纤维素硫酸钠-聚二甲基二烯丙基氯化铵微胶囊固定化Candida krusei产甘油条件优化

研究了利用一种新型的纤维素硫酸钠／聚二甲基二烯丙基氯化铵（Nacs／PDMDAAc）中空微胶囊包埋Can—dida krusei ZJU5205制备甘油的过程。通过摇瓶培养过程中对初始包菌量、胶囊和胶珠、初始甘油浓度、胶囊大小、胶囊体积／发酵液体积等关键固定化参数和培养条件的优化,确立了NaCS／PDMDAAC微胶囊固定化Candida krusei的最佳工艺参数为包菌量为0．6g／L,发酵初加入20g／L甘油,胶囊体积／发酵液体积为0．4。     

氯仿处理厌氧污泥发酵制氢中微生物多样性的解析

研究了不同浓度氯仿对厌氧污泥产氢及其微生物多样性的影响。在氯仿浓度为0.050%时,累积氢、氢气产率、VFA和总糖降解率均达到最大,分别为639mL、1.71molH2/mol消耗葡萄糖、2880mg/L和85%。利用PCR-DGGE技术对不同浓度氯仿处理的污泥样品中微生物多样性和种群结构进行分析显示,4个细菌克隆属于Clostridia,2个细菌克隆分别属于Acidobacteria和δ-proteobacteria,其他4个均属于不可培养细菌。Clostridia中的4个菌群均属产氢菌群,条带7中含有的细菌可能属于HPB。发酵产氢后的污泥样品C3(氯仿浓度=0.05%)中细菌类型主要有:Megasphaera sueciensis、Megasphaera paucivorans、Clostridium cellulosi、Clostridium sp.和不可培养细菌,为最适产氢群落结构。     

厌氧细菌Acetanaerobacterium elongatum从葡萄糖的产氢特性研究

为了了解影响厌氧发酵产氢细菌Acetanaerobacterium elongatumZ7产氢效率的因素,采用生理学方法对其进行了研究。结果表明:乙醇型发酵菌A.elongatumZ7的最适产氢温度为37℃,最适产氢的起始pH为8.0。该菌发酵葡萄糖和阿拉伯糖产氢的能力较强,氢气产率分别为1.55mol H2/mol葡萄糖和1.50mol H2/mol阿拉伯糖。酵母粉是菌株Z7生长和产氢所必须的生长因子;pH影响菌株的生长和葡萄糖利用率;氢压则影响电子流的分配,从而改变代谢产物乙酸和乙醇的比例;当产氢菌与甲烷菌共培养以维持发酵体系低的氢压时,可使氢的理论产量提高约4倍;培养基中乙酸钠浓度>60mmol/L明显抑制产氢。另外,一个只利用蛋白类物质的细菌能够促进菌株Z7对葡萄糖的利用,进而提供氢产量,为生物制氢的工业化生产提供理论参考。     

乳杆菌微胶囊化培养的研究

采用MaCSPDMDAAC微胶囊对两种乳杆菌进行了固定化发酵研究。结果表明,两种乳杆菌能够在微胶囊内很好地生长和繁殖,菌浓度可分别达到18×1011/mL 胶囊和269×1011/mL胶囊,比游离培养高出十倍以上,并且能与游离发酵一样产生乳酸,糖耗时间可缩短1/3～2/3。进行的多批次发酵显示了巨大的产酸能力。     

产氢细菌Enterbacter sakazakii HP的分离及产氢特性

在自然环境中分离到一株具有高产氢活性的微生物菌株,经细菌鉴定仪及16S rRNA基因序列分析,鉴定该菌株为Enterbacter sakazakii HP。分析了起始pH值、反应温度、碳源、起始糖浓度、起始氧浓度及菌体密度等因素对菌株产氢活性的影响。研究表明,该菌株发酵产氢较适合的条件为:以葡萄糖为产氢底物,起始pH值8.0,菌体密度OD600=0.7,反应温度35℃,糖浓度为0.1mol/L,氧浓度为0%的条件下,此时产氢菌株的最高产氢活性为5.34μmolH2/h.mgdw,氢的得率为1.94molH2/mol葡萄糖。     

