菊糖芽孢乳杆菌利用麸皮水解液发酵生产D-乳酸

考察菊糖芽孢乳杆菌YBS1-5利用麸皮的水解液发酵生产D-乳酸的性能。首先研究了不同蛋白酶对麸皮中蛋白组分的水解效率,优选酸性蛋白酶并对其进行水解工艺的优化,最终其水解液中的含氮量为4.6 g/L,水解效率为85.8%。对酸性蛋白酶的水解液残渣进行稀酸预处理后,利用纤维素酶对其进行酶解。通过批次补料酶解,水解液中的还原糖质量浓度达141.2 g/L,其中葡萄糖质量浓度为138.1 g/L、木糖质量浓度为1.4 g/L。利用麸皮的蛋白酶水解液和纤维素酶水解液替代葡萄糖和酵母粉发酵制备D-乳酸。在96 h内,D-乳酸产量达99.5 g/L,生产速率达1.04 g/(L·h),转化率89.1%。     

亚硫酸盐甘蔗渣浆酶解液发酵制备乙醇

以亚硫酸盐甘蔗渣浆酶解液作为原料,利用C. shehatae发酵制取燃料乙醇。结果表明：还原糖最适初始质量浓度为葡萄糖140 g/L、木糖60 g/L、酶解液总糖80 g/L。利用初始葡萄糖55.06 g/L、木糖11.18 g/L、纤维二糖4.51 g/L的亚硫酸盐甘蔗渣浆酶解液发酵,经18 h获得乙醇22.98 g/L。乙醇得率为67.23%,葡萄糖利用率为99.27%,木糖利用率为32.96%,C. shehatae适合作为蔗渣为原料的乙醇发酵菌株。     

丙酮丁醇梭菌发酵菊芋汁生产丁醇

对丙酮丁醇梭菌Clostridium acetobutylicum L7发酵菊芋汁酸水解液生产丁醇进行了初步研究。实验结果表明,以该水解液为底物生产丁醇,不需要添加氮源和生长因子。当水解液初始糖浓度为48.36 g/L时,其发酵性能与以果糖为碳源的对照组基本相同,发酵终点丁醇浓度为8.67 g/L,丁醇、丙酮和乙醇的比例为0.58∶0.36∶0.06,但与以葡萄糖为碳源的对照组相比,发酵时间明显延长,表明该菌株葡萄糖转运能力强于果糖。当水解液初始糖浓度提高到62.87 g/L时,发酵终点残糖浓度从3.09 g/L增加到3.26 g/L,但丁醇浓度却提高到11.21 g/L,丁醇、丙酮和乙醇的比例相应为0.64∶0.29∶0.05,表明适量糖过剩有助于C.acetobutylicum L7胞内代谢从丙酮合成向丁醇合成途径调节;继续提高水解液初始糖浓度,发酵终点残糖浓度迅速升高,丁醇生产的技术经济指标受到明显影响。     

玉米芯稀酸水解及L-乳酸发酵研究

对玉米芯稀硫酸水解条件及糖化液发酵L-乳酸进行了初步研究。结果表明,玉米芯木聚糖最适水解条件为2%H2SO_4、120℃、30 min、固液比1:10,糖化液还原糖含量可达40.8 g/L,主要成分为木塘。细菌A-19可以利用水解液中的葡萄糖和木糖产酸,最适发酵条件为45℃、pH 6.5,从45℃～51℃、pH 5.5～pH 6.5产量均较高。用未浓缩的水解液发酵24 h,L-乳酸产量为30.6g/L,残糖为1.6 g/L,糖酸转化率为82.6%;用浓缩1倍的水解液发酵48 h,L-乳酸产量为41.4 g/L,残糖4.1g/L,糖酸转化率为68.2%,在发酵48 h后继续补料发酵至72 h(补料液为浓缩3倍的水解液),L-乳酸产量为50.9 g/L,残糖6.3 g/L,糖酸转化率为71.8%。该研究为利用木质纤维素生产L-乳酸奠定了一定基础。     

利用甜菜糖蜜补料发酵生产丁醇

从土壤中分离出1株适合利用甜菜糖蜜发酵生产丁醇的丙酮丁醇梭菌(Clostridium acetobutylicum)2N,通过优化发酵条件,得到最适发酵温度为33℃,玉米浆最适添加量为15g/L,发现甜菜糖蜜中还原糖质量浓度高于50g/L时影响菌株的生长和溶剂生产。以补料分批发酵方式降低底物抑制,33℃发酵48h后,丁醇和总溶剂的质量浓度分别达到14.15g/L和19.65g/L,丁醇质量分数超过70%。     

