牲畜粪便与麦秆混合厌氧发酵的产气量、发酵时间及最优温度

探索牲畜粪便与作物秸秆混合发酵的产气量和发酵时间与发酵温度之间的关系,是解决农村户用沼气原料选择、确定最优发酵温度和提高农作物秸秆资源化利用效率的关键.采用可控型恒温发酵装置,以猪粪、牛粪和麦秆作为发酵原料,以常温厌氧发酵池的底物为接种物,在总固体（total solid,TS）质量分数为8%的条件下进行批量试验,研究了混合发酵的产气量、发酵时间及最优温度.结果表明：粪便与麦秆混合发酵明显提高了原料的产气效率,其中猪粪与麦秆混合发酵的累积产气量比猪粪作为单一发酵原料高24倍,而牛粪与麦杆混合发酵的累积产气量与单一牛粪无显著差异.猪粪、牛粪与麦秆混合发酵的最优温度均在30 ℃以上,发酵时间在60 d左右.厌氧发酵的发酵时间不总是随着温度的升高而缩短,单一以温度来断定厌氧发酵时间的长短是不可行的.     

生物热对传统固态发酵菌群演替及其代谢影响的研究进展

解析传统固态发酵中产生的生物热对微生物菌群代谢的影响,是认识发酵机制、调控发酵过程、保证发酵效率的关键之一。固态发酵过程中,微生物菌群代谢活动所产生的生物热及传热效率低等问题引起微环境温度升高,进而影响微生物的生长与代谢。然而,关于传统固态发酵微生物受生物热的影响及其适应机制仍不明晰。因此,本文以传统固态发酵体系为研究对象,阐述持续生物热介导的高温对固态发酵过程中微生物群落演替和代谢功能的影响,并提出复杂群落中具有多层次调控微生物代谢以适应高温环境的方式,主要从微生物群体与个体层面介绍可能存在的耐热机制。了解生物热对传统固态发酵微生物的影响及潜在的耐热机制,有助于靶向调控发酵过程、强化高温发酵等,以满足未来的工业化需求。     

Novel Method of Lactic Acid Production by Electrodialysis Fermentation

In lactic acid fermentation by Lactobacillus delbrueckii, the produced lactic acid affected the lactic acid productivity. Therefore, for the purpose of alleviating this inhibitory effect, an electrodialysis fermentation method which can continuously remove produced lactic acid from the fermentation broth was applied to this fermentation process. As a result, the continuation of fermentation activity was obtained, and the productivity was three times higher than in non-pH-controlled fermentation. In electrodialysis fermentation, the amount of produced lactic acid was 82.2 g/liter, which was about 5.5 times greater than that produced in non-pH-controlled fermentation. It was concluded that these good results were obtained on account of alleviating the lactic acid inhibitory effect by electrodialysis fermentation. However, the fouling of anion-exchange membranes by cells was observed in electrodialysis fermentation.     

Multi-energy metabolic mechanisms of the fungus Fusarium oxysporum in low oxygen environments

The fungus Fusarium oxysporum produces energy under hypoxic and anoxic conditions by denitrification (nitrate respiration) and ammonia fermentation respectively. Here we found that glucose repressed both of these metabolisms, whereas it supported another anoxic metabolism, hetero-lactic acid fermentation. Ammonia fermentation occurred only after the glucose present in the medium was metabolized to ethanol via alcohol fermentation. During this transition, clear diauxic growth was observed. Glucose regulated the activity of the enzymes involved in ammonia fermentation, hetero-lactic acid fermentation, and denitrification. Highest cell growth was supported by hetero-lactic acid fermentation, followed by denitrification and ammonia fermentation. These results indicate that the energy metabolisms of F. oxysporum are dependent not only on environmental O(2) tension but also on the carbon source, and that ammonia fermentation is an adaptative mechanism acting physiologically as a secondary fermentative mechanism replacing the primary hetero-lactic acid fermentation.     

