污泥厌氧消化产酸发酵过程中乙酸累积机制

[目的]研究污泥厌氧消化产挥发性脂肪酸(VFA)过程中的有机物碳流的转化机制,阐明乙酸累积机理。[方法]研究溴乙烷磺酸盐(BES)和氯仿(CHCl3)抑制模型下中间代谢产物和气体的累积,检测各产乙酸功能菌群数量,推断污泥产酸发酵过程中的有机物碳流方向和乙酸累积机理。[结果]BES模型乙酸浓度达27 mmol/L,fhs基因拷贝数比对照组高2-3倍,产氢产乙酸菌略有下降。CHCl3模型乙酸浓度达22 mmol/L,fhs基因拷贝数比BES组低一个数量级,产氢产乙酸菌下降明显。[结论]BES特异性较高,除产甲烷菌外对其他厌氧产酸细菌没有影响,乙酸浓度增加并且其主要来源于水解发酵产酸以及同型产乙酸过程。氯仿除抑制产甲烷菌外,对同型乙酸菌和产氢产乙酸菌也有强烈的抑制作用。     

初始pH值对产氢产乙酸/耗氢产乙酸两段耦合工艺定向生产乙酸的影响

以葡萄糖为底物,以经加热预处理并活化过的厌氧污泥为种泥,研究了初始pH值对产氢产乙酸/耗氢产乙酸两段耦合工艺厌氧发酵定向生产乙酸的影响。实验考察了7个初始pH值(5、6、7、8、9、10、11)条件下的底物降解、产物产生和发酵过程pH值的变化。结果表明:产氢产乙酸段初始pH值的变化不仅影响本阶段产酸,而且影响耗氢产乙酸段产酸。初始pH=5时主要进行乙醇型发酵;pH=6和7时主要进行丁酸型发酵;pH=8时混合酸型发酵类型逐渐占优势,pH=8~11时均以乙酸为主要产物,耦合系统生产乙酸最优初始pH值为10。在初始pH=8~11范围内,产氢产乙酸段初期的乙醇浓度一般较高,但到后期因乙醇被微生物进一步代谢转化成乙酸而使其含量下降。     

产气抑制剂对污泥和食品废弃物混合发酵产酸过程的应用研究

为了提高有机酸的浓度,探讨污泥产酸工业化的可行性,考察了三种产气抑制剂对污泥和食 品废弃物混合发酵的VFA浓度及其组成、底物转化率、产气量及产甲烷势的影响.结果表明 ,采用BES、氯仿和碱(pH10)三种手段可以有效抑制发酵后期产气作用,提高底物产酸转化率,并且对有机酸组成也有一定影响.     

污泥厌氧消化中同型产乙酸菌富集研究

在市政污泥厌氧消化过程中,采用三阶段选择性富集同型产乙酸菌,通过监测培养过程中pH值、挥发性脂肪酸、关键酶的活性以及不同碳源利用率等,研究同型产乙酸菌在系统中的累积情况.实验数据表明:经过40 d的富集培养,pH值稳定在8.0,乙酸含量逐渐趋于稳定,占COD的比例为46.4％,同型产乙酸菌对底物的利用率达到了87％,乙酸激酶和乙酰磷酸转移酶呈现明显上升的趋势.结果显示,通过本方法可在市政污泥中有效地富集同型产乙酸菌.     

酸碱调控污泥厌氧发酵实现乙酸累积及微生物种群变化

摘要：【目的】通过对污泥厌氧发酵pH调控,研究挥发性脂肪酸的累积、产酸微生物种群变化及产氢产乙酸菌群对乙酸产生的贡献。【方法】测定不同pH条件下污泥厌氧发酵过程中挥发性脂肪酸的累积;分别应用末端限制性片段长度多态性（T-RFLP）和荧光原位杂交技术（FISH）分析产酸系统中微生物种群结构的变化及产氢产乙酸菌的数量。【结果】 pH为10.0时,有机酸和乙酸的产率在发酵结束时分别达到652.6 mg COD/g-VS和322.4 mg COD/g-VS,显著高于其它pH条件。T-RFLP结果表明,pH值为12     

