneous saccharification and fermentation (SSF). Different pretreatment and saccharification processes were compared. Acid pretreatment and saccharification achieved the highest sugar concentrations from wheat straw. Monoethanolamine pretreatment achieved highest sugars from hardwood. Comparisons and analysis of different types of fermentation processes illustrated that immobilised reactor provided the best butanol rate of production. Integration of fermentation with product removal process improved butanol production in immobilised reactor. Gas stripping method was illustrated to be the product removal process. © 2011 Canadian Society for Chemical Engineering 相似文献
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Studies on simultaneous saccharification and fermentation (SSF) of wheat bran flour, a grain milling residue as the substrate
using coculture method were carried out with strains of starch digesting Aspergillus niger and nonstarch digesting and sugar fermenting Kluyveromyces marxianus in batch fermentation. Experiments based on central composite design (CCD) were conducted to maximize the glucose yield and
to study the effects of substrate concentration, pH, temperature, and enzyme concentration on percentage conversion of wheat
bran flour starch to glucose by treatment with fungal α-amylase and the above parameters were optimized using response surface
methodology (RSM). The optimum values of substrate concentration, pH, temperature, and enzyme concentration were found to
be 200 g/L, 5.5, 65°C and 7.5 IU, respectively, in the starch saccharification step. The effects of pH, temperature and substrate
concentration on ethanol concentration, biomass and reducing sugar concentration were also investigated. The optimum temperature
and pH were found to be 30°C and 5.5, respectively. The wheat bran flour solution equivalent to 6% (w/V) initial starch concentration gave the highest ethanol concentration of 23.1 g/L after 48 h of fermentation at optimum conditions
of pH and temperature. The growth kinetics was modeled using Monod model and Logistic model and product formation kinetics
using Leudeking-Piret model. Simultaneous saccharificiation and fermentation of liquefied wheat bran starch to bioethanol
was studied using coculture of amylolytic fungus A. niger and nonamylolytic sugar fermenting K. marxianus. 相似文献
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Yinxiu CAO Hongchi TIAN Kun YAO Yingjin YUAN 《Frontiers of Chemical Science and Engineering》2011,5(3):318
Due to its merits of drought tolerance and high yield, sweet potatoes are widely considered as a potential alterative feedstock for bioethanol production. Very high gravity (VHG) technology is an effective strategy for improving the efficiency of ethanol fermentation from starch materials. However, this technology has rarely been applied to sweet potatoes because of the high viscosity of their liquid mash. To overcome this problem, cellulase was added to reduce the high viscosity, and the optimal dosage and treatment time were 8 U/g (sweet potato powder) and 1 h, respectively. After pretreatment by cellulase, the viscosity of the VHG sweet potato mash (containing 284.2 g/L of carbohydrates) was reduced by 81%. After liquefaction and simultaneous saccharification and fermentation (SSF), the final ethanol concentration reached 15.5% (v/v), and the total sugar conversion and ethanol yields were 96.5% and 87.8%, respectively. 相似文献
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Studies on simultaneous saccharification and fermentation (SSF) of wheat bran flour, a grain milling residue as the substrate using coculture method were carried out with strains of starch digesting Aspergillus niger and nonstarch digesting and sugar fermenting Kluyveromyces marxianus in batch fermentation. Experiments based on central composite design (CCD) were conducted to maximize the glucose yield and to study the effects of substrate concentration, pH, temperature, and enzyme concentration on percentage conversion of wheat bran flour starch to glucose by treatment with fungal α-amylase and the above parameters were optimized using response surface methodology (RSM). The optimum values of substrate concentration, pH, temperature, and enzyme concentration were found to be 200 g/L, 5.5, 65°C and 7.5 IU, respectively, in the starch saccharification step. The effects of pH, temperature and substrate concentration on ethanol concentration, biomass and reducing sugar concentration were also investigated. The optimum temperature and pH were found to be 30°C and 5.5, respectively. The wheat bran flour solution equivalent to 6% (w /V ) initial starch concentration gave the highest ethanol concentration of 23.1 g/L after 48 h of fermentation at optimum conditions of pH and temperature. The growth kinetics was modeled using Monod model and Logistic model and product formation kinetics using Leudeking-Piret model. Simultaneous saccharificiation and fermentation of liquefied wheat bran starch to bioethanol was studied using coculture of amylolytic fungus A. niger and nonamylolytic sugar fermenting K. marxianus . 相似文献
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Badal C Saha Michael A Cotta 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2007,82(10):913-919
BACKGROUND: The objective of this work is to develop an efficient pretreatment method that can help enzymes break down the complex carbohydrates present in wheat straw to sugars, and to then ferment of all these sugars to ethanol. RESULTS: The yield of sugars from wheat straw (8.6%, w/v) by lime pretreatment (100 mg g?1 straw, 121 °C, 1 h) and enzymatic hydrolysis (45 °C, pH 5.0, 120 h) using a cocktail of three commercial enzyme preparations (cellulase, β‐glucosidase, and xylanase) at the dose level of 0.15 mL of each enzyme preparation g?1 straw was 568 ± 13 mg g?1 (82% yield). The concentration of ethanol from lime pretreated enzyme saccharified wheat straw (78 g) hydrolyzate by recombinant Escherichia coli strain FBR5 at pH 6.5 and 35 °C in 24 h was 22.5 ± 0.6 g L?1 with a yield of 0.50 g g?1 available sugars (0.29 g g?1 straw). The ethanol concentration was 20.6 ± 0.4 g L?1 with a yield of 0.26 g g?1 straw in the case of simultaneous saccharification and fermentation by the E. coli strain at pH 6.0 and 35 °C in 72 h. CONCLUSION: The results are important in choosing a suitable pretreatment option for developing bioprocess technologies for conversion of wheat straw to fuel ethanol. Copyright © 2007 Society of Chemical Industry 相似文献
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酒精不仅是重要的可再生能源,在食品、化工、医药等领域应用也极其广泛。高密度发酵(HCDF)能有效提高酒精产率降低能耗及废液排放,极具应用潜力。本文针对目前淀粉质原料HCDF中酵母选育、培养条件优化、工艺过程优化同步耦合及动力学模型的多元统计控制,综合分析了神经交叉网络-模糊控制和基于经验的实验系统等国内外最新进展,旨在为HCDF酒精生产工艺的进一步研究提供参考依据。 相似文献