化学改性甘蔗渣对固定化细胞发酵产丁醇的影响

旨在研究化学改性的甘蔗渣作为固定化载体对丙酮丁醇梭菌Clostridium acetobutylicum XY16发酵制备生物丁醇的影响。首先利用不同浓度的聚乙烯亚胺(PEI)和1 g/L戊二醛(GA)对甘蔗渣表面进行化学改性,增强甘蔗渣对Clostridium acetobutylicum XY16的附载能力。经4 g/L聚乙烯亚胺和1 g/L戊二醛改性的甘蔗渣(添加量10 g/L)应用到固定化批次发酵中,发酵36 h后丁醇和总溶剂浓度最高,分别达到了12.24 g/L和21.67 g/L,同时溶剂的生产速率达到0.60 g/(L·h),生产速率比游离细胞和未改性甘蔗渣固定化细胞分批发酵分别提高了130.8%和66.7%。在此基础上对改性甘蔗渣固定化的细胞进行6次重复批次发酵,丁醇和总溶剂的产量稳定,溶剂生产速率逐渐提高至0.83 g/(L·h),同时转化率也提高至0.42 g/g。     

休哈塔假丝酵母乙醇发酵性能的研究

木糖的高效发酵是制约纤维素燃料乙醇生产的技术瓶颈之一,高性能发酵菌种的开发是本领域研究的重点。以木糖发酵的典型菌株休哈塔假丝酵母为材料,研究氮源配比、葡萄糖和木糖初始浓度、葡萄糖添加及典型抑制物等因素对其木糖利用和乙醇发酵性能的影响规律。结果表明,硫酸铵更适宜于木糖和葡萄糖发酵产乙醇。在摇瓶振荡发酵条件下,该酵母可发酵164.0 g/L葡萄糖生成61.9 g/L乙醇,糖利用率和乙醇得率分别为99.8%和74.0%;受酵母细胞膜上转运体系的限制,对木糖的最高发酵浓度为120.0 g/L,可生成45.7 g/L乙醇,糖利用率和乙醇得率分别达到94.8%和87.0%。休哈塔假丝酵母发酵木糖的主要产物为乙醇,仅生成微量的木糖醇;添加葡萄糖可促进木糖的利用;休哈塔假丝酵母在葡萄糖发酵时的乙酸和甲酸的耐受浓度分别为8.32和2.55 g/L,木糖发酵时的乙酸和甲酸的耐受浓度分别为6.28和1.15 g/L。     

玉米秸秆酶水解过程中的酶复配条件优化

降低酶解成本是纤维素乙醇生产的关键。利用酶复配技术优化蒸汽爆破处理后玉米秸秆的酶水解工艺条件,以提高纤维素的转化率。通过单因素实验和正交实验,研究了纤维素酶、木聚糖酶和β-葡萄糖苷酶对酶解效率的影响规律。结果表明,汽爆玉米秸秆,纤维素含量达42.21%,半纤维素仅为3.65%。纤维素酶对酶解过程起决定性作用,添加40 FPU/g时,酶解率为75.45%;木聚糖酶可促使更多的纤维素暴露出来,添加1 500 IU/g时,酶解率最高为78.03%;β-葡萄糖苷酶有助于消除纤维二糖积累造成的反馈抑制,用量40 IU/g时,纤维二糖浓度为0.330 4 g/100 m L,酶解率达76.45%。正交实验确定最佳工艺为:纤维素酶用量30 FPU/g,木聚糖酶用量800 IU/g,β-葡萄糖苷酶用量40 IU/g;该条件下,进行底物质量浓度25%的验证实验,葡萄糖达9.3g/100 m L,若用单一天冠纤维素酶,葡萄糖仅5.9 g/100 m L,提高了57.63%。三种酶的影响顺序为:纤维素酶木聚糖酶β-葡萄糖苷酶。     

产D-乳酸重组大肠杆菌ptsG基因的敲除及其混合糖同步发酵

为构建能够同时高效利用五碳糖和六碳糖发酵产D-乳酸的重组大肠杆菌工程菌,以能高效利用五碳糖发酵产D-乳酸的大肠杆菌工程菌E.coli JH13为出发菌株,通过Red同源重组技术敲除葡萄糖跨膜转运基因pts G。实验结果表明,pts G缺陷菌株E.coli JH15在10%混合糖(5%葡萄糖和5%木糖)培养基中发酵,可同时利用五碳糖和六碳糖以完成发酵;而对照菌葡萄糖消耗完才利用木糖,发酵结束还有18 g/L木糖残留;JH15乳酸产量为83.04 g/L,相比于对照菌株提高了25.86%;在稻草秸秆水解液中发酵,JH15同时利用葡萄糖、木糖和L-阿拉伯糖,乳酸产量为25.15 g/L,转化率为86.42%。JH15作为能利用混合糖同步发酵产D-乳酸的大肠杆菌工程菌,它的成功构建为利用廉价的木质纤维素水解物为原料发酵生产D-乳酸提供参考依据。     

