固定化光合细菌产氢过程的基质利用动力学

研究了固定化荚膜红假单胞菌386、红假单胞菌D两菌株产氢过程基质利用的动力学特性。基质利用与产氢过程以不同的速率进行．琼脂包埋固定化细胞的产氢能力高于海藻酸钙固定化细胞,但最大产氢活性的进程迟于后者。固定化D菌株利用葡萄糖的动力学遵循一级反应,其反应常数K值为1．2×10　2h-1。宏观动力学分析表明,利用基质的产氢过程属于反应控制,扩散传质过程不构成控速步骤。386和D两个菌株固定化细胞生物反应器连续产氢系统,在以乳酸作基质时．平均产氢量分别可达到0．659L／d和0．457L／d,容积(液相)产氢率接近1．OL／L·d。     

固氮螺菌氢代谢与固氮作用的关系I.固氮螺菌放氢现象与吸氢能力的研究

本文研究了固氮螺菌(Azosptrillum brastlense)的放氢现象和吸氢酶活性以及与固氮作用的关系。测定了57株固氮螺菌的放氢现象及其固氮酶活性,其中不放氢41株,微放氢14株,其放氢量为2·63—31.00n mol C2H4／ml菌液·小时。放氢量较多的2株R38{和R256A都是从水稻根表上分离获得,其放氢量分别为185.75n mol H2／ml 菌液·小时和547．00 moIH2／ml 菌液·小时。测定了53株螺菌的吸氢酶活性,它们均具有吸氢能力,其吸氢量各异,0-63-27·38n mol H2／ml菌液。小时。生长在含有NH4CI培养基上的固氮螺菌既没有固氮能力,也不产氢。在无氮培养基上所产生的氢是固氮过程中放出的氢。实验结果指出,C2H2抑制氢酶的活性。当吸氢的菌株与放氢菌株混合培养时,其固氮酶活性比单株纯培养高,有氢存在时,固氮酶活性比不加氢时高。     

红假单胞菌H菌株生长细胞光照放氢条件的研究

本文报道红假单胞菌属（Ｒｈｏｄｏｐｓｅｕｄｏｍｏｎａｓ）Ｈ菌株光照放氢的主要条件。结果表明,Ｈ菌株除利用苹果酸外,还可以利用葡萄糖、丁酸钠、乳酸钠等底物光照放氢,尤以葡萄糖产氢量较高。Ｈ菌株光照放氢的适宜ｐＨ为７．０,与细胞生长最适ｐＨ值一致。可以明显地抑制生长细胞放氢,在气相完全为Ｎ_２条件下,Ｈ菌株仍能以较高速率光照放氢。Ｈ菌株光照放氢的适宜温度为３０℃。空气能抑制光照放氢,加入一定浓度的Ｎａ_２Ｓ可以缓解这种抑制作用。     

金龟子绿僵菌菌株生长环境变量的优化

金龟子绿僵菌(Metarhizium anisopliae var.anisopliae)是一种广谱的昆虫病原真菌,提高菌株的生长速率及产孢量具有重要的意义.分别对2株金龟子绿僵菌菌株MA4与MAlml的菌丝生长及次代产孢具有影响的培养温度、培养基初始pH、装液比、光照及微量元素等环境因素进行了测定.经过优化得到2菌株最佳培养条件分别为:MA4菌株在28℃、pH 7、装液比为75ml/250ml、加入微量元素Mn全光照培养时生长最好、次代产孢量最高;MAlml菌株在28℃、pH9、装液比为75ml/250ml、加入微量元素Cu、黑暗培养时生长最好、次代产孢量最高.     

