产氢菌Enterobacter sp.和Clostridium sp.的分离鉴定及产氢特性

在高温水体中分离得到2株具有较高产氢活性的微生物菌株Z-16和C-32。根据两菌株的16SrDNA序列分析,初步鉴定菌株Z-16为Enterobactersp.,菌株C-32为Clostridiumsp.。研究了起始pH值、反应温度、碳源等对菌株放氢活性的影响。菌株Z-16的最适产氢条件为:反应系统起始pH7·0,反应温度35℃,以蔗糖为产氢底物。在最适条件下,菌株Z-16的氢转化率为2·68molH2/mol蔗糖。菌株C-32的最适产氢条件为:反应系统起始pH8·0,反应温度35℃,以麦芽糖为产氢底物。在最适条件下,菌株C-32的氢转化率为2·71molH2/mol麦芽糖。以葡萄糖为碳源时,菌株Z-16和菌株C-32的氢转化率分别为2·35和2·48molH2/mol葡萄糖。     

产酸克雷伯氏菌耐氧产氢及其可溶性氢酶耐氧特性研究

目的：考察产酸克雷伯氏菌（KZebsielaloxytocaHPl）耐氧产氢特性及其可溶性氢酶的氧耐受特性。方法：研究K．oxytocctHPl在不同气相氧浓度条件下利用葡萄糖（1％,m/v）、丙酮酸钠（0．5％,m／v）及甲酸（0．1％,v／v）等底物产氢活性的以及K．oxyto-07,HPl可溶性氢酶在空气及氧饱和溶液中催化产氢活性。结果：K．oxytocaHP1在葡萄糖（1％,m/v）底物中具有较高耐氧产氢活性,6h内在气相氧浓度为5％、10％和21％条件下的氢产量分别为厌氧条件下的20．9％、13．7％、8．3％;K．oxytoca HP1可溶性氢酶在空气中孵育12h后,其活性残余85．4％,在氧饱和溶液中活性损失一半约3h。结论：试验结果提示K．oxytoca HP1具有耐氧产氢特性,其可溶性氢酶具有较高氧耐受性,在氢能源的开发中具有潜在的应用前景。     

高效产氢菌株Enterococcus sp. LG1的分离及产氢特性

采用Hungate厌氧培养技术分别从厌氧污泥、好氧污泥及河底泥中分离出12株厌氧产氢细菌,并对其中的Enterococcus sp.LG1(注册号:EU258743)进行了研究.结果表明,该株细菌为专性厌氧菌,经革兰氏染色结果为阴性.通过16S rDNA碱基测序和比对证实,该菌株是目前尚未报道过的1个新菌种,初步确定其细菌学上的分类地位.同时,以灭菌预处理的污泥为底物培养基,对该菌的产氢能力及污泥发酵过程中底物性质变化(SCOD、可溶性蛋白质、总糖和pH值等)进行了探讨.实验结果显示,产氢茵Enterococcus sp.LG1的发酵过程中只有H2和CO2产生,无CH4产生.产气量最高为36.48 mL/g TCOD,氢气含量高达73.5%,为已报道文献中以污泥为底物发酵制氢中之最高.根据污泥发酵产物分析得知,该菌的发酵类行为典型的丁酸型发酵.     

厌氧降解丁酸共培养物中产氢产乙酸细菌与产甲烷细菌的分离与再组合

由处理啤酒厂废水的厌氧消化器颗粒污泥中分离和纯化了一个能厌氧降解丁酸产生甲烷的共培养物BF2。共培养物BF2可降解包括异丁酸在内的含4～18个碳原子的脂肪酸,最适生长温度37℃,最适pH7.7。以巴豆酸为底物,成功地将共培养物BF2分离为专性质子还原产乙酸细菌沃尔夫互营单胞菌嗜脂肪亚种菌株CF2和产甲烷细菌甲酸甲烷杆菌菌株MF2两个纯培养,将它们再组合后仍可降解丁酸。菌株CF2与亨氏甲烷螺菌、布氏甲烷短杆菌菌株1125、甲酸甲烷杆菌菌株1535和普通脱硫弧菌G11组合成人工共培养物,可以厌氧降解丁酸。     