酵母发酵蔗渣半纤维素水解物生产木糖酶

采用二次正交旋转组合设计研究了蔗渣半纤维素水解过程中硫酸浓度与液 固比对木糖收率的影响。回归分析表明 ,这两个因素与木糖的收率之间存在显著的回归关系。通过回归方程优化水解条件 ,当硫酸浓度 2 .4g L ,液 固 =6 .2 ,在蒸汽压力 2 .5× 10 4Pa的条件下水解 2 .5h ,10 0g蔗渣可水解生成木糖约 2 4g。大孔树脂吸附层析处理蔗渣半纤维素水解物 ,能有效地减少其中的酵母生长抑制物含量 ,显著改善水解物的发酵性能。用大孔树脂在pH 2条件下处理过的蔗渣半纤维素水解物作基质 ,含木糖 2 0 0g L ,产木糖醇酵母菌株CandidatropicalisAS2 .1776发酵 110h耗完基质中的木糖 ,生成木糖醇 12 7g L ,产物转化率 0 .6 4(木糖醇g 木糖g) ,产物生成速率 1.15g L·h .     

磁性Fe3O4微粒对葵花籽壳酶水解的影响研究

将磁化后的Fe3O4微粒添加于葵花籽壳酶水解过程中, 分析在不同的Fe3O4添加量和不同的添加方法下, 葵花籽壳酶水解过程中纤维素酶酶活﹑纤维素转化率及还原糖浓度的变化特征, 研究磁性Fe3O4微粒对纤维素酶水解葵花籽壳的影响。并通过考察酶水解反应前后水解液的表面张力值和pH值的变化, 探讨和分析磁性Fe3O4微粒作用下纤维素酶的磁效应机制。结果表明, 磁性Fe3O4添加量为0.5 g/L~2.0 g/L时, 对纤维素酶酶活的提高﹑还原糖浓度的增加和纤维素的转化在48 h后表现出较明显的促进作用。磁性Fe     

Ethanol production from non-starch carbohydrates of wheat bran

Wheat bran (WB), produced worldwide in large quantities as a by-product of the wheat milling industry, constitutes a significant underutilized source of sugars. This paper describes various methods of hydrolyzing the abundant polysaccharides in bran to yield a sugar feedstock suitable for fermentation into bioethanol. Firstly, the starch in the bran was released using amylolytic enzymes. The fibrous material remaining was further hydrolyzed. Acid hydrolysis, heat pretreatment followed by enzymatic hydrolysis and direct enzymatic hydrolysis were compared in terms of total sugar yield and pentose sugar yield. The maximum total sugar yield was achieved when small amounts of acid were added at the pretreatment step prior to enzymatic hydrolysis. This form of pretreatment released most pentosans and significantly enhanced the hydrolysis of cellulose. The overall sugar yield of this combined hydrolysis method reached 80% of the theoretical and it consisted of 13.5 g arabinose, 22.8 g xylose and 16.7 g glucose per 100 g starch-free bran.     

Enhanced acetone-butanol fermentation using repeated fed-batch operation coupled with cell recycle by membrane and simultaneous removal of inhibitory products by adsorption

A novel acetone-butanol production process was developed which integrates a repeated fed-batch fermentation with continuous product removal and cell recycle. The inhibitory product concentrations of the fermentation by Clostridium acetobutylicum were reduced by the simultaneous extraction process using polyvinylpyridine (PVP) as an adsorbent. Because of the reduced inhibition effect, a higher specific cell growth rate and thus a higher product formation rate was achieved. The cell recycle using membrane separation increased the total cell mass density and, therefore, enhanced the reactor productivity. The repeated fed-batchoperation overcame the drawbacks typically associated with a batch operation such as down times, long lag period, and the limitation on the maximum initial substrate concentration allowed due to the substrate inhibition. Unlike a continuous operation, the repeated fed-batch operation could beoperated for a long time at a relatively higher substrate concentration without sacrificing the substrate loss in the effluent. As a result, the integrated process reached 47.2 g/L in the equivalent solvent concentration (including acetone, butanol, and ethanol) and 1.69 g/L . h in the fermentor productivity, on average, over a 239.5-h period. Compared with a controlled traditional batch acetone-butanol fermentation, the equivalent solvent concentration and the tormentor productivity were increased by 140% and 320%, respectively. (c) 1995 John Wiley & Sons Inc.     