产氢菌的复合诱变选育及突变株HCM-23的产氢特性

以厌氧产氢细菌Clostridium sp. H-61为原始菌株, 先后经亚硝基胍(NTG)、紫外(UV)诱变, 选育得到1株高产突变株HCM-23。在葡萄糖浓度为10 g/L的条件下, 其产氢量为3024 mL/L, 比原始菌株提高了69.89%; 其最大产氢速率为33.19 mmol H2/g DW·h, 比原始菌株(19.74 mmol H2/g DW·h)提高了68.14%。经过多次传代试验, 稳定性良好。其发酵末端产物以乙醇和乙酸为主, 属于典型乙醇型发酵代谢类型。其最适产氢初始pH为6.5, 最适生长温度为36℃, 以蔗糖为最佳碳源。与原始菌株相比, 突变株HCM-23的产氢特性发生了改变, 如生长延滞期延长, 可利用无机氮源等。     

沼泽红假单胞菌乙酸光合放氢研究

依据光合细菌生长代谢特性和有机废水降解主要产物类型,11种有机物被用于沼泽红假单胞菌（Rhodopseudomonas palustris）Z菌株的光合产氢研究,其中,乙酸反应体系产氢活性最高。在此基础上,研究了该菌株的生长与产氢动力学行为,探求了影响该菌株光合放氢的主要限制性影响因素。结果表明,该菌株产氢与生长部分相关。种子培养基和菌龄对产氢活性有明显影响。细胞最适产氢和生长所需要的光照强度和温度基本一致。当种子来源于硫酸铵高菌龄预培养物或谷氨酸钠对数期预培养物时,该菌株产氢活性显著增加,产氢延滞期明显缩短。氧浓度和接种量对产氢活性也有显著影响。供氢体和氮源浓度直接决定细胞的生长与光放氢活性。在低于70 mmol/L乙酸钠和15 mmol/L谷氨酸钠时,产氢活性随底物浓度的增加而增强。谷氨酸钠浓度高于15mmol/L时,由于游离NH₄⁺的出现,产氢活性受到抑制,但却明显刺激细胞的生长。在标准状况下,该菌株的最大产氢速率可达19.4 mL·L^-1·h^-1。     

产氢紫色非硫光合细菌的分离与筛选

从不同来源的样品中分离到5株紫色非硫光合细菌,从中筛选出2株产氢量较高的菌株——菌株D和菌株H。对其产氢动力学研究表明,在含有20mmol/L谷氨酸钠和50mmol/L D,L-苹果酸培养基中,两株菌可连续稳定产氢5—8d,其产氢速率分别为10.18和20.61μ/h·mg细胞干重。     

光合细菌产氢条件的研究

从被有机物污染的土壤及水域中分离得到13株属于红螺菌科的光合细菌,对其在苹果酸、乳酸、葡萄糖、乙酸、丙酸及丁酸中的光致产氢现象进行了研究。最高产氢量为39.8ml·20ml菌液~(-1)·48h~(-1),产氢活性为7.8ml·g生物量~(-1)·h~(-1)”。底物对不同菌株的产氢量与产氢活性均具有影响,pH对产氢过程也有明显的作用,大于6000lx的光强度对提高产氢活性已无明显作用。固定化细胞在静态培养条件下也能提高产氢能力,但延长产氢时间的作用不明显。     

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。     

铁和镍对光合细菌生长和产氢的影响

基于金属元素在生物体功能发挥中的作用以及它们参与光合细菌光合放氢的重要性,着重进行了铁和镍对沼泽红假单胞菌（Rhodopseudomonas palustris）Z菌株和一株红杆菌（Rhodobactersp.）细胞生长、光合放氢和光合色素合成影响的研究。结果表明,高浓度Fe3+可显著提高两菌株光放氢能力和生物合成能力,最适浓度的Fe3+可使其产氢能力分别达对照组的1.32倍和2.8倍,产氢得率分别为360.6mL/g和385.9 mL/g,生物量分别为对照组的1.42倍和1.54倍。9μmol/L Ni2+的添加可使两菌株产氢能力分别达对照组的1.48倍和1.96倍,产氢得率分别为429.7mL/g和456.3 mL/g。而当Ni2+浓度为12μmol/L时,两菌株的产氢活性受到不同程度的抑制,产氢得率分别降低46.7%和19.4%。在铁浓度相同时,添加6μmol/L Ni2+能明显促进两菌株的生长。而当Ni2+浓度大于6μmol/L时,细胞生长受到抑制。Fe3+和Ni2+对Rhodobactersp.菌株类胡萝卜色素有显著影响。研究结果显示, 426nm色素峰随铁浓度的增加和镍的添加而消失,同时,产氢活性提高。     

