深红红螺菌吸氢酶缺失突变株在管式光合反应器中的产氢

本研究设计了一种2 L分体式管式光合反应器, 并研究了深红红螺菌(Rhodospirillum rubrum)吸氢酶缺失突变株在该反应器中分别利用人工光源(持续光照与光暗交替)和自然光的产氢规律。结果表明在人工光照条件下R. rubrum的产氢可维持5 d, 持续光照和光暗交替条件下(12 h: 12 h)的氢产量可分别达到5752 mL/PBR ± 158 mL/PBR和5012 mL/PBR ± 202 mL/PBR; 自然光条件下, 最适产氢光照强度为30000 Lux~40000 Lux; 在此光照条件下, R. rubrum产氢可维持6 d~ 10 d, 最高氢产量可达到2800 mL/PBR。尽管利用自然光的氢产量比利用人工光源氢产量低, 但是利用自然光的产氢比较经济, 并且该光合产氢系统操作简单, 该工艺有望开发为低成本的光合细菌产氢技术。     

Microaerobic hydrogen production by photosynthetic bacteria in a double-phase photobioreactor

The rate of hydrogen production by the marine nonsulfur photosynthetic bacterium, Rhodovulum sp., increased with increasing light intensity. A light intensity of 1800 W/m(2) hydrogen production rate was achieved at the rate of 9.4 micromol/mg dry weight/h. The hydrogen production of this strain was enhanced by the addition of a small amount of oxygen (12 micromol O(2)/reactor). Intracellular ATP content was most efficiently accumulated under microaerobic, dark conditions. Hydrogen production rate by Rhodovulum sp. was investigated using a double-phase photobioreactor consisting of light and dark compartments. This rate was compared with data obtained using a conventional photobioreactor. Rhodovulum sp. produced hydrogen at a rate of 0.38+/-0.03 micromol/mg dry weight/h under microaerobic conditions using the double-phase photobioreactor. The hydrogen production rate was four times greater under microaerobic conditions, as compared with anaerobic conditions using either type of photobioreactor. Hydrogen production using a double-phase photobioreactor was demonstrated continuously at the same rate for 150 h.     

Bioconversion of synthesis gas to hydrogen using a light-dependent photosynthetic bacterium,Rhodospirillum rubrum

Biological hydrogen production from synthesis gas was carried out in batch culture. The phototrophic anaerobic bacterium, Rhodospirillum rubrum was used to oxidize CO and water to CO₂ and hydrogen. The bacteria were grown under anaerobic conditions in liquid medium; also acetate was used as carbon source in presence of synthesis gas. Biological hydrogen production was catalysed by R. rubrum via the water–gas shift reaction. A light-dependent cell growth modelled with a desired rate of hydrogen production and CO uptake was determined. The effect of light intensity on microbial cell growth was also studied at 500, 1,000 and 1,500 m.cd. A complete conversion of CO to hydrogen and maximum light efficiency were obtained with an acetate concentration of 1 g/l and light intensity of 500 m.cd. Utilization of the carbon monoxide from the gas phase was often considered as a mass transfer limited process, which needed to diffuse through the gas–liquid interface and then further diffuse into liquid medium prior to reaction. The results from this study showed that maximum cell propagation and hydrogen production were achieved with a limited light intensity of 1,000 m.cd. It was also found that high-light intensity may interfere with cell metabolism. In low-light intensity and substrate concentration, no inhibition was observed, however at extreme conditions, non-competitive inhibition was identified. The adverse effect of high-light intensity was shown at 5,000 m.cd, where the CO conversion drastically dropped to as low as 21%. Maximum CO conversion of 98% and maximum yield of 86% with an acetate concentration of 1.5 g/l and a light intensity of 1,000 m.cd were achieved.     

Acetate as a carbon source for hydrogen production by photosynthetic bacteria

Hydrogen is a clean energy alternative to fossil fuels. Photosynthetic bacteria produce hydrogen from organic compounds by an anaerobic light-dependent electron transfer process. In the present study hydrogen production by three photosynthetic bacterial strains (Rhodopseudomonas sp., Rhodopseudomonas palustris and a non-identified strain), from four different short-chain organic acids (lactate, malate, acetate and butyrate) was investigated. The effect of light intensity on hydrogen production was also studied by supplying two different light intensities, using acetate as the electron donor. Hydrogen production rates and light efficiencies were compared. Rhodopseudomonas sp. produced the highest volume of H2. This strain reached a maximum H2 production rate of 25 ml H2 l(-1) h(-1), under a light intensity of 680 micromol photons m(-2) s(-1), and a maximum light efficiency of 6.2% under a light intensity of 43 micromol photons m(-2) s(-1). Furthermore, a decrease in acetate concentration from 22 to 11 mM resulted in a decrease in the hydrogen evolved from 214 to 27 ml H2 per vessel.     