一个新的产氢细菌的鉴定及产氢特性的研究

利用Hungate滚管技术从福建省漳州垃圾处理厂厌氧消化器的颗粒污泥中分离到一株产氢的细菌L15。菌株L15为严格厌氧的革兰氏阳性杆菌,菌体大小为0.5μm～0.7μm×2.5μm～5.0μm,以侧生鞭毛运动。在孢肉培养基上产生端生的卵圆形芽孢。温度生长范围15℃～45℃（最适温度30℃～37℃）;pH 范围5.0～8.4（最适pH 6.3～6.8）。该菌株不水解明胶和七叶灵,不还原硫酸盐,牛奶变酸但不凝固,发酵多糖和少数的单糖、双糖和寡糖;发酵葡萄糖的最终产物为乙酸、丁酸、H2和CO2。G+C含量为298mol%。16S rDNA序列分析表明,该菌株属于梭菌的簇Ⅰ,与Clostridium paraputrificum较为接近（相似性为97.1%）。通过生理特征和16S rDNA序列的同源性分析,表明菌株L15应是梭菌属簇Ⅰ中的一个新种,命名为Clostridium defluvii。菌株L15保藏在中国普通微生物菌种保藏中心,保藏号为AS1.3489。菌株L15的最佳产氢温度为34℃、pH为7.0。当葡萄糖浓度为0.4%时,氢气产率可达到1.41mol H2/mol 葡萄糖。该菌可利用下列底物产酸产氢,括号内为产氢率(底物浓度1%)：果糖(1.00mol H2/mol)、麦芽糖(2.17mol H2/mol)、蔗糖(1.69mol H2/mol)、菊糖(4.70mol H2/mol)、糖原(5.49mmol H2/g)、淀粉(7.34mmol H2/g)。     

产氢菌Enterobacter sp.和Clostridium sp.的分离鉴定及产氢特性

在高温水体中分离得到2株具有较高产氢活性的微生物菌株Z-16和C-32。根据两菌株的16S rDNA序列分析,初步鉴定菌株Z-16为Enterobacter sp.,菌株C-32为Clostridium sp.。研究了起始pH值、反应温度、碳源等对菌株放氢活性的影响。菌株Z-16的最适产氢条件为：反应系统起始pH7.0,反应温度35℃,以蔗糖为产氢底物。在最适条件下,菌株Z-16的氢转化率为2.68mol H₂/mol蔗糖。菌株C-32的最适产氢条件为：反应系统起始pH 8.0,反应温度35℃,以麦芽糖为产氢底物。在最适条件下,菌株C-32的氢转化率为2.71mol H₂/mol 麦芽糖。以葡萄糖为碳源时,菌株Z-16和菌株C-32的氢转化率分别为2.35和2.48mol H₂/mol葡萄糖。     

产氢菌Enterobacter sp.和Clostridium sp.的分离鉴定及产氢特性

在高温水体中分离得到2株具有较高产氢活性的微生物菌株Z-16和C-32。根据两菌株的16S rDNA序列分析,初步鉴定菌株Z-16为Enterobacter sp.,菌株C-32为Clostridium sp.。研究了起始pH值、反应温度、碳源等对菌株放氢活性的影响。菌株Z-16的最适产氢条件为：反应系统起始pH7.0,反应温度35℃,以蔗糖为产氢底物。在最适条件下,菌株Z-16的氢转化率为2.68mol H₂/mol蔗糖。菌株C-32的最适产氢条件为：反应系统起始pH 8.0,反应温度35℃,以麦芽糖为产氢底物。在最适条件下,菌株C-32的氢转化率为2.71mol H₂/mol 麦芽糖。以葡萄糖为碳源时,菌株Z-16和菌株C-32的氢转化率分别为2.35和2.48mol H₂/mol葡萄糖。     

