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%。     

萃取耦合技术对玉米秸秆水解液发酵产丁醇的影响

本研究以玉米秸秆水解液为原料,通过萃取发酵技术生产燃料丁醇,以提高丁醇产量,降低生产成本。通过对萃取剂的筛选与条件优化,确定纤维丁醇发酵的萃取剂为油醇,添加时间为发酵0 h,添加比例为1:1 (V/V)。该条件下发酵32 g/L糖浓度的玉米秸秆水解液,丁醇和总溶剂产量分别为3.28 g/L和4.72 g/L,比对照分别提高958.1%和742.9%。以D301树脂脱毒后5%总糖浓度的玉米秸秆水解液进行丁醇萃取发酵,丁醇和总溶剂产量分别达到10.34 g/L和14.72 g/L,发酵得率为0.31 g/g,与混合糖发酵结果相当。研究结果表明萃取发酵技术能够显著提高原料的利用率和丁醇产量,为纤维丁醇工业化生产提供了技术支撑。     

一株拜氏梭菌利用甘蔗废糖蜜发酵生产丙酮丁醇

以甘蔗废糖蜜作为原料,利用Clostridium beijerinckii DSM 6422菌株进行丙酮丁醇发酵的初步研究.结果表明:采用H2SO4预处理糖蜜,初糖质量浓度60 g/L,(NH4)2SO4 2g/L,CaCO3 10 g/L,温度30℃,pH 5.5～7.0,接种量6％(体积分数),在5L发酵罐中发酵培养96 h,总溶剂产量为16.17 g/L,其中丁醇质量浓度为10.07 g/L,总溶剂产率为30.2％,糖利用率为89.3％.     

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。     

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。     

拜氏梭菌13-2发酵甘蔗渣水解液生产丁醇的研究

目的:蔗渣是一种重要的可再生生物质资源,蔗渣原料生产丁醇将大大降低丁醇的成本.方法:实验利用0.25 ～3.0%不同浓度稀H2SO4对蔗渣进行121℃的高温作用1h,以水解液为碳源,进行丁醇的发酵实验.结果:相对于8052菌株,13 -2菌株对甘蔗渣水解液具有更高的发酵效率,在0.5%硫酸用量条件下,13 -2菌株的丁醇发酵量最高,达到4.5g/L.而8052只有2.3g/L的丁醇发酵量.结论:在同等条件下,拜氏梭菌菌株13 -2比模式菌株8052具有更高的溶剂产量和抑制物耐受能力,最佳的蔗渣水解条件为1.5%硫酸用量,丁醇发酵量和总溶剂分别为4.57g/L和5.41 g/L.     

利用甘蔗糖蜜发酵生产花生四烯酸的研究

通过培养高山被孢霉利用糖蜜来发酵生产花生四烯酸(ARA),研究了不同甘蔗糖蜜预处理方法对ARA发酵生产的影响。研究表明:H2SO4法是最利于ARA发酵生产的糖蜜预处理方法。利用预处理的甘蔗糖蜜发酵生产ARA,通过单因素实验设计,确定了最优的培养条件,包括初始还原糖80 g/L,N源6 g/L,接种量20%,初始pH6.0和培养温度25℃,在此条件下发酵,干细胞质量、油脂含量、ARA产量和糖利用率分别达到28.5 g/L、11.7g/L、3.68 g/L和94.5%。     

预处理沙柳酶解液脱毒及其丁醇发酵

为了提高沙柳原料的丁醇发酵效果,考察沙柳原料经过蒸爆、超微粉碎+稀酸和超微粉碎+稀碱预处理后补料酶解的效果,优化了沙柳酶解液活性炭脱毒工艺参数,并对经过脱毒处理的酶解液进行了丁醇发酵研究,结果表明:预处理沙柳原料酶解底物质量浓度为200 g/m L时,3种预处理方法中蒸爆处理法水解效果最好,每克底物的滤纸酶酶加量15 U,酶解96 h后,酶解液总糖质量浓度达到57 g/L。活性炭脱毒处理的最优条件:p H 4.8,碳加量4%(质量分数)、温度70℃、1 h,该条件下的沙柳水解液脱色率达到97.4%、糖损失率3.1%。3种预处理沙柳原料的酶解液经活性炭脱毒后都可以被丁醇梭菌正常利用发酵产丁醇,发酵液总溶剂(ABE)质量浓度约为14 g/L。     

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。     

果糖及葡萄糖混合物为底物的丙酮丁醇发酵

旨在以果糖和葡萄糖混合物模拟能源作物菊芋块茎水解液发酵生产丁醇。在培养基初始pH 5.5,发酵过程不控制pH的混合糖发酵中,出现了发酵提前终止现象,终点残糖浓度达23.26 g/L,而丁醇产量仅5.51 g/L。进一步对比混合糖及葡萄糖、果糖不控制pH的发酵结果表明,导致这一现象的原因可能是有机酸毒性太大和pH太低。全程控制pH的混合糖发酵结果表明,高pH条件有利于提高糖利用率,但产酸多,丁醇产量较低;而低pH条件下发酵残糖较多,但丁醇产量相对较高。基于此,文中采用阶段性pH调控策略,即将发酵初期的pH控     