厌氧细菌Acetanaerobacterium elongatum从葡萄糖的产氢特性研究

为了了解影响厌氧发酵产氢细菌Acetanaerobacterium elongatum Z7产氢效率的因素,采用生理学方法对其进行了研究。结果表明：乙醇型发酵菌A. elongatum Z7的最适产氢温度为37℃, 最适产氢的起始pH为8.0。该菌发酵葡萄糖和阿拉伯糖产氢的能力较强,氢气产率分别为1.55mol H2/mol葡萄糖和1.50mol H2/mol阿拉伯糖。酵母粉是菌株Z7生长和产氢所必须的生长因子;pH影响菌株的生长和葡萄糖利用率;氢压则影响电子流的分配,从而改变代谢产物乙酸和乙醇的比例;当产氢菌与甲烷菌共培养以维持发酵体系低的氢压时,可使氢的理论产量提高约4倍;培养基中乙酸钠浓度> 60mmol/L明显抑制产氢。另外,一个只利用蛋白类物质的细菌能够促进菌株Z7对葡萄糖的利用,进而提供氢产量,为生物制氢的工业化生产提供理论参考。     

木糖发酵产氢菌的筛选及其生长产氢特性研究

利用改进的Hungate厌氧技术, 从牛粪堆肥中分离出一株能有效利用木糖发酵产氢的中温菌HR-1。通过16S rRNA系统发育树分析表明, 菌株 HR-1 与丙酮丁醇梭菌Clostridium acetobutylicum ATCC 824 相似性最高为96%, 结合生理生化和生长特性分析表明, HR-1是梭菌属Clostridium的一个新种, 命名为Clostridium sp. HR-1。菌株HR-1为单胞生长的规则杆状菌(0.3 mm ~0.6 mm)×(1.4 mm~2.3 mm), 革兰氏染色为阴性, 无荚膜、无鞭毛、表面光滑、无明显凸起, 专性厌氧菌。HR-1可在10°C~45°C, pH 4.0~10.0条件下生长; 37°C和pH 8.0分别为其最适生长条件。发酵PYG的主要发酵产物有氢气、二氧化碳、乙酸、丁酸及少量乙醇。HR-1可以利用有机氮源和无机氮源生长并产氢, 酵母提取物是其最佳产氢氮源。HR-1在木糖浓度为3 g/L和初始pH 6.5条件下, 其比产氢量为1.84 mol-H2/mol-木糖, 最大比产氢速率为10.52 mmol H2/h·g-细胞干重。HR-1可以亦利用葡萄糖、半乳糖、纤维二糖、甘露糖和果糖等碳源生长并发酵产氢, 发酵葡萄糖时比产氢量为2.36 mol-H2/mol-葡萄糖。     

保加利亚乳杆菌微胶囊化工艺研究

目的制备保加利亚乳杆菌微胶囊,提高菌株的酸、热耐受性及降低菌体的分离成本。方法以保加利亚乳杆菌(Lactobacillus bulgaricus)为研究对象,海藻酸钠(SA)为壳材、CaCl2为固化剂,制备保加利亚乳杆菌微胶囊;包埋率、颗粒平均化程度、机械强度等为考核指标,研究保加利亚乳杆菌微胶囊化的工艺。结果当海藻酸钠浓度为0.75%、CaCl2浓度为3%、电压为600V、泵速为1.96mL/min、震动频率为80Hz时,微胶囊化包埋效果最佳,经固定化后的菌微胶囊保持了良好的保加利亚乳杆菌的活性,微囊化保加利亚乳杆菌经过2次连续发酵后的产酸量分别达到59.4g/L和55.8g/L。结论本研究为工业化生产乳酸提供了一条具有经济价值的途径。     

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。     

十三碳二元酸发酵过程产酸期拟均相动力学模型及其应用

分析了十三碳二元酸发酵过程中产酸期的代谢特点,对产酸期四相体系发酵动力学进行了研究。提出了菌体生长、产物形成及底物消耗的动力学模型,对模型参数进行了回归估值,并对产酸期进行了拟合,结果表明,模型的计算值和实测值较为吻合,平均相对偏差为3．6％。利用所建模型对产酸期进行了多种操作条件下的模拟计算,结果表明,提高进入产酸期的菌体浓度、缩短菌体生长期时间及降低发酵液中产物浓度具有提高产物形成速率的有效途径。     

NaCS‐PDMDAAC immobilized cultivation of recombinant Dictyostelium discoideum for soluble human Fas ligand production