不同生境微生物转化H2/CO2产乙酸及其在合成气发酵中应用

【目的】合成气发酵对大力开发可再生资源和促进国家可持续发展具有重要意义,研究旨在探究不同生境微生物转化H2/CO2产乙酸及其合成气发酵的潜力。【方法】采集剩余污泥、牛粪、产甲烷污泥和河道底物样品在中温(37 °C)条件下生物转化H2/CO2气体,将来源于牛粪样品的H2/CO2转化富集物用于合成气发酵,通过454高通量技术和定量PCR技术分析复杂微生物群落的组成,GC气相色谱法检测气体转化产生的挥发性脂肪酸(VFAs)浓度。【结果】牛粪和剩余污泥微生物利用H2/CO2气体生成乙酸、乙醇和丁酸等,最高乙酸浓度分别为63 mmol/L和40 mmol/L,明显高于河道底物和产甲烷污泥样品的最高乙酸浓度3 mmol/L和16 mmol/L。牛粪和剩余污泥微生物中含有种类多样化的同型产乙酸菌,剩余污泥中同型产乙酸菌主要为Clostridium spp.、Sporomusa malonica和Acetoanaerobium noterae,牛粪中则为Clostridium spp.、Treponema azotonutricium和Oxobacter pfennigii。【结论】同型产乙酸菌的丰富度和数量两个因素都对复杂微生物群落转化H2/CO2产乙酸效率至关重要;转化H2/CO2得到的富集物可用于合成气发酵产乙酸和乙醇,这为基于混合培养技术的合成气发酵提供了依据。     

不同生境微生物转化H_2/CO_2产乙酸及其在合成气发酵中应用（英文）

【目的】合成气发酵对大力开发可再生资源和促进国家可持续发展具有重要意义,研究旨在探究不同生境微生物转化H_2/CO_2产乙酸及其合成气发酵的潜力。【方法】采集剩余污泥、牛粪、产甲烷污泥和河道底物样品在中温(37°C)条件下生物转化H_2/CO_2气体,将来源于牛粪样品的H_2/CO_2转化富集物用于合成气发酵,通过454高通量技术和定量PCR技术分析复杂微生物群落的组成,GC气相色谱法检测气体转化产生的挥发性脂肪酸(VFAs)浓度。【结果】牛粪和剩余污泥微生物利用H_2/CO_2气体生成乙酸、乙醇和丁酸等,最高乙酸浓度分别为63 mmol/L和40 mmol/L,明显高于河道底物和产甲烷污泥样品的最高乙酸浓度3 mmol/L和16 mmol/L。牛粪和剩余污泥微生物中含有种类多样化的同型产乙酸菌,剩余污泥中同型产乙酸菌主要为Clostridium spp.、Sporomusa malonica和Acetoanaerobium noterae,牛粪中则为Clostridium spp.、Treponema azotonutricium和Oxobacter pfennigii。【结论】同型产乙酸菌的丰富度和数量两个因素都对复杂微生物群落转化H_2/CO_2产乙酸效率至关重要;转化H_2/CO_2得到的富集物可用于合成气发酵产乙酸和乙醇,这为基于混合培养技术的合成气发酵提供了依据。     

活性污泥产酸发酵研究进展

有机物的厌氧生物处理一般经过三个阶段:水解阶段、产酸发酵阶段和产甲烷阶段;研究证明,产酸相不同发酵类型的形成对产甲烷相乃至整个工艺的稳定运行具有至关重要的作用,此外,污泥厌氧消化过程所产生的大量的挥发性脂肪酸(VFAs),如乙酸、丙酸、丁酸及戊酸等,还可作为化工原料用于发酵工业生产各种高附加值产品.近年来,产酸发酵受到越来越多的关注,该文主要对污泥产酸阶段的产酸发酵类型、产酸发酵细菌的生态学、产酸过程的影响因素和生态因子以及产酸发酵的液相末端产物VFAs的测定方法进行了论述.     