拜氏梭菌Clostridium beijerinckii NCIMB 8052发酵玉米皮生产丁醇

玉米皮作为玉米淀粉加工的副产物,是一种可用于生产液体燃料的潜在廉价优质的生物质资源。本文以玉米皮为原料,对拜氏梭菌发酵生产丁醇进行了研究。实验结果表明,玉米皮首先在最优的预处理温度140℃下使用0.5%硫酸水溶液以固液比1∶8处理20 min,再添加200 IU/g底物糖化酶、1.0 IU/g底物木聚糖酶进行酶解,可以使原料中的淀粉和半纤维素转化为可发酵糖,此时水解液中的总糖浓度为50.46 g/L。然后使用1.0%的活性炭对水解液进行脱毒处理以去除发酵抑制物,再进行丁醇发酵,丁醇产量为9.72 g/L,总溶剂产量可达14.09 g/L,糖醇转化率为35.1%。上述研究结果证明玉米皮作为一种粮食加工废弃物用于液体燃料丁醇的生产在技术上是完全可行的。     

木薯发酵产丁醇的研究

对丙酮丁醇梭菌发酵木薯产溶剂进行研究,分别考察了N源、木薯含量、酶处理条件和培养基pH对发酵产丁醇的影响。结果表明：最佳的产丁醇发酵培养基为木薯粉120g／L,乙酸铵6g／L;木薯粉先用高温淀粉酶按酶量20U／g、90℃水解60min,再糊化30min;发酵初始pH为6．0,发酵96h。在此条件下,5L发酵罐中丁醇产量达到13．5g／L,总溶剂达到22．8g／L。     

Citric acid production by solid state fermentation using sugarcane bagasse

A solid state fermentation (SSF) method was used to produce citric acid by Aspergillus niger DS 1 using sugarcane bagasse as a carrier and sucrose or molasses based medium as a moistening agent. Initially bagasse and wheat bran were compared as carrier. Bagasse was the most suitable carrier, as it did not show agglomeration after moistening with medium, resulting in better heat and mass transfer during fermentation and higher product yield. Different parameters such as moisture content, particle size, sugar level and methanol concentration of the medium were optimised and 75% moisture level, 31.8 g sugar/100 g dry solid, 4% (v/w) methanol and particles of the size between 1.2 and 1.6 mm were found to be optimal. Sucrose and clarified and non-clarified molasses medium were also tested as moistening agents for SSF and under optimised conditions, 20.2, 19.8 and 17.9 g citric acid /100 g of dry solid with yield of 69.6, 64.5 and 62.4% (based on sugar consumed) was obtained in sucrose, clarified and non-clarified molasses medium respectively, after 9 days of fermentation.     

响应面法优化甘蔗糖蜜发酵产丁醇

以甘蔗糖蜜为底物,用响应面法对高丁醇比突变菌株拜氏梭菌(Clostridium beijerinckii)ART124发酵生产丁醇的培养条件进行优化.首先利用Plackett - Burman试验设计筛选出影响丁醇生产的3个重要因素CaCO3和NH4 HCO3和K2HPO4的用量,再通过最陡爬坡路径逼近最大向应区域,最后根据响应面中心组合设计理论,确定主要影响因素的最佳条件:CaCO3、NH4HCO3和K2HPO4的质量浓度分别为2.65、2.16和0.43 g/L.利用数学模型分析预测得甘蔗糖蜜质量浓度为30 g/L时,最佳的丁醇产量为8.10 g/L,比优化前提高了53.14％.在最佳工艺条件下得到的实验结果与模型预测值很吻合,说明所建立的模型是有效的.     

Bioproduction of butanol in bioreactors: new insights from simultaneous in situ butanol recovery to eliminate product toxicity

Simultaneous acetone butanol ethanol (ABE) fermentation by Clostridium beijerinckii P260 and in situ product recovery was investigated using a vacuum process operated in two modes: continuous and intermittent. Integrated batch fermentations and ABE recovery were conducted at 37 °C using a 14-L bioreactor (7.0 L fermentation volume) containing initial substrate (glucose) concentration of 60 g/L. The bioreactor was connected in series with a condensation system and vacuum pump. Vacuum was applied continuously or intermittently with 1.5 h vacuum sessions separated by 4, 6, and 8 h intervals. A control ABE fermentation experiment was characterized by incomplete glucose utilization due to butanol toxicity to C. beijerinckii P260, while fermentation coupled with in situ recovery by both continuous and intermittent vacuum modes resulted in complete utilization of glucose, greater productivity, improved cell growth, and concentrated recovered ABE stream. These results demonstrate that vacuum technology can be applied to integrated ABE fermentation and recovery even though the boiling point of butanol is greater than that of water.     