Dictyostelium discoideum is a promising eukaryotic host for the expression of heterologous proteins requiring post‐translational modifications. However, the dilute nature of D. discoideum cell culture limits applications for high value proteins production. D. discoideum cells, entrapped in sodium cellulose sulfate/poly‐dimethyl‐diallyl‐ammonium chloride (NaCS‐PDMDAAC) capsules were used for biosynthesis of the heterologous protein, soluble human Fas ligand (hFasL). Semi‐continuous cultivations with capsules recycling were carried out in shake flasks. Also, a scaled‐up cultivation of immobilized D. discoideum for hFasL production in a customized vitreous airlift bioreactor was conducted. The results show that NaCS‐PDMDAAC capsules have desirable biophysical properties including biocompatibility with the D. discoideum cells and good mechanical stability throughout the duration of cultivation. A maximum cell density of 2.02 × 10⁷ cells mL^?1 (equivalent to a maximum cell density of 2.22 × 10⁸ cells mL^?1 in capsules) and a hFasL concentration of 130.40 μg L^?1 (equivalent to a hFasL concentration of 1434.40 μg L^?1 in capsules) were obtained in shake flask cultivation with capsules recycling. Also, a maximum cell density of 1.72 × 10⁷cells mL^?1 (equivalent to a maximum cell density of 1.89 × 10⁸ cells mL^?1 in capsules) and a hFasL concentration of 106.10 μg L^?1 (equivalent to a hFasL concentration of 1167.10 μg L^?1 in capsules) were obtained after ～170 h cultivation in the airlift bioreactor (with a working volume of 200 mL in a 315 mL bioreactor). As the article presents a premier work in the application of NaCS‐PDMDAAC immobilized D. discoideum cells for the production of hFasL, more work is required to further optimize the system to generate higher cell densities and hFasL titers for large‐scale applications. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 31:424–430, 2015     

Rapid formation of hydrogen-producing granules in an anaerobic continuous stirred tank reactor induced by acid incubation

A novel approach to rapidly initiate granulation of hydrogen-producing sludge was developed in an anaerobic continuous stirred tank reactor at 37 degrees C. To induce microbial granulation, the acclimated culture was subject to an acid incubation for 24 h by shifting the culture pH from 5.5 to 2.0. The culture was resumed to pH 5.5 after the incubation and the reactor was operated at hydraulic retention times (HRTs) of 12, 6, 2, 1, and 0.5 h in sequence. Microbial aggregation took place immediately with the initiation of acid incubation and granules were developed at 114 h. No granule was observed in the absence of acid incubation in the control test. Changing the culture pH resulted in improvement in surface physicochemical properties of the culture favoring microbial granulation. The zeta potential increased from -11.6 to -3.5 mV, hydrophobicity in terms of contact angle improved from 31 degrees to 43 degrees and extracellular proteins/polysaccharides ratio increased from 0.2 to 0.5-0.8. Formation of granular sludge facilitated biomass retention of up to 32.2 g-VSS/L and enhanced hydrogen production. The hydrogen production rate and hydrogen yield increased with the reduction in HRT at an influent glucose concentration of 10 g/L once steady granular sludge layer was formed, achieving the respective peaks of 3.20 L/L x h and 1.81 mol-H(2)/mol-glucose at 0.5 h HRT. The experimental results suggested that acid incubation was able to initiate the rapid formation of hydrogen-producing granules by regulating the surface characteristics of microbial aggregates in a well-mixed reactor, which enhanced the hydrogen production.     

Co-production of biomass and metabolites by cell retention culture of <Emphasis Type="Italic">Leuconostoc citreum</Emphasis>

Cell retention culture of lactic acid bacterium Leuconostoc citreum was carried out in a fermentor equipped with an internal ceramic filtration system to co-produce biomass and metabolites. The filtration system was composed of porous ceramic filter module with pore size of 0.1 μm and total surface area of 330 cm². High cell density cultivation of L. citreum was achieved within the fermentor, while extracellular metabolites such as mannitol and d-lactic acid were produced through the filter with high productivities. In batch culture of L. citreum using a medium containing 50 g/L of glucose and 100 g/L of fructose, the maximum optical density (OD) monitored at 660 nm was 13 with 65 g/L of mannitol and 38 g/L of lactic acid. In cell retention culture of L. citreum with dilution rate of 0.07 h⁻¹, OD increased to 75, which was 6 times higher than that in batch culture. The concentrations of mannitol and lactic acid increased to 85 and 45 g/L, respectively, and were maintained throughout the cultivation to 105 h. By increasing dilution rate to 0.13 h⁻¹, the productivities of mannitol and lactic acid increased to 8.5 and 4.2 g/L/h, respectively, which were 2.7 to 3 times higher than those in batch culture, suggesting that cell retention culture using internal filtration system is highly effective for co-production of useful cell biomass and various extracellular metabolites.     