燃料乙醇发酵技术研究进展

在分析木质纤维素类生物质制备燃料乙醇原理基础上,重点对燃料乙醇转化过程的发酵工艺进行了论述。目前乙醇发酵工艺主要包括直接发酵、分步糖化发酵、同步糖化发酵、同步糖化共发酵和联合生物加工技术等,对这几种技术的研究现状进行了分析并对其发展趋势进行了展望,通过基因工程构建高效发酵菌种的联合生物加工技术将是未来高效发酵工艺的发展趋势,旨在为有效提高发酵菌株的底物代谢能力,获得高的乙醇产量提供重要参考。     

Streptomyces sp.FIM-16-06产他克莫司摇瓶发酵条件的优化

采用单因素试验和正交试验研究发酵培养基组成,优化Streptomyces sp. FIM-16-06产他克莫司的发酵条件,探讨摇瓶发酵的主要影响因子初始p H、装液量、转速等发酵参数的影响。确定了适宜的发酵培养基和发酵参数:6. 0%玉米淀粉、2. 0%黄豆粉、2. 0%葡萄糖和0. 5%玉米浆,初始pH 7. 5,装液量50 m L/500 m L三角瓶,种子菌龄48 h,接种量10%,摇床转速250 r/min,发酵温度27℃,发酵周期7 d。优化后的发酵水平较原生产工艺提高60%以上。他克莫司的优化发酵工艺为其工业化生产奠定了基础。     

Performance comparison of ethanol and butanol production in a continuous and closed-circulating fermentation system with membrane bioreactor

Since both ethanol and butanol fermentations are urgently developed processes with the biofuel-demand increasing, performance comparison of aerobic ethanol fermentation and anerobic butanol fermentation in a continuous and closed-circulating fermentation (CCCF) system was necessary to achieve their fermentation characteristics and further optimize the fermentation process. Fermentation and pervaporation parameters including the average cell concentration, glucose consumption rate, cumulated production concentration, product flux, and separation factor of ethanol fermentation were 11.45?g/L, 3.70?g/L/h, 655.83?g/L, 378.5?g/m²/h, and 4.83, respectively, the corresponding parameters of butanol fermentation were 2.19?g/L, 0.61?g/L/h, 28.03?g/L, 58.56?g/m²/h, and 10.62, respectively. Profiles of fermentation and pervaporation parameters indicated that the intensity and efficiency of ethanol fermentation was higher than butanol fermentation, but the stability of butanol fermentation was superior to ethanol fermentation. Although the two fermentation processes had different features, the performance indicated the application prospect of both ethanol and butanol production by the CCCF system.     

Acetic Acid Production by an Electrodialysis Fermentation Method with a Computerized Control System

In acetic acid fermentation by Acetobacter aceti, the acetic acid produced inhibits the production of acetic acid by this microorganism. To alleviate this inhibitory effect, we developed an electrodialysis fermentation method such that acetic acid is continuously removed from the broth. The fermentation unit has a computerized system for the control of the pH and the concentration of ethanol in the fermentation broth. The electrodialysis fermentation system resulted in improved cell growth and higher productivity over an extended period; the productivity exceeded that from non-pH-controlled fermentation. During electrodialysis fermentation in our system, 97.6 g of acetic acid was produced from 86.0 g of ethanol; the amount of acetic acid was about 2.4 times greater than that produced by non-pH-controlled fermentation (40.1 g of acetic acid produced from 33.8 g of ethanol). Maximum productivity of electrodialysis fermentation in our system was 2.13 g/h, a rate which was 1.35 times higher than that of non-pH-controlled fermentation (1.58 g/h).     

L-缬氨酸的发酵工艺研究

目的:以黄色短杆菌XV0505为生产菌株,探讨发酵培养基和发酵控制条件对L-缬氨酸的产量和糖酸转化率的影响。方法:应用单因素实验确定发酵的工艺条件;利用纸层析-色斑洗脱比色法测定发酵液中L-缬氨酸的含量。结果:在最优发酵条件下,通过10L罐流加发酵72h,产酸量可达53.4g/L,糖酸转化率为26.7%,分别比补料分批发酵提高11.9%和3.5%。结论:环境因子和发酵控制工艺对发酵生产L-缬氨酸具有重要影响。     