The effect of light intensity on hydrogen production by sulfur-deprived Chlamydomonas reinhardtii

The effect of light intensity on hydrogen production by sulfur-deprived Chlamydomonas reinhardtii was studied in situ using either long- or short-term experiments, or alternatively, with samples withdrawn from the photobioreactor. Overall hydrogen production by S-deprived culture was shown to depend on the light intensity and to exhibit regions of light limitation and light inhibition. The optimal incident light intensity for hydrogen production was independent of the method of sulfur deprivation or the initial acetate concentration in the medium (12-34 mM). However, it varied with the Chl concentration and the thickness of the photobioreactor. To calculate the average light intensity in the photobioreactor under different experimental conditions, a special mathematics approach was developed. The optimal average light intensity for H(2) production appeared to be 30-40 microE m(-2)s(-1) and was independent of the Chl or acetate concentrations and the method of S deprivation. The inhibitory effect of high light intensity was related to the enhanced O(2) evolution activity during the photosynthetic stage of sulfur deprivation and to the high activity of photosystem II at the beginning of the H(2)-production phase. Data support the major role of photosystem II in supplying reductants through photosystem I to the hydrogenase throughout the H(2)-production phase.     

Simultaneous production of H(2) and O(2) in closed vessels by marine Cyanobacterium anabaena sp. TU37-1 under high-cell-density conditions

A marine cyanobacterium, Anabaena sp. TU37-1, exhibited stable production of hydrogen and oxygen in closed vessels. About 8.4 and 4.3 mL (at atmospheric pressure) of hydrogen and oxygen accumulated, respectively, in flasks with 20 mL gas phase during 48 h incubation. Thus, concentration of H(2) and O(2) became 26 and 13% of the gas phase, respectively. Duration of hydrogen production was prolonged by the periodic gas replacement in the reaction vessel. The conversion efficiencies of photosynthetically active radiation (fluorescent light, 22 W/m(2)) to hydrogen were 2.4 and 2.2% during the initial 12- and 24-h incubation periods, respectively. (c) 1995 John Wiley & Sons, Inc.     

Kinetic modeling of light limitation and sulfur deprivation effects in the induction of hydrogen production with Chlamydomonas reinhardtii. Part II: Definition of model‐based protocols and experimental validation

Photosynthetic hydrogen production under light by the green microalga Chlamydomonas reinhardtii was investigated in a torus‐shaped PBR in sulfur‐deprived conditions. Culture conditions, represented by the dry biomass concentration of the inoculum, sulfate concentration, and incident photon flux density (PFD), were optimized based on a previously published model (Fouchard et al., 2009. Biotechnol Bioeng 102:232–245). This allowed a strictly autotrophic production, whereas the sulfur‐deprived protocol is usually applied in photoheterotrophic conditions. Experimental results combined with additional information from kinetic simulations emphasize effects of sulfur deprivation and light attenuation in the PBR in inducing anoxia and hydrogen production. A broad range of PFD was tested (up to 500 µmol photons m⁻² s⁻¹). Maximum hydrogen productivities were 1.0 ± 0.2 mL H₂/h/L (or 25 ± 5 mL H₂/m² h) and 3.1 mL ± 0.4 H₂/h L (or 77.5 ± 10 mL H₂/m² h), at 110 and 500 µmol photons m⁻² s⁻¹, respectively. These values approached a maximum specific productivity of approximately 1.9 mL ± 0.4 H₂/h/g of biomass dry weight, clearly indicative of a limitation in cell capacity to produce hydrogen. The efficiency of the process and further optimizations are discussed. Biotechnol. Bioeng. 2011;108: 2288–2299. © 2011 Wiley Periodicals, Inc.     

Photoproduction of hydrogen by adapted cells of Chlorella pyrenoidosa

Photoproduction of hydrogen gas by the green alga Chlorella pyrenoidosa was studied in a large scale culture of 2.1. Hydrogen was produced by adding sodium hydrosulfite directly to an algal suspension after anaerobiosis in darkness for activation of hydrogenase. The hydrogen production rate showed a characteristic course of an initial burst of gas then steady production, and this course appeared most clearly at cell concentrations around 0.6–0.7 kg/m³. In the final third phase, the hydrogen production rate gradually decreased until evolution ceased. The steady hydrogen evolution was inhibited 75% by a herbicide, DCMU, which blocks electron flow through photosystem II, indicating that the electron donor for hydrogen production was mainly water. The average light intensity within the culture vessel was measured with a diffusing sphere photoprobe. The rate of hydrogen evolution increased hyperbolically with the average light intensity. The duration of hydrogen photoproduction was shorter at higher light intensity due to the inhibition of hydrogenase by concomitantly released oxygen. The duration was shorter also at higher concentrations of algal suspension. It was foudd that the optimum concentration of algae, about 0.7 kg/m³ in this system, must be selected to maximize the yield of hydrogen.     