Influence of substrate concentration on the stability and yield of continuous biohydrogen production

The effect of substrate concentration (sucrose) on the stability and yield of a continuous fermentative process producing hydrogen was studied. High substrate concentrations are attractive from an energy standpoint as they would minimise the energy required for heating. The reactor was a CSTR; temperature was maintained at 35 degrees C; pH was controlled between 5.2 and 5.3, and the hydraulic retention time (HRT) was 12 h. Online measurements were taken for ORP, pH, temperature, %CO2, gas output and %H2, and data logged using a MatLAB data acquisition toolbox. Steady-state operation was obtained at 10, 20 and 40 g/L of sucrose in the influent, but a subsequent step change to 50 g/L was unsustainable. The hydrogen content ranged between 50% and 60%. The yield of hydrogen decreased as the substrate concentration increased from 1.7 +/- 0.2 mol/mol hexose added at 10 g/L, to 0.8 +/- 0.1 mol/mol at 50 g/L. Sparging with nitrogen improved the hydrogen yield by at least 35% at 40 g/L and at least 33% at 50 g/L sucrose. Sparging also enabled steady-state operation at 50 g/L sucrose. Addition of an extra 4 g/L of n-butyric acid to the reactor operating at 40 g/L sucrose increased the butyrate concentration from 9,830 to 18,900 mg/L, immediately stopping gas production and initiating the production of propionate, whilst the addition of 2 g/L taking the butyrate concentration to 12,200 mg/L did not do so. It was shown that operation at 50 g/L sucrose in a CSTR in butyrate fermentation is possible.     

Production of succinate by a <Emphasis Type="Italic">pfl</Emphasis>B <Emphasis Type="Italic">ldh</Emphasis>A double mutant of <Emphasis Type="Italic">Escherichia coli</Emphasis> overexpressing malate dehydrogenase

The gene encoding malate dehydrogenase (MDH) was overexpressed in a pflB ldhA double mutant of Escherichia coli, NZN111, for succinic acid production. With MDH overexpression, NZN111/pTrc99A-mdh restored the ability to metabolize glucose anaerobically and 0.55 g/L of succinic acid was produced from 3 g/L of glucose in shake flask culture. When supplied with 10 g/L of sodium bicarbonate (NaHCO₃), the succinic acid yield of NZN111/pTrc99A-mdh reached 1.14 mol/mol glucose. Supply of NaHCO₃ also improved succinic acid production by the control strain, NZN111/pTrc99A. Measurement of key enzymes activities revealed that phosphoenolpyruvate (PEP) carboxykinase and PEP carboxylase in addition to MDH played important roles. Two-stage culture of NZN111/pTrc99A-mdh was carried out in a 5-L bioreactor and 12.2 g/L of succinic acid were produced from 15.6 g/L of glucose. Fed-batch culture was also performed, and the succinic acid concentration reached 31.9 g/L with a yield of 1.19 mol/mol glucose.     

K562 cell growth activity and metabolism characteristics in APA microencapsulated culture and modeling study

Cell microencapsulation is likely to play a major role in cell and transplantation therapies in the next decade. The microcapsules provide a special microenvironment in which cells always have different behaviors compared with free non-encapsulated culture. In this work, the behaviors of K562 leukemia cells were studied once entrapped in solid and liquefied APA microcapsules as well as in free non-encapsulated culture. Glucose pulse culture was employed to characterize the growth and metabolism of microencapsulated K562 cells. And mathematical modeling was presented to develop a basis for the deeper understanding of cells responses to different culture environments. Based on the results of experiments and modeling, it was found that cells presented a better growing pattern and maintain the activity at a higher level for extending time. The concentration of lactate was higher in solid microcapsules culture than that of liquefied microcapsules culture, but the cell number was lower. And the lactate yield coefficients (lactate/glucose) were 0.8129, 0.6978 and 0.601 for free non-encapsulated, solid microcapsules and liquefied microcapsules culture, respectively. An increase of glucose concentration led a decrease of cell activity, The glucose consumption ratio were 99.9%, 86.8%, 49.4% and 28.6% with the decrease in its concentration from 2 to 4, 6, 10 g/L, however, the lactate yield coefficient were 0.7184, 0.6654, 0.8239 and 0.9693, respectively.     