农抗120发酵高产培养基优选

采用正交试验浓度加倍的方法 ,进行了农抗 12 0发酵培养基筛选 ,获得两种培养基配方Q1和Q2 。经摇瓶发酵试验 ,发酵水平分别比原始配方提高了 197 3%和 130 9%。摩式自动控制发酵罐试验 ,发酵水平是原始配方的 32 7%和 181%。 2 0M3发酵罐中试 ,发酵水平比原始配方提高了 30 0 0～ 50 0 0单位。     

链霉菌A048产几丁质酶最佳发酵工艺研究

将链霉菌A048在完全培养基中培养至对数生长末期,离心洗涤收集菌丝体,然后接种入发酵产酶培养基中,进行二步发酵工艺牛产几丁质酶,几丁质酶活力比一步发酵工艺提高1．1倍,发酵周期共54h,比一步发酵工艺缩短66h;把菌丝体与几丁质粉共固定化,接入发酵产酶培养基中培养36h,几丁质酶活力比一步发酵工艺提高1．8倍,发酵周期缩短54h;在二步发酵工岂中另添加0．4％纤维素,几丁质酶活力可提高4倍,比一步发酵工艺提高10倍,酶活力达18．52U／mL。采用几丁质和纤维索双因子诱导二步发酵工艺可能是链霉菌A048生产几丁质酶的最佳工艺。     

Production of Botrytis cinerea for potential introduction into a vineyard

Botrytis cinerea was produced in solid-phase fermentation, liquid fermentation and on potato dextrose agar. Stored products were evaluated for grape colonization in grape bioassays and in field trials, and for B. cinerea density using colony forming unit analyses and a nucleic-acid-based method. B. cinerea colony forming unit density was significantly correlated to the probability of successful grape colonization in grape bioassays (p-value=0.0002). Solid fermentation products could be stored longer than liquid fermentation and potato dextrose agar products. There was little difference in the rate of grape colonization in laboratory bioassays among solid-phase fermentation, liquid fermentation and plate culture products. Although the initial B. cinerea colonization rate of field grapes was slightly greater on vines treated with solid-phase fermentation and plate culture products compared to vines treated with product from liquid fermentation, there was no significant difference in final colonization between vines treated with solid-phase fermentation, liquid fermentation and plate culture products and untreated vines.     

微生物发酵青蒿叶和叶渣的研究

为扩大青蒿原料的应用途径,延伸青蒿产业链,对青蒿叶和叶渣进行发酵研究.拟开发可用于动物保健的青蒿来源的产品.采用微生物发酵青蒿及青蒿叶渣,检测枯草芽孢杆菌、酿酒酵母菌、植物乳杆菌等菌株发酵青蒿叶和叶渣后其粗蛋白、粗脂肪、粗纤维素以及青蒿素、青蒿乙素、双氢青蒿酸、青蒿酸含量变化.青蒿叶发酵产物及功效成分含量与对照组比较,...     

Non-sterile fermentations for the economical biochemical conversion of renewable feedstocks

Heavy reliance on petroleum-based products drives continuous exploitation of fossil fuels, and results in serious environmental and climate problems. To address such an issue, there is a shift from petroleum sources to renewable ones. Biochemical conversion via fermentation is a primary platform for converting renewable sources to biofuels and bulk chemicals. In order to provide cost-competitive alternatives, it is imperative to develop efficient, cost-saving, and robust fermentation processes. Non-sterile fermentation offers several benefits compared to sterile fermentation, including elimination of sterility, reduced maintenance requirements, relatively simple bioreactor design, and simplified operation. Thus, cost effectiveness of non-sterile fermentation makes it a practical platform for low cost, large volume production of biofuels and bulk chemicals. Many approaches have been developed to conduct non-sterile fermentation without sacrificing the yields and productivities of fermentation products. This review focuses on the strategies for conducting non-sterile fermentation. The challenges facing non-sterile fermentation are also discussed.     