外源氧化铁对水稻土中有机酸含量的影响

在水稻土泥浆中添加Fe(OH) 3 可显著降低乙酸浓度 .在新鲜水稻土样品中 ,由于添加Fe(OH) 3导致对乙酸的竞争消耗 ,在培养 5d后 ,乙酸浓度降至 10～ 2 0 μmol·L-1的稳态浓度 ,而此刻对照中的乙酸浓度仍在 12 0 0 μmol·L-1以上 .在乙酸产生量较低的土壤中 ,添加Fe(OH) 3 可完全消耗体系中的乙酸 ,并导致产CH4过程的完全被抑制 .添加纤铁矿同样可使乙酸浓度显著减少 ,但作用效果不如无定形氧化铁 .添加赤铁矿可造成培养初期 (10d以内 )乙酸的大量积累 ,但并不引起产CH4量的增大 .添加Fe(OH) 3 、纤铁矿及铝取代针铁矿 ,能引起厌氧培养的水稻土中丙酸浓度的降低 ,其抑制效率为Fe(OH) 3 >纤铁矿 >铝取代针铁矿 .新鲜土样和经过 11周厌氧处理后的土样中 ,有机酸种类和含量有较大差别 .     

果蔬废弃物两相厌氧发酵产己酸的效能研究

利用厌氧菌群生物合成己酸被认为是一种非常有潜力的新型废弃物资源化技术,但是其合成效能的提高是目前亟待解决的关键问题。本研究以实际果蔬废弃物为原料,对两相厌氧发酵产己酸的效能进行了研究。首先优化接种比以提高酸化相的水解转化效率;在此基础上通过调控醇酸比和pH以强化产己酸相的发酵效能。结果显示,果蔬废弃物厌氧产酸的最佳接种比为2∶1,此时水解率和酸化率分别可达到98.1%和83.2%,乙酸和丁酸产量分别达到5.4 g/L和3.3 g/L。合理控制醇酸比和pH对提高产己酸相的发酵效能非常关键。当醇酸比和pH控制为4∶1和7.5时,己酸生成量可达14.9 g/L,约占液相总COD的80.84%;而低醇酸比和低pH易造成丁酸的累积,从而降低了己酸产量。己酸发酵过程属于非生长偶联型,己酸菌(Clostridium kluyveri)指数增长期伴随着丁酸的生成,而己酸合成主要发生在生长中后期。此外,己酸菌对于pH变化较为敏感,适当提高pH有助于减轻有机酸毒性,提高生物量;但是碱性环境会严重抑制己酸菌的生长繁殖。研究表明,通过分别对酸化相和产己酸相进行优化和调控,两相发酵策略更有利于提高己酸合成效能。     

Competition between reductive acetogenesis and methanogenesis in the pig large-intestinal flora

Washed bacterial suspensions obtained from the pig hindgut were incubated under ¹³CO₂ in a buffer containing NaH¹³CO₃ and carbohydrates. Incorporation of ¹³C into short chain fatty acids was assayed by quantitative nuclear magnetic resonance. The effects of different levels of H₂ added to the gas phase (0, 20 and 80% v/v) and of the specific methanogenesis inhibitor 2-bromoethane-sulphonic acid (BES) were determined. In control incubations increasing the concentration of H₂ markedly increased methane production. Single- and double-labelled acetate and butyrate were formed in all incubations. In the absence of BES, increasing H₂ significantly increased the incorporation of ¹³CO² into butyrate and the proportion of double-labelled acetate in total labelled acetate. The addition of BES proved to be very successful as a methane inhibitor and greatly enhanced the amount of mono- and double-labelled acetate, especially at the highest H₂ partial pressure. The results suggest that methanogenesis inhibited both routes of reductive acetogenesis, i.e. the homoacetate fermentation of hexose (represented for the most part by single labelling) and the synthesis of acetate from external CO₂ and H₂ (represented mostly by double labelling). A highly significant interaction between BES and H₂ concentration was observed. At the highest pH2 BES increased the proportion of labelled acetate in total acetate from 17.1% for the control to 50.9%. It was concluded that although acetogenesis and methanogenesis can occur simultaneously in the pig hindgut, reductive acetogenesis may become a significant pathway of acetate formation in the absence of methanogenesis.     