Influence of enzyme loading and physical parameters on the enzymatic hydrolysis of steam-pretreated softwood

Softwood is an interesting raw material for the production of fuel ethanol as a result of its high content of hexoses, and it has attracted attention especially in the Northern hemisphere. However, the enzymatic hydrolysis of softwood is not sufficiently efficient for the complete conversion of cellulose to glucose. Since an improvement in the glucose yield is of great importance for the overall economy of the process, the influence of various parameters on the cellulose conversion of steam-pretreated spruce has been investigated. The addition of beta-glucosidase up to 50 IU g(-)(1) cellulose to the enzymatic hydrolysis process resulted in increased cellulose conversion at a cellulase loading up to 48 FPU g(-)(1) cellulose. Despite very high enzyme loading (120 FPU g(-)(1) cellulose) only about 50% of the cellulose in steam-pretreated spruce was converted to glucose when all of the material following pretreatment was used in the hydrolysis step. The influence of temperature, residence time, and pH were investigated for washed pretreated spruce at a dry matter (DM) content of 5% and a cellulase activity of 18.5 FPU g(-)(1) cellulose. The optimal temperature was found to be dependent on both residence time and pH, and the maximum degree of cellulose conversion, 69.2%, was obtained at 38 degrees C and pH 4.9 for a residence time of 144 h. However, when the substrate concentration was changed from 5% to 2% DM, the cellulose conversion increased to 79.7%. An increase from 5% to 10% DM resulted, however, in a similar degree of cellulose conversion, despite a significant increase in the glucose concentration from 23 g L(-)(1) to 45 g L(-)(1). The deactivation of beta-glucosidase increased with increasing residence time and was more pronounced with vigorous agitation.     

The effects of four different pretreatments on enzymatic hydrolysis of sweet sorghum bagasse

Four pretreatment processes including ionic liquids, steam explosion, lime, and dilute acid were used for enzymatic hydrolysis of sweet sorghum bagasse. Compared with the other three pretreatment approaches, steam-explosion pretreatment showed the greatest improvement on enzymatic hydrolysis of the bagasse. The maximum conversion of cellulose and the concentration of glucose obtained from enzymatic hydrolysis of steam explosion bagasse reached 70% and 25 g/L, respectively, which were both 2.5 times higher than those of the control (27% and 11 g/L). The results based on the analysis of SEM photos, FTIR, XRD and NMR detection suggested that both the reduction of crystallite size of cellulose and cellulose degradation from the Iα and Iβ to the Fibril surface cellulose and amorphous cellulose were critical for enzymatic hydrolysis. These pretreatments disrupted the crystal structure of cellulose and increased the available surface area, which made the cellulose better accessible for enzymatic hydrolysis.     

Enzymatic cellulose hydrolysis in an attrition bioreactor combined with an aqueous two-phase system

Cellulose was hydrolyzed in the attrition bioreactor (ABR) with enzyme recycling by employing an aqueous two-phase system (composed of dextran and polyethylene glycol) and an ultrafiltration unit. The ABR combines wet ball milling and enzymatic hydrolysis in one process step. The cellulase enzymes were more stable in the two-phase system than in the normal buffer solution. With the initial substrate concentration (Solka Floe BW200) of 40 g/L and intermittent addition of cellulose, sugar was semicontinuously produced at dilution rates of 0.06 h(-1) and productivities of 2.1 g/L h, which is approximately a 10-fold increase of the previously reported values performed in a regular stirred reactor with an aqueous two-phase system. The conversion of the substrate was 86%.     

Isolation of mesophilic solvent-producing clostridia from Colombian sources: physiological characterization, solvent production and polysaccharide hydrolysis

One hundred and seventy-eight new butanol-acetone producing bacteria related to saccharolytic clostridia were isolated from agricultural sources in Colombia and their fermentation potential was evaluated. Thirteen isolates produced more total solvents from glucose than Clostridium acetobutylicum ATCC 824. The isolates with the highest single solvent production were IBUN 125C and IBUN 18A with 0.46 mol butanol and 0.96 mol ethanol formed from 1 mol glucose, yielding 25. 2 and 29.1 g l(-1) total solvents, respectively, which is close to the maximum values described to date. Most of the new isolates produced exoenzymes for the hydrolysis of starch, carboxymethyl cellulose, xylan, polygalacturonic acid, inulin and chitosan. Together with the high efficiency of solvent production, these hydrolytic isolates may be useful for the direct fermentation of biomass. According to their physiological profile, the most solvent-productive isolates could be classified as strains of C. acetobutylicum, Clostridium beijerinckii, and Clostridium NCP262.     