Comparative fermentation studies of industrial strains belonging to four species of solvent-producing clostridia

Industrial and culture collection strains of solvent-producing clostridia, classified as Clostridium acetobutylicum, Clostridium beijerinckii, Clostridium saccharobutylicum, and Clostridium saccharoperbutylacetonicum were utilised in a comparative study of fermentation performance in a laboratory fermentation medium, a molasses fermentation medium, and a maize fermentation medium under standardised culture conditions. At least one representative strain was selected from each of the sub-groups within the four species. Preliminary evaluations were first undertaken for the three different fermentation media to determine the most appropriate media formulations, carbohydrate concentrations, and culture conditions for comparison of the solvent-producing ability of these strains. Standardised fermentation media and culture conditions were then selected for each of the comparative fermentation studies. These included TYA medium containing 4% glucose, a supplemented molasses medium containing 6% fermentable sugars, and a supplemented maize mash medium containing 8% maize. Additional comparative fermentation studies on industrial strains belonging to two species of solvent-producing clostridia were carried out in molasses containing higher concentrations of fermentable sugars, and the sugar concentrations supporting maximum levels of solvent production were determined. Although all the strains tested grew in the maize fermentation medium and degraded starch, only a few strains produced consistently high solvent levels. Optimum starch utilisation and solvent production was obtained at a maize concentration of 80 g/l. Pretreatment of the maize by milling or saccharification decreased the buffering capacity of the medium and resulted in decreased solvent production. Decreasing the time used to gelatinise the starch had little effect. Solvent yields and concentrations obtained in this study were compared with various published data in the scientific and patent literature and appeared to closely simulate the results obtained in the industrial fermentation process. The fermentation performances of individual strains could provide useful comparative data for the selection and development of strains for use on various commercial fermentation substrates.     

利用核糖体工程选育丙酮丁醇菌提高丁醇产量

利用核糖体工程技术对丙酮丁醇梭菌Clostridium acetobutylicum L7进行诱变筛选,以获得丁醇高产菌株。使用链霉素诱变C.acetobutylicum L7并结合设计的平板转接逐次提高链霉素浓度的筛选路线,获得丁醇产量较高的菌株S3。结果表明,S3丁醇产量为(12.48±0.03)g/L,乙醇产量为(1.70±0.07)g/L,相对于原始菌分别提高了11.2%及50%;丁醇/葡萄糖转化率由原始菌的0.19提高到0.22,丁醇生产率达到0.24 g/(L.h),相比提高30.5%;耐受丁醇浓度由原始菌的12 g/L提高到14 g/L;发酵液粘度下降到4 mPa/s,同比降低了60%,利于后续分离工作的进行,降低发酵成本。进一步研究工作表明,S3菌株遗传稳定性良好。因此,核糖体工程技术是一种选育丁醇高产菌株的有效方法。     

Enhanced isopropanol and <Emphasis Type="Italic">n</Emphasis>-butanol production by supplying exogenous acetic acid via co-culturing two clostridium strains from cassava bagasse hydrolysate

The focus of this study was to produce isopropanol and butanol (IB) from dilute sulfuric acid treated cassava bagasse hydrolysate (SACBH), and improve IB production by co-culturing Clostridium beijerinckii (C. beijerinckii) with Clostridium tyrobutyricum (C. tyrobutyricum) in an immobilized-cell fermentation system. Concentrated SACBH could be converted to solvents efficiently by immobilized pure culture of C. beijerinckii. Considerable solvent concentrations of 6.19 g/L isopropanol and 12.32 g/L butanol were obtained from batch fermentation, and the total solvent yield and volumetric productivity were 0.42 g/g and 0.30 g/L/h, respectively. Furthermore, the concentrations of isopropanol and butanol increased to 7.63 and 13.26 g/L, respectively, under the immobilized co-culture conditions when concentrated SACBH was used as the carbon source. The concentrations of isopropanol and butanol from the immobilized co-culture fermentation were, respectively, 42.62 and 25.45 % higher than the production resulting from pure culture fermentation. The total solvent yield and volumetric productivity increased to 0.51 g/g and 0.44 g/L/h when co-culture conditions were utilized. Our results indicated that SACBH could be used as an economically favorable carbon source or substrate for IB production using immobilized fermentation. Additionally, IB production could be significantly improved by co-culture immobilization, which provides extracellular acetic acid to C. beijerinckii from C. tyrobutyricum. This study provided a technically feasible and cost-efficient way for IB production using cassava bagasse, which may be suitable for industrial solvent production.