Effect of 2-bromoethanesulfonic acid and Peptostreptococcus productus ATCC 35244 addition on stimulation of reductive acetogenesis in the ruminal ecosystem by selective inhibition of methanogenesis.

Evidence is provided that reductive acetogenesis can be stimulated in ruminal samples during short-term (24-h) incubations when methanogenesis is inhibited selectively. While addition of the reductive acetogen Peptostreptococcus productus ATCC 35244 alone had no significant influence on CH4 and volatile fatty acid (VFA) production in ruminal samples, the addition of this strain together with 2-bromoethanesulfonic acid (BES) (final concentration, 0.01 or 0.03 mM) resulted in stimulation of acetic acid production and H2 consumption. Since acetate production exceeded amounts that could be attributed to reductive acetogenesis, as measured by H2 consumption, it was found that P. productus also fermented C6 units (glucose and fructose) heterotrophically to mainly acetate (> 99% of the total VFA). Using 14CH3COOH, we concluded that addition of BES and BES plus P. productus did not alter the consumption of acetate in ruminal samples. The addition of P. productus to BES-treated ruminal samples caused supplemental inhibition of CH4 production and stimulation of VFA production, representing a possible energy gain of about 13 to 15%.     

Conversion of sewage sludge into lipids by Lipomyces starkeyi for biodiesel production

The potential of accumulation of lipids by Lipomyces starkeyi when grown on sewage sludge was assessed. On a synthetic medium, accumulation of lipids strongly depended on the C/N ratio. The highest content of lipids was measured at a C/N-ratio of 150 with 68% lipids of the dry matter while at a C/N-ratio of 60 only 40% were accumulated. Within a pH range from 5.0 to 7.5 the highest lipid accumulation was found at pH 5.0 while the highest yield per litre was pH 6.5. Although sewage sludge had no inhibitory effects on growth or accumulation on L. starkeyi when added to synthetic medium, there was no significant growth on untreated sewage sludge. However, pretreatment of sludge by alkaline or acid hydrolysis, thermal or ultrasonic treatment lead to accumulation of lipids by L. starkeyi with highest values of 1 g L(-1) obtained with ultrasound pre-treatment. Based on the content of free fatty acids and phosphorus, lipids accumulated from sewage sludge could serve as a substrate for the production of biodiesel.     

Trophic link between syntrophic acetogens and homoacetogens during the anaerobic acidogenic fermentation of sewage sludge

Acetate production during anaerobic sludge treatment has significant economic and environmental benefits. In this study, trophic links between syntrophic acetogens and homoacetogens in the anaerobic acidogenic fermentation of sewage sludge were investigated using methanogenic inhibitor 2-bromoethanesulfonate (BES) to block the methanogenesis pathway and butyrate to enhance syntrophic acetogenesis. The Gibbs free energies (ΔG) of the butyrate-degrading and homoacetogenic processes were close to the thermodynamic threshold of the reaction activity (−15 kJ/mol). In addition, microbial quantification analysis revealed that the growth of syntrophic acetogenic bacteria and homoacetogens in the treatment incubations was higher than that of the control. The results indicated that hydrogen-producing butyrate degraders are stimulated with homoacetogens when methanogenesis was specifically inhibited.     