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。     

可产酸快生小菌的分离鉴定

目的：鉴定在实验过程中分离到的一株生长快速,并且可以将L-山梨糖转化为2-酮基-L-古龙酸的菌株。方法：将快生小菌传代,并进行产酸、抗菌谱、山梨糖脱氢酶活性等分析,通过PCR方法扩增并分析16S rDNA。结果：在传代过程中还分离得到了不产酸菌株;从快生小菌中扩增得到了普通酮古龙酸菌16S rDNA;从产酸菌中能够扩增得到包含酮古龙酸菌和乙酸钙不动杆菌的16S rDNA序列;在不产酸菌中只检测到乙酸钙不动杆菌的16S rDNA序列。结论：产酸的快生小菌可能是普通酮古龙酸菌和乙酸钙不动杆菌形成的融合细胞,这种融合细胞基因组表现为很不稳定,普通酮古龙酸菌基因组容易丢失,且丢失后也失去了产酸能力。     

一个新的高温产氢菌及产氢特性的研究

利用Hungate滚管技术从西藏山南地区热泉淤泥中分离到一株高温产氢的厌氧发酵细菌T42。菌株T42革兰氏染色反应为阴性,但KOH裂解试验证实其为革兰氏阳性杆菌。菌体大小为0.7μm~0.9μm×3.2μm~7μm,不运动,不产芽孢。其生长温度范围为32℃~69℃,最适生长温度为60℃~62℃,生长pH范围为5.0~8.8,最适生长pH为7.0~7.5,代时30min。有机氮源是T42菌株的必需生长因子。菌株T42利用淀粉、纤维二糖、蔗糖、麦芽糖、糊精、果糖、糖原和海藻糖等底物生长并发酵产氢,发酵葡萄糖的终产物为乙酸、乙醇、H2和CO2。G C含量为31.2mol%。系统发育分析表明菌株T42与Thermobrachium celere和Caloramator indicus位于同一分支,生理生化特征也表明菌株T42应是Thermobrachium属的一个新菌株,在中国普通微生物菌种保藏中心的保藏号为AS1.5039。菌株T42的最佳产氢初始pH为7.2,最佳产氢温度为62℃,其氢转化率为1.06mol H2/mol葡萄糖,最大产氢速率为24.0mmol H2/gDW/h。20mmol/L的Mg2 和2mmol/L的Fe2 可分别提高菌株T42的产氢量20%和23.3%,而Ni2 对其产氢无明显的作用。当菌株T42和热自养甲烷热杆菌(Methanothermobacter thermautotrophicus)Z245共培养时,由于降低了氢分压,使其葡萄糖利用率和氢产量分别提高1倍和2.8倍,发酵产物乙酸和乙醇的比例也从1提高到1.7。     

一株高温高效产氢细菌的分离及产氢特征研究

实验组采用非选择性培养、选择性培养、液体培养和固体培养一整套培养方法,结合平面厌氧操作技术与培养瓶厌氧技术,从混合产氢培养液中分离得到1株较好的产氢细菌。细菌需氧实验证明:此细菌为厌氧细菌;Gram实验和芽孢染色实验表明:此菌为革兰氏阴性杆菌,无芽孢。在不同的pH值、不同金属离子与温度下,于间歇式条件下测定其产氢量。实验结果表明:此菌株对pH值敏感,其最适产氢pH值为5.5,最适温度在45℃左右,在最适宜条件下产气量在1000 mL/(5 g葡萄糖),产气周期在15 d左右。金属离子影响实验表明:缺少铁和镁离子对此产气菌株的产气量有明显影响,此菌株对铜离子(0.1 g/L)无抗性。     

Citric acid production by recycling its wastewater treated with anaerobic digestion and nanofiltration