Simultaneous hydrogen utilization and in situ biogas upgrading in an anaerobic reactor

The possibility of converting hydrogen to methane and simultaneous upgrading of biogas was investigated in both batch tests and fully mixed biogas reactor, simultaneously fed with manure and hydrogen. Batch experiments showed that hydrogen could be converted to methane by hydrogenotrophic methanogenesis with conversion of more than 90% of the consumed hydrogen to methane. The hydrogen consumption rates were affected by both (hydrogen partial pressure) and mixing intensity. Inhibition of propionate and butyrate degradation by hydrogen (1 atm) was only observed under high mixing intensity (shaking speed 300 rpm). Continuous addition of hydrogen (flow rate of 28.6 mL/(L/h)) to an anaerobic reactor fed with manure, showed that more than 80% of the hydrogen was utilized. The propionate and butyrate level in the reactor was not significantly affected by the hydrogen addition. The methane production rate of the reactor with H₂ addition was 22% higher, compared to the control reactor only fed with manure. The CO₂ content in the produced biogas was only 15%, while it was 38% in the control reactor. However, the addition of hydrogen resulted in increase of pH (from 8.0 to 8.3) due to the consumption of bicarbonate, which subsequently caused slight inhibition of methanogenesis. Biotechnol. Bioeng. 2012; 109:1088–1094. © 2011 Wiley Periodicals, Inc.     

Rhodobacter sphaeroides RV cultivation and hydrogen production in a one- and two-stage chemostat

Rhodobacter sphaeroides RV cultivation and hydrogen production were studied in a one- and two-stage chemostat using lactic acid as substrate. Light saturation was observed when light intensities equal to or above 10 klx were applied. Under light saturation, the two-stage chemostat appeared to be very effective for hydrogen production, allowing complete nitrogen removal by bacterial growth in the first reactor. The hydrogen evolution rate in the second reactor was up to 75 ml H₂ (g dry weight)^–1 h^–1. Accumulation of storage material was observed in the second reactor of the two-stage chemostat under a large carbon excess and limiting light irradiance. The optimal hydraulic residence time was 15 h for both stages, leading to a total hydrogen production about 40% higher than in the one-stage chemostat. Under increasing influent ammonium and yeast extract concentrations, opposite trends of decreasing bacterial activity and increasing concentration resulted in a linear increase of the overall hydrogen production to 1.4–1.6lH₂ (l reactor)^–1 day^–1. Hydrogen production quickly fell when nitrogen was not completely metabolised. The hydrogen evolution rate was also found to depend on lactic acid concentration, and maximum bacterial activity was observed at 100 mM influent lactic acid.     

固定化光合细菌利用有机物产氢的研究

应用固定化细胞技术包埋荚膜红假单胞菌(Rhodopseudomonas capsulata)菌株386．研究在光照下利用有机物产氢的特性。实验观察到,光照培养120小时,悬浮培养物的产氢量为68．2ml·比产氢速率为104．1ml H2/g(生物量)·h;用琼脂包埋后．其产氢能力得到改善,产氢量和比产氢速率分别达到128．4ml和l 9s．8mlH2/g·h。该菌株除可利用苹果酸外,还可利用葡萄糖、乳酸、丙酸等基质高效地产氢。基质浓度只有控制在适当水平时,才具有较高的基质转化产氢效率。此外．菌体生物量、菌龄、培养液pH、光照强度、光照／黑暗时间比以及温度对产氢过程均有不同程度的影响。     

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。     

Hydrogen production by Anabaena variabilis PK84 under simulated outdoor conditions