废弃活性污泥中产聚羟基脂肪酸酯菌株Bacillus sp. PB-3的发酵条件优化

通过尼罗红染色法结合荧光显微镜镜检,从废弃活性污泥中分离得到1株高产聚羟基脂肪酸酯(PHAs)的菌株Bacillus sp.PB-3,经气相色谱法鉴定该菌株胞内产物为聚β-羟基丁酸酯(PHB)。对培养基成分及发酵条件优化后,获得最佳培养方案:12 g/L的葡萄糖为C源,2 g/L的牛肉膏为N源,初始pH 7.5,培养基装液量80 mL,转速为200 r/min,37℃培养48 h,PHB质量分数可达菌体干质量的32.09%,比优化前提高30%。     

Influence of inoculum activity on the bio-methanization of a kitchen waste under different waste/inoculum ratios

The use of a granular inoculum prevented acidification during the anaerobic batch biodegradation of a kitchen waste for waste/inoculum ratios in the range of 0.5–2.3 g VS/g VS, when the alkalinity/COD ratio was 37 mg NaHCO₃/g COD. In similar experiments but using a suspended sludge with a significantly lower activity, the methane production rates and the biodegradability were significantly lower and the pH decreased below 5.5 at the waste/inoculum ratio of 2.3 g VS/g VS. When the added alkalinity was decreased to 2 mg NaHCO₃/g COD, the ratio waste/inoculum was clearly more important than the inoculum activity, since, irrespective of the sludge used, acidification occurred at waste/inoculum ratios higher than 0.5 g VS/g VS. The advantage of using granular sludge was further investigated in order to define reasonable condition of waste/inoculum ratio and added alkalinity that could be applied in practice. For a waste/inoculum ratio of 1.35, there were no significant differences between the results obtained for the biodegradability and maximum methane production rate (MMPR), when the alkalinity decreased from 44 to 22 mg NaHCO₃/g COD.     

Effects of pH and hydraulic retention time on hydrogen production versus methanogenesis during anaerobic fermentation of organic household solid waste under extreme-thermophilic temperature (70 degrees C)

Two continuously stirred tank reactors were operated with household solid waste at 70 degrees C, for hydrogen and methane production. The individual effect of hydraulic retention time (HRT as 1, 2, 3, 4, and 6 days) at pH 7 or pH (5, 5.5, 6, 6.5, 7) at 3-day HRT was investigated on the hydrogen production versus methanogenesis. It was found that at pH 7, the maximum hydrogen yield was 107 mL-H(2)/g VS(added) (volatile solid added) but no stable hydrogen production was obtained as after some time methanogenesis was initiated at all tested HRTs. This demonstrated that sludge retention time alone was not enough for washing out the methanogens at pH 7 under extreme-thermophilic conditions. Oppositely, we showed that keeping the pH level at 5.5 was enough to inhibit methane and produce hydrogen stably at 3-day HRT. However, the maximum stable hydrogen yield was low at 21 mL-H(2)/g VS(added).     

Enhancement of acetate production by a novel coupled syntrophic acetogenesis with homoacetogenesis process

A novel process was developed and demonstrated that a coupled syntrophic acetogenesis with homoacetogenesis reaction was able to enhance acetate production from high strength synthetic wastewater containing glucose by mixed cultures. A coupling system was constructed with two bioreactors which were connected via a silicon rubber pipe. The first reactor (bioreactor A) was for syntrophic acetogenesis, in which glucose was converted to volatile fatty acids consisting primarily of acetate. The second (bioreactor H) was for homoacetogenesis in which CO₂ and H₂ from bioreactor A were converted to acetate. Acetate yield in the coupling system was 87% higher than that in control 1, in which the homoacetogenesis did not occur. Also, acetate yield in the coupling system was 52% higher than that in control 2, which consisted of only bioreactor A and the gas in the headspace was released manually once a day. Enhancement of acetate production was contributed principally to relieve of the products (H₂ and CO₂) inhibition to syntrophic acetogenesis in bioreactor A, in which the degradation of glucose and the conversion of ethanol were enhanced. This coupling process provides a strategy for increasing acetate production and the degradation rate of the substrate.