Hydrogen production by photoreactive nanoporous latex coatings of nongrowing Rhodopseudomonas palustris CGA009

Nonuniform light distribution is a fundamental limitation to biological hydrogen production by phototrophic bacteria. Numerous light distribution designs and culture conditions have been developed to reduce self-shading and nonuniform reactivity within bioreactors. In this study, highly concentrated (2.0 x 108 CFU/muL formulation) nongrowing Rhodopseudomonas palustris CGA009 were immobilized in thin, nanoporous, latex coatings. The coatings were used to study hydrogen production in an argon atmosphere as a function of coating composition, thickness, and light intensity. These coatings can be generated aerobically or anaerobically and are more reactive than an equivalent number of suspended or settled cells. Rhodopseudomonas palustris latex coatings remained active after hydrated storage for greater than 3 months in the dark and over 1 year when stored at -80 degrees C. The initial hydrogen production rate of the microphotobioreactors containing 6.25 cm2, 58.4 mum thick Rps. palustris latex coatings illuminated by 34.1 PAR mumol photons m-2 s-1 was 6.3 mmol H2 m-2 h-1 and had a final yield of 0.55 mol H2 m-2 in 120 h. A dispersible latex blend has been developed for direct comparison of the specific activity of settled, suspended, and immobilized Rps. palustris.     

Microbial hydrogen production with immobilized sewage sludge

Municipal sewage sludge was immobilized to produce hydrogen gas under anaerobic conditions. Cell immobilization was essentially achieved by gel entrapment approaches, which were physically or chemically modified by addition of activated carbon (AC), polyurethane (PU), and acrylic latex plus silicone (ALSC). The performance of hydrogen fermentation with a variety of immobilized-cell systems was assessed to identify the optimal type of immobilized cells for practical uses. With sucrose as the limiting carbon source, hydrogen production was more efficient with the immobilized-cell system than with the suspended-cell system, and in both cases the predominant soluble metabolites were butyric acid and acetic acid. Addition of activated carbon into alginate gel (denoted as CA/AC cells) enhanced the hydrogen production rate (v(H2)) and substrate-based yield (Y((H2)/sucrose)) by 70% and 52%, respectively, over the conventional alginate-immobilized cells. Further supplementation of polyurethane or acrylic latex/silicone increased the mechanical strength and operation stability of the immobilized cells but caused a decrease in the hydrogen production rate. Kinetic studies show that the dependence of specific hydrogen production rates on the concentration of limiting substrate (sucrose) can be described by Michaelis-Menten model with good agreement. The kinetic analysis suggests that CA/AC cells may contain higher concentration of active biocatalysts for hydrogen production, while PU and ALSC cells had better affinity to the substrate. Acclimation of the immobilized cells led to a remarkable enhancement in v(H2) with a 25-fold increase for CA/AC and ca. 10- to 15-fold increases for PU and ALSC cells. However, the ALSC cells were found to have better durability than PU and CA/AC cells as they allowed stable hydrogen production for over 24 repeated runs.     

Enzymatic synthesis of γ-glutamylmethylamide from L-glutamylhydrazine and methylamine catalysed by immobilized recombinant γ-glutamyltranspeptidase

In many organisms, γ-glutamylmethylamide is a significant amino acid constituent. In this research, a novel method of γ-glutamylmethylamide synthesis is presented. The synthesis of γ-glutamylmethylamide was catalysed by immobilized recombinant γ-glutamyltranspeptidase and used L-glutamylhydrazine as an economical substrate. The optimal enzymes and γ-glutamyltranspeptidase reaction conditions for the production of γ-glutamylmethylamide were 200?mM L-glutamylhydrazine, 1?M methylamine, and 0.1?g/ml immobilized γ-glutamyltranspeptidase cells at pH 10 and 37?°C for 10?h. The immobilized γ-glutamyltranspeptidase cells were used for 10 reactions, and the average conversion ratio from L-glutamylhydrazine to γ-glutamylmethylamide reached 93.2%. The activity of immobilized recombinant γ-glutamyltransferase was not inhibited by 200?mM L-glutamylhydrazine. The immobilized γ-glutamyltranspeptidase cells exhibited favourable operational stability.     