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.     

Fedbatch operation using Clostridium acetobutylicum suspension culture as biocatalyst for enhancing hydrogen production

We demonstrated the feasibility of fedbatch operation using Clostridium acetobutylicum suspension culture as a biocatalyst for the continuous production of hydrogen. The optimum operating pH and temperature of the current cultivation system for hydrogen production were pH 6.0 and 37 degrees C, respectively. The volumetric loading of the bioreactor for hydrogen production can be as high as 650 mmol hydrogen/L culture with a yield at approximately 2.0 mol hydrogen/mol glucose. Acetate and butyrate made up approximately 80% of the total metabolites. The inhibitory effect from the two metabolites on the hydrogen production process was investigated. Butyrate at a concentration higher than 13 g/L significantly inhibited not only cell growth but also hydrogen production (i.e., specific hydrogen production rate). Acetate appears to be less toxic than butyrate to the hydrogen production process. While significantly inhibiting cell growth, acetate hardly affected hydrogen production. Finally, the factors limiting cultivation performance were discussed and possible strategies for enhancing the production of hydrogen were proposed.     

Optimization of bio-hydrogen production from biodiesel wastes by Klebsiella pneumoniae

Biodiesel wastes containing glycerol were utilized by Klebsiella pneumoniae DSM 2026 to produce hydrogen. The optimization of medium components was performed using both Plackett-Burman and uniform design methods. Using the Plackett-Burman design, glycerol, yeast extract, NH(4)Cl, KCl and CaCl2 were found to be the most important components, which were further investigated by uniform design and second-order polynomial stepwise regression analysis. The optimized medium containing 20.4 g.L(-1) glycerol, 5.7 g.L(-1) KCl, 13.8 g.L(-1) NH(4)Cl, 1.5 g.L(-1) CaCl(2) and 3.0 g.L(-1) yeast extract resulted in 5.0-fold increased level of hydrogen (57.6 mL/50 mL medium) production compared to initial level (11.6 mL/50 mL medium) after 24 h of fermentation The optimization of fermentation condition (pH, temperature and inoculum) was also conducted. When the strain grew in the optimized medium under optimal fermentation condition in a 5-L stirred tank bioreactor for batch production, hydrogen yield and production reached 0.53 mol/mol and 117.8 mmol/L, respectively. The maximum hydrogen evolution rate was 17.8 mmol/(L.h). Furthermore, 1,3-propanediol (6.7 g.L(-1)) was also obtained from the liquid medium as a by-product.     

Process development of itaconic acid production by a natural wild type strain of <Emphasis Type="Italic">Aspergillus terreus</Emphasis> to reach industrially relevant final titers

Itaconic acid is a promising organic acid and is commercially produced by submerged fermentation of Aspergillus terreus. The cultivation process of the sensitive filamentous fungus has been studied intensively since 1932, with respect to fermentation media components, oxygen supply, shearing rate, pH value, or culture method. Whereas increased final titers were achieved over the years, the productivity has so far remained quite low. In this study, the impact of the pH on the itaconic acid production was investigated in detail. The pH during the growth and production phase had a significant influence on the final itaconic acid concentration and pellet diameter. The highest itaconic acid concentration of 160 g/L was achieved at a 1.5-L scale within 6.7 days by raising and controlling the pH value to pH 3.4 in the production phase. An ammonia solution and an increased phosphate concentration were used with an itaconic acid yield of 0.46 (w/w) and an overall productivity of 0.99 g/L/h in a fed-batch mode. A cultivation with a lower phosphate concentration resulted in an equal final concentration with an increased yield of 0.58 (w/w) after 11.8 days and an overall productivity of 0.57 g/L/h. This optimized process was successfully transferred from a 1.5-L scale to a 15-L scale. After 9.7 days, comparable pellet morphology and a final concentration of 150 g/L itaconic acid was reached. This paper provides a process strategy to yield a final titer of itaconic acid from a wild-type strain of A. terreus which is in the same range as the well-known citric acid production.