We have developed an integrated citric acid-methane fermentation process to solve the problem of wastewater pollution in the citric acid industry. Citric acid wastewater was initially treated by anaerobic digestion. After subsequent ultrafiltration and nanofiltration, the anaerobic digestion effluent (ADE) could be recycled as process water for the next fermentation, maintaining excellent citric acid production efficiency while eliminating wastewater discharge and reducing water consumption. Untreated ADE was not suitable for direct recycling. The effects on citric acid fermentation of components in the ADE were investigated. Production was inhibited when Na⁺ and Mg²⁺ concentrations in recycled ADE were >200 mg/L and >40 mg/L, respectively. This problem was resolved by treating the ADE using ultrafiltration and nanofiltration to reduce Na⁺ and Mg²⁺ concentrations to acceptable levels. Our results prove the technical feasibility of cleaner production in the citric acid industry and provide a strategy for management of wastewater in other submerged fermentation industries.     

Development of a pilot scale anaerobic digester for biogas production from cow manure and whey mix

This paper presents results from anaerobic digestion of cow manure and whey mix. A pilot scale anaerobic digester, 128 l in volume, has been developed, to operate under batch and fed-batch conditions. The versatile and unique characteristics of the instrument allowed testing the methane production directly in the farm. The digester performance was evaluated with two calibration tests, the main for a period of 56 days. The study test was divided into three phases, one for each type of feeding operation (batch, fed-batch, batch). The initial phase of digestion resulted in 57 l-CH₄/kg-VS, the second phase had a yield of 86.6 l-CH₄/kg-VS and the third one had a production of 67 l-CH₄/kg-VS. The total methane yield was equal to 211.4 l-CH₄/kg-VS. Using the obtained pilot plant results to a real scale diary production cycle, it was possible to evaluate an electricity production equal to 8.86 kwh per 1 t/d. The conducted tests did show that there is a good potential to the use of a cow manure and whey biomass mix for biogas production.     

Fermentative production of acetic acid from various pure and natural cellulosic materials by Clostridium lentocellum SG6

Clostridium lentocellum SG6 fermented various pure crystalline cellulosic materials efficiently with maximum acetic acid yield (gram acetic acid/gram substrate) of 0.67, at low substrate (8 g l⁻¹) concentration. The strain grew poorly on crude biopolymers but fermented them easily after alkali treatment, when grown with 8 g substrate l⁻¹ concentration of alkali-extracted cotton straw (AECS), paddy straw (AEPS) and sorghum stover (AESS) etc. The acetic acid to substrate (A/S) ratios were similar to those obtained with pure cellulosic materials. An increase in substrate concentration led to a decreased A/S ratio and a decreased percentage of substrate degraded. At high substrate concentration of 75 g filter paper l⁻¹, the strain SG6 converted 63.2 g filter paper into 31.28 g acetic acid l⁻¹. At 100 g l⁻¹ concentrations, AECS and AEPS served as the best substrates for acetic acid production when compared with other biopolymers. A maximum amount of 30.98 and 30.86 g acetic acid was produced from 70.6 g AEPS and 70.1 g AESS l⁻¹ of medium by strain SG6, respectively. Acetic acid production of 0.67 g g⁻¹ pure cellulose (Whatman No. 1 filter paper), 0.63 g g⁻¹ of alkali-treated cotton straw (AECS) are the highest among the cellulolytic bacteria reported so far in mono culture fermentations with pure and native cellulosic materials. This revised version was published online in July 2006 with corrections to the Cover Date.     

Using enriched cultures for elevation of anaerobic syntrophic interactions between acetogens and methanogens in a high-load continuous digester

Volatile fatty acids (VFAs) are key intermediates in anaerobic digestion. Enriched acetogenic and methanogenic cultures were used for syntrophic anaerobic digestion of VFAs in a high-load continuous reactor fed with acetic (HAc), propionic (HPr) and butyric (HBu) acids at maximum concentrations of 5, 3 and 4 g/L, respectively. Interactive effects of HPr, HBu and HAc were analyzed. Furthermore, hydraulic retention time (HRT) and methanogen to acetogen population ratio (M/A) were investigated as key microbiological and operating variables of VFA anaerobic degradations. Optimum conditions were found to be HPr = 1125.0 mg/L, HBu = 1833.4 mg/L, HAc = 1727.4 mg/L, HRT = 21 h and M/A = 2.5 (corresponding to maximum VFA removal and biogas production rate (BPR)). Results of verification experiments and predicted values from fitted correlations were in close agreement at 95% confidence interval. HRT and M/A had positive effects on VFA removal and BPR. M/A was the most important factor that affected BPR. All VFAs inhibited VFA removals.     