Hydrogen production by autotrophic, vanadium-grown cells of Anabaena variabilis PK84, a cyanobacterial mutant impaired in the utilization of molecular hydrogen, has been studied under simulated outdoor conditions. The cyanobacterium was cultivated in an automated helical tubular photobioreactor (4.35 L) under air containing 2% CO(2), with alternating 12-h light (36 degrees C) and 12-h dark (14 degrees to 30 degrees C) periods. A. variabilis steadily produced H(2) directly in the photobioreactor during continuous cultivation for 2.5 months. The maximum H(2) production by the continuously aerated culture under light of 332 microE. s(-1). m(-2) was 230 mL per 12-h light period per photobioreactor and was observed at a growth density corresponding to 3.6 to 4.6 microgram Chl a. mL(-1) (1.2 to 1.6 mg dry weight. mL(-1)). Replacement of air with an argon atmosphere enhanced H(2) evolution by a factor of 2. This stimulatory effect was caused mainly by N(2) deprivation in the cell suspension. A short-term decrease of the CO(2) concentration in the air suppressed H(2) evolution. Anoxygenic conditions over the dark periods had a negative effect on H(2) production. The peculiarity of hydrogen production and some physiological characteristics of A. variabilis PK84 during cultivation in the photobioreactor under a light-dark regime are investigated.     

Application of polyethylene glycol immobilized Clostridium sp. LS2 for continuous hydrogen production from palm oil mill effluent in upflow anaerobic sludge blanket reactor

A novel polyethylene glycol (PEG) gel was fabricated and used as a carrier to immobilize Clostridium sp. LS2 for continuous hydrogen production in an upflow anaerobic sludge blanket (UASB) reactor. Palm oil mill effluent (POME) was used as the substrate carbon source. The optimal amount of PEG-immobilized cells for anaerobic hydrogen production was 12% (w/v) in the UASB reactor. The UASB reactor containing immobilized cells was operated at varying hydraulic retention times (HRT) that ranged from 24 to 6 h at 3.3 g chemical oxygen demand (COD)/L/h organic loading rate (OLR), or at OLRs that ranged from 1.6 to 6.6 at 12 h HRT. The best volumetric hydrogen production rate of 336 mL H₂/L/h (or 15.0 mmol/L/h) with a hydrogen yield of 0.35 L H₂/g COD_removed was obtained at a HRT of 12 h and an OLR of 5.0 g COD/L/h. The average hydrogen content of biogas and COD reduction were 52% and 62%, respectively. The major soluble metabolites during hydrogen fermentation were butyric acid followed by acetic acid. It is concluded that the PEG-immobilized cell system developed in this work has great potential for continuous hydrogen production from real wastewater (POME) using the UASB reactor.     

High-density photoautotrophic algal cultures: design, construction, and operation of a novel photobioreactor system

A photobioreactor system has been designed, constructed and implemented to achieve high photosynthetic rates in high-density photoautotrophic algal cell suspensions. This unit is designed for efficient oxygen and biomass production rates, and it also can be used for the production of secreted products. A fiber-optic based optical transmission system that is coupled to an internal light distribution system illuminates the culture volume uniformly, at light intensities of 1.7 mW/cm(2) over a specific surface area of 3.2 cm(2)/cm(3). Uniform light distribution is achieved throughout the reactor without interfering with the flow pattern required to keep the cells in suspension. An on-line ultrafiltration unit exchanges spent with fresh medium, and its use results in very high cell densities, up to 10(9) cells/mL [3% (w/v)] for eukaryotic green alga chlorella vulgaris. DNA histograms obtained form flow cytometric analysis reveal that on-line ultrafiltration influences the growth pattern. Prior to ultrafiltration the cells seem to have at a particular point in the cell cycle where they contain multiple chromosomal equivalents. Following ultrafiltration, these cells divide, and the new cells are committed to division so that cell growth resumes. The Prototype photobioreactor system was operated both in batch and in continuous mode for over 2 months. The measured oxygen production rate of 4-6 mmol/L culture h under continuous operation is consistent with the predicted performance of the unit for the provided light intensity.     

Effects of light/dark cycle, mixing pattern and partial pressure of H2 on biohydrogen production by Rhodobacter sphaeroides ZX-5

The effects of light/dark cycle, mixing pattern and partial pressure of H₂ on the growth and hydrogen production of Rhodobacter sphaeroides ZX-5 were investigated. The results from light/dark cycle culture showed that little or no hydrogen production was observed during the dark periods, and the hydrogen production immediately recovered once illumination was resumed. Also, it was found that the optimum condition of shaking velocity was 120 rpm for hydrogen photo-fermentation. Meanwhile, shaking during H₂ production phase (i.e., cell growth stationary phase) of photo-fermentation played a crucial role on effectively enhancing the phototrophic hydrogen production, rather than that during cell exponential growth phase. The other factor evaluated was hydrogen partial pressure in the culture system. The substrate conversion efficiency increased from 86.07% to 95.56% along with the decrease of the total pressure in the photobioreactor from 1.082 × 10⁵ to 0.944 × 10⁵ Pa, which indicated that reduction of H₂ partial pressure by lowering the operating pressure substantially improved H₂ production in an anaerobic, photo-fermentation process.     