Biological hydrogen production by immobilized cells of Clostridium tyrobutyricum JM1 isolated from a food waste treatment process

A fermentative hydrogen-producing bacterium, Clostridium tyrobutyricum JM1, was isolated from a food waste treating process using 16S rRNA gene sequencing and amplified ribosomal DNA restriction analysis (ARDRA). A fixed-bed bioreactor packed with polyurethane foam as support matrix for the growth of the isolate was operated at different hydraulic retention time (HRT) to evaluate its performance for hydrogen production. The reactor achieved the maximal hydrogen production rate of 7.2 l H(2)l(-1)d(-1) at 2h HRT, where hydrogen content in biogas was 50.0%, and substrate conversion efficiency was 97.4%. The maximum hydrogen yield was 223 ml (g-hexose)(-1) with an influent glucose concentration of 5 g l(-1). Therefore, the immobilized reactor using C. tyrobutyricum JM1 was an effective and stable system for continuous hydrogen production.     

Efficient conversion of wheat straw wastes into biohydrogen gas by cow dung compost

Efficient conversion of wheat straw wastes into biohydrogen gas by cow dung compost was reported for the first time. Batch tests were carried out to analyze influences of several environmental factors on biohydrogen production from wheat straw wastes. The performance of biohydrogen production using the raw wheat straw and HCl pretreated wheat straw was then compared in batch fermentation tests. The maximum cumulative hydrogen yield of 68.1 ml H2/g TVS was observed at 126.5 h, the value is about 136-fold as compared with that of raw wheat straw wastes. The maximum hydrogen production rate of 10.14 ml H2/g TVS h was obtained by a modified Gompertz equation. The hydrogen content in the biogas was 52.0% and there was no significant methane observed in this study. In addition, biodegradation characteristics of the substrate were also discussed. The experimental results showed that the pretreatment of the substrate plays a key role in the conversion of the wheat straw wastes into biohydrogen by the composts generating hydrogen.     

Start‐up of Anaerobic Hydrogen Producing Reactors Seeded with Sewage Sludge

The procedure for starting‐up continuously stirred tank reactors (CSTR) for acclimating anaerobic hydrogen‐producing microorganisms with sewage sludge was investigated. Initially, feeding with glucose and sucrose as well as mixing were carried out in semicontinuous mode; hydraulic retention time (HRT) was in an order of 20, 15, 10, 5, 2.5 and 2 days. When the pH declined to its lowest value (pH 5.18), it was adjusted to 6.7 using sodium hydroxide (1 N). At the same time, the semi‐continuous operation was changed to a continuous one. Finally, the pH was continuously regulated at approximately 6.7. The results indicate that this procedure can be used to cultivate seed sludge for hydrogen production from sewage sludge resulting in a large hydrogen production in less than 60 days. When the substrate was glucose, a hydrogen yield of 1.63 mol H₂/mol glucose and a specific hydrogen production rate of 321 mmol H₂/g VSS day at an HRT of 13.3 h was achieved. When the substrate was sucrose with the same HTR, a hydrogen yield of 4.45 mol H2/mol sucrose and a specific hydrogen production rate of 707 mmol H₂/g VSS day was obtained.     

Continuous production of itaconic acid by Aspergillus terreus immobilized in a porous disk bioreactor