Clostridium lentocellum SG6--a potential organism for fermentation of cellulose to acetic acid

A cellulolytic, acetic acid producing anaerobic bacterial isolate, Gram negative, rod-shaped, motile, terminal oval shaped endospore forming bacterium identified as Clostridium lentocellum SG6 based on physiological and biochemical characteristics. It produced acetic acid as a major end product from cellulose fermentation at 37°C and pH 7.2. Acetic acid production was 0.67 g/g cellulose substrate utilized in cellulose mineral salt (CMS) medium. Yeast extract (0.4%) was the best nitrogen source among the various nitrogenous nutrients tested in production medium containing 0.8% cellulose as substrate. No additional vitamins or trace elemental solution were required for acetic acid fermentation. This is the highest acetic acid fermentation yield in monoculture fermentation for direct conversion of cellulose to acetic acid.     

Kinetic characterization in batch and continuous culture of Escherichia coli mutants affected in phosphoenolpyruvate metabolism: differences in acetic acid production

The growth kinetics of an Escherichia coli wild type strain and two derivative mutants were examined in batch cultures and in glucose-limited chemostats. One mutant (PB12) had an inactive phosphotranferase transport system and the other (PB25) had interrupted pykA and pykF genes that code for the two pyruvate kinase isoenzymes. In both batch and continuous culture, important differences in acetic acid accumulation and other metabolic activities were found. Compared to the wild type strain, we observed a reduction in acetic acid accumulation of 25 and 80% in PB25 and PB12 strains respectively, in batch culture. Continuous culture experiments revealed that compared to the other two strains, PB25 accumulated less acetic acid as a function of dilution rate. In continuous cultures, oxidoreductase metabolic activities were substantially affected in the two mutant strains. These changes in turn were reflected in different levels of biomass and CO₂ production, and in oxygen consumption.     

Mixed culture of Saccharomyces cerevisiae and Acetobacter pasteurianus for acetic acid production

Mixed culture of Saccharomyces cerevisiae and Acetobacter pasteurianus was carried out for high yield of acetic acid. Acetic acid production process was divided into three stages. The first stage was the growth of S. cerevisiae and ethanol production, fermentation temperature and aeration rate were controlled at 32 °C and 0.2 vvm, respectively. The second stage was the co-culture of S. cerevisiae and A. pasteurianus, fermentation temperature and aeration rate were maintained at 34 °C and 0.4 vvm, respectively. The third stage was the growth of A. pasteurianus and production of acetic acid, fermentation temperature and aeration rate were controlled at 32 °C and 0.2 vvm, respectively. Inoculation volume of A. pasteurianus and S. cerevisiae was 16% and 0.06%, respectively. The average acetic acid concentration was 52.51 g/L under these optimum conditions. To enhance acetic acid production, a glucose feeding strategy was subsequently employed. When initial glucose concentration was 90 g/L and 120 g/L glucose was fed twice during fermentation, acetic acid concentration reached 66.0 g/L.     

YCA1 participates in the acetic acid induced yeast programmed cell death also in a manner unrelated to its caspase-like activity

Yeast cells lacking the metacaspase-encoding gene YCA1 (Δyca1) were compared with wild-type (WT) cells with respect to the occurrence, nature and time course of acetic-acid triggered death. We show that Δyca1 cells undergo programmed cell death (PCD) with a rate lower than that of the WT and that PCD in WT cells is caused at least in part by the caspase activity of Yca1p. Since in Δyca1 cells this effect is lost, but z-VAD-fmk does not prevent both WT and Δyca1 cell death, PCD in WT cells occurs via a Yca1p caspase and a non-caspase route with similar characteristics.