2-酮-L-古洛酸的补料分批发酵的研究

通过对２－酮－Ｌ－古洛酸的一般发酵与补料分批发酵过程比较研究,发现了补糖分批发酵的一些表观特征,为其发酵控制提供了依据。     

By-product inhibition effects on ethanolic fermentation by Saccharomyces cerevisiae

Inhibition by secondary fermentation products may limit the ultimate productivity of new glucose to ethanol fermentation processes. New processes are under development whereby ethanol is selectively removed from the fermenting broth to eliminate ethanol inhibition effects. These processes can concentrate minor secondary products to the point where they become toxic to the yeast. Vacuum fermentation selectively concentrates nonvolatile products in the fermentation broth. Membrane fermentation systems may concentrate large molecules which are sterically blocked from membrane transport. Extractive fermentation systems, employing nonpolar solvents, may concentrate small organic acids. By-product production rates and inhibition levels in continuous fermentation with Saccharomyces cerevisiae have been determined for acetaldehyde, glycerol, formic, lactic, and acetic acids, 1-propanol, 2-methyl-1-butanol, and 2,3-butanediol to assess the potential effects of these by-products on new fermentation processes. Mechanisms are proposed for the various inhibition effects observed.     

A membrane-integrated fermentation reactor system: its effects in reducing the amount of sub-raw materials for D-lactic acid continuous fermentation by Sporolactobacillus laevolacticus

Continuous fermentation by retaining cells with a membrane-integrated fermentation reactor (MFR) system was found to reduce the amount of supplied sub-raw material. If the amount of sub-raw material can be reduced, continuous fermentation with the MFR system should become a more attractive process for industrialization, due to decreased material costs and loads during the refinement process. Our findings indicate that the production rate decreased when the amount of the sub-raw material was reduced in batch fermentation, but did not decrease during continuous fermentation with Sporolactobacillus laevolacticus. Moreover, continuous fermentation with a reduced amount of sub-raw material resulted in a productivity of 11.2 g/L/h over 800 h. In addition, the index of industrial process applicability used in the MFR system increased by 6.3-fold as compared with the conventional membrane-based fermentation reactor previously reported, suggesting a potential for the industrialization of this D-lactic acid continuous fermentation process.     

郫县豆瓣细菌多样性及群落结构动态变化北大核心

【目的】通过检测郫县豆瓣在不同发酵阶段细菌的种类、丰度及数量,探究郫县豆瓣的不同发酵产品发酵过程中细菌的动态变化情况。【方法】采用16S rRNA基因测序对郫县豆瓣4个发酵阶段中细菌种类及丰度进行分析,利用荧光定量PCR(quantitative real-time PCR,qPCR)方法检测不同发酵阶段的细菌总数。【结果】郫县豆瓣在初期的发酵过程中细菌群落处于动态稳定,在不同发酵阶段细菌群落组成相对丰富,从郫县豆瓣整个初期的发酵过程来看,细菌群落多样性呈现升高的趋势,Shannon指数从1.25升高到3.50;在郫县豆瓣初期发酵过程中细菌群落的数量以及多样性与发酵环境息息相关,不同发酵阶段细菌群落的多样性也有所不同,其中在干辣椒发酵阶段中泛菌属(Pantoea)为最优势菌属,占比为20%;在蚕豆瓣发酵阶段中葡萄球菌属(Staphylococcus)的相对丰度最高,占比为38%;混合发酵后,在红油豆瓣发酵阶段的最优势菌属是乳酸杆菌属(Lactobacillus),占比达到27%,郫县豆瓣发酵阶段的最优势菌属是乳酸杆菌属(Lactobacillus),占比为62%。【结论】推断在郫县豆瓣不同发酵阶段初期相对丰度较大的菌属对郫县豆瓣的质量以及产量可能会产生重大影响。     

红谷霉素生料发酵工艺的研究

红谷霉素是链霉菌702发酵所产的一种生物活性物质,具有较强抗细菌活性。在摇瓶条件下,对链霉菌702生料发酵生产红谷霉素进行研究。采用单因素实验探索生料发酵工艺,筛选出摇瓶生料发酵条件为7.5%的种子接种量和添加抗菌剂1.5ml。在此条件下进行生料发酵,使红谷霉素摇瓶发酵产量达到1.46g/L,比常规灭菌发酵产量提高25.7%,实验结果表明红谷霉素生料发酵是一种潜在可行的发酵方法,不但可以很好的节约发酵成本,还可以提高发酵产量。