Genetic modification in cellulose‐synthase reduces crystallinity and improves biochemical conversion to fermentable sugar

The cellulose synthase (CESA) membrane complex synthesizes microfibrils of cellulose that surround all plant cells. Cellulose is made of sugar (β,1‐4 glucan) and accessing the sugar in cellulose for biofuels is of critical importance to stem the use of fossil fuels and avoid competition with food crops and pristine lands associated with starch‐based biofuel production. The recalcitrance of cellulose to enzymatic conversion to a fermentable form of sugar is related to the degree of hydrogen bonding or crystallization of the glucan chain. Herein, we isolate the first viable low biomass‐crystallinity mutant by screening for altered cell wall structure using X‐ray scattering as well as screening for enzymatic conversion efficiency on a range of cell wall mutants in the model plant Arabidopsis thaliana (L.) Heynh. Through detailed analysis of the kinetics of bioconversion we identified a mutant that met both selection criteria. This mutant is ixr1‐2, which contains a mutation in a highly conserved consensus sequence among the C‐terminal transmembrane regions within CESA3. A 34% lower biomass crystallization index and 151% improvement in the efficiency of conversion from raw biomass to fermentable sugars was measured relative to that of wild type (Col‐0). Recognizing the inherent ambiguities with an insoluble complex substrate like cellulose and how little is still understood regarding the regulation of CESA we propose a general model for how to manipulate CESA enzymes to improve the recalcitrance of cellulose to enzymatic hydrolysis. This study also raises intriguing possibilities as to the functional importance of transmembrane anchoring in CESA complex and microfibril formation.     

沙柳原料高浓度底物酶解发酵乙醇工艺

为了提高沙柳生物转化过程的经济可行性,考察了沙柳原料经过蒸爆、超微粉碎+稀酸、超微粉碎+稀碱预处理后高浓度底物补料酶解的效果,并对其高浓度水解糖液进行了乙醇发酵。结果表明:蒸爆处理法水解效果最好,通过补料酶解,底物质量分数可以达到30%,酶解液中总糖质量浓度达到132 g/L,葡萄糖质量浓度105 g/L;超微粉碎+稀酸预处理原料底物质量分数可以达到22%,酶解液中总糖质量浓度达到123 g/L,葡萄糖质量浓度73 g/L;超微粉碎+稀碱预处理原料底物质量分数可以达到22%,酶解液中总糖质量浓度133 g/L,葡萄糖质量浓度77 g/L。3种预处理使沙柳原料的酶解糖液都可以较好地被酿酒酵母利用发酵产乙醇,蒸爆处理原料的酶解糖液乙醇发酵效果最好,乙醇质量浓度达到47 g/L。     

Saccharification of concentrated brewing bagasse slurries with dilute sulfuric acid for producing acetone-butanol by Clostridium acetobutylicum

A comprehensive kinetic study of the acid hydrolysis of concentrated brewing bagasse slurries was performed. The use of the simple series reaction model was found to be suitable when a "heterogeneous correction" (pseudosubstrate-inhibition) is taken into account in slurries with low liquid-to-biomass ratios. Rate constants are shown to be dependent not only on temperature and acid concentration but essentially also on the initial biomass concentration. Actual rate constants, activation energies, and acid and substrate reaction orders are reported for xylan, arabinan, and alpha-glucan acid saccharification. There is a threshold acid loading necessary to overcome the 80% conversion, but no threshold has been found to overcome the "neutralizing" property of cellulosic materials. Reversible acid capture from brewing bagasse has been postulated. The highest monosccharide concentration into hydrolyzates has been found (65 g/L) after 10 h treatment, but economic considerations led us to treat a mean-concentrated slurry (156 g/L) with 0.3M H(2)SO(4) at 96 degrees C, thus obtaining 45.5 g/L monosaccharides in 5 h with 50% less furfural content. After pH regulation only, growth of Clostridium acetobutylicum has been obtained, although complete sugar comsumption has not been achieved. Experiments are now underway to reach complete digestion and to investigate the increase of enzymic accessibility into residual substrate rich in cellulose.