Summary Aspergillus terreus NRRL 1960 was grown on porous disks rotating intermittently in and out of the liquid phase. This immobilized fungal cell bioreactor was used to produce itaconic acid from glucose in a continuous operation. The effect of temperature, pH, disk rotation speed, and feed rate on the itaconic acid concentration and volumetric productivity were studied. The highest itaconic acid concentration and volumetric productivity obtained were 18.2 g/l and 0.73 g/l·h, respectively, under the following conditions: temperature at 36°C, pH 3.0, disk rotation speed at 8 rpm, and feed rate at 60 ml/h. These results are better than those by conventional fermentation or by other immobilized method.Nomenclature F feed rate (l/h) - K _1s saturation constant for immobilized cells (g/l) - K _2s saturation constant for suspended cells (g/l) - M ₁ increased mass of immobilized cells (g) - M ₂ total mass of immobilized cells (g) - P concentration of itaconic acid (g/l) - S substrate concentration in and out of the reactor (g/l) - S ₀ substrate concentration in the feed (g/l) - V liquid volume of the reactor (1) - X concentration of the suspended cells (g/l) - Y ₁ apparent yield of the immobilized cells (g cells/g substrate) - Y ₂ apparent yield of the suspended cells (g cell/g substrate) - Y ₃ apparent yield of itaconic acid (g itaconic acid/g substrate) - m ₁ maintenance and by-products coefficient of the immobilized cells (g substrate/g cell·h) - m ₂ maintenance and by-products coefficient of the suspended cells (g substrate/g cell·h) - µ_1max maximum specific growth rate of the immobilized cells (h^-1) - µ_2max maximum specific growth rate of the suspended cells (h^-1)     

Hydrogen Production by the Photosynthetic Bacterium Rhodospirillum rubrum

Continuous photosynthetic production of hydrogen by Rhodospirillum rubrum in batch cultures was observed up to 80 days with the hydrogen donor, pure lactate or lactic acid-containing wastes, supplied periodically. Hydrogen was produced at an average rate of 6 ml/h per g (dry weight) of cells with whey as a hydrogen donor. In continuous cultures with glutamate as a growth-limiting nitrogen source and lactate as a hydrogen donor, hydrogen was evolved at a rate of 20 ml/h per g (dry weight). The composition of the gas evolved remained practically constant (70 to 75% H₂, 25 to 30% CO₂). Photosynthetic bacteria processing specific organic wastes could be an advantage in large-scale production of hydrogen together with food protein of high value, compared to other biological systems.     

Production of molecular hydrogen with immobilized cells ofRhodospirillum rubrum

Summary Cells ofRhodospirillum rubrum have been immobilized in various gels and tested for photobiological hydrogen production. Agar proved to be the best immobilizing agent with respect to production rates as well as stability. Agar immobilized cells were also superior compared to liquid suspension cultures. Growth conditions of the cells prior to immobilization, e.g. cell age, light intensity or nutrient composition, were of primary importance for the activity in the later immobilized state. A reactor with agar immobilized cells has been operated successfully over 3000 h with a loss of the activity of about 60%. Mean rates for hydrogen production for immobilized cells in this work during the first 60 to 70 hours after immobilization were in the range of 18 to 34 μl H₂ mg⁻¹ d.w. h⁻¹ and thus by a factor of up to 2 higher than liquid cultures under the same conditions. Maximal rates of hydrogen production (57 μl H₂ ml⁻¹ immobilized cell suspension) were reached in agar gel beads with cells immobilized after 70 h growth in liquid culture in the light and a cell density of 1.0 mg ml⁻¹, 70 h after immobilization.     

R-mandelic acid production with immobilized recombinant Escherichia coli cells in a recirculating packed bed reactor

A recirculating packed bed reactor (RPBR) was used for efficient production of R-mandelic acid (R-MA) by kinetic resolution of racemic R,S-mandelonitrile (R,S-MN) using the recombinant E. coli cells crosslinked with diatomite (DA)/glutaraldehyde (GA)/polyethyleneimine (PEI). The performance and productivity of RPBR were evaluated by several parameters, including cell load, substrate feeding rate, height diameter (H/D) ratio, reactor structures, and operation stability. The kinetic resolution process showed higher initial reaction rate (1.52?mM/min) and yield (100%) by recycling 100?mL of substrate solution (70?mM) through RPBR packed with 6.0?g immobilized cells at a substrate-feeding rate of 19?mL/min while the H/D ratio was 2.8. The immobilized cells were successfully applied into kinetic resolution of R,S-MN in the RPBR for 50 batches with an average productivity of 4.12?g/L/h for R-MA with >99% of enantiomeric excess.