Milking microalga Dunaliella salina for beta-carotene production in two-phase bioreactors

A new method was developed for production of beta-carotene from Dunaliella salina. Cells were grown in low light intensity and then transferred to a production bioreactor illuminated at a higher light intensity. It was a two-phase bioreactor consisting of an aqueous and a biocompatible organic phase. Mixing of the cells and extraction were performed by recirculation of the organic phase. Two experiments were performed. In the first experiment, bioreactors were operated at two different solvent recirculation rates of 150 and 200 mL min(-1). The beta-carotene extraction rate increased significantly at the higher recirculation rate, without exerting any influence on cell number and viability. A second experiment was carried out at a recirculation rate (200 mL min(-1)) appropriate for the study of long-term production of beta-carotene. The results show that D. salina at high light intensity remained viable for a long period (>47 days) in the presence of a biocompatible organic phase; however, cell growth was very slow. beta-Carotene could be continuously extracted to the organic phase; the cells continued to produce beta-carotene and the extracted molecules were continuously reproduced. As a result, beta-carotene was continuously removed ("milked") from the cells. beta-Carotene extraction efficiency in this system was >55%, and productivity was 2.45 mg m(-2) day(-1), much higher than that of commercial plants.     

Single cell protein production of Euglena gracilis and carbon dioxide fixation in an innovative photo-bioreactor

The biological fixation using microalgae has been known as an effective and economical carbon dioxide reduction technology. Carbon dioxide (CO2) fixation by microalgae has been shown to be effective and economical. Among various algae, a species Euglena gracilis was selected as it has advantages such as high protein content and high digestibility for animal feed. A kinetic model was studied in order to determine the relationship between specific growth rate and light intensity. The half-saturation constant for light intensity in the Monod model was 178.7 micromol photons/m2/s. The most favorable initial pH, temperature, and CO2 concentration were found to be 3.5, 27 degrees C, and 5-10% (vol/vol), respectively. Light intensity and hydraulic retention time were tested for effects on cell yield in a laboratory-scale photo-bioreactor of 100l working volume followed by semi-continuous and continuous culture. Subsequently, an innovative pilot-scale photo-bioreactor that used sunlight and flue gas was developed to increase production of this bioresource. The proposed pilot-scale reactor showed improved cell yield compared with the laboratory-scale reactor.     

A perfusion culture system using a stirred ceramic membrane reactor for hyperproduction of IgG2a monoclonal antibody by hybridoma cells

A novel perfusion culture system for efficient production of IgG2a monoclonal antibody (mAb) by hybridoma cells was developed. A ceramic membrane module was constructed and used as a cell retention device installed in a conventional stirred-tank reactor during the perfusion culture. Furthermore, the significance of the control strategy of perfusion rate (volume of fresh medium/working volume of reactor/day, vvd) was investigated. With the highest increasing rate (deltaD, vvd per day, vvdd) of perfusion rate, the maximal viable cell density of 3.5 x 10(7) cells/mL was obtained within 6 days without any limitation and the cell viability was maintained above 95%. At lower deltaD's, the cell growth became limited. Under nutrient-limited condition, the specific cell growth rate (mu) was regulated by deltaD. During the nonlimited growth phase, the specific mAb production rate (qmAb) remained constant at 0.26 +/- 0.02 pg/cell x h in all runs. During the cell growth-limited phase, qmAb was regulated by deltaD within the range of 0.25-0.65 vvdd. Under optimal conditions, qmAb of 0.80 and 2.15 pg/cell x h was obtained during the growth-limited phase and stationary phase, respectively. The overall productivity and yield were 690 mg/L x day and 340 mg/L x medium, respectively. This study demonstrated that this novel perfusion culture system for suspension mammalian cells can support high cell density and efficient mAb production and that deltaD is an important control parameter to regulate and achieve high mAb production.     

Model-based control of feed rate and illuminance in a photosynthetic fed-batch reactor for H2S removal

Traditional application of computer to fermentation processes has focused on the measurement and control of parameters such as temperature, pH, vessel pressure, sparge rate, dissolved oxygen, substrate concentration, and product concentration. In a fed-batch reactor with the photosynthetic green sulfur bacterium Chlorobium thiosulfatophilum which converts hydrogen sulfide to elementary sulfur or sulfate, separate measurement of cell mass concentration and sulfur particle concentration turbidimetrically was difficult due to their combined contributions to the total turbidity. Instead of on-line measurement of many process variables, a model-based control of feed rate and illuminance was designed. Optimal operation condition relating feed rate vs. light intensity was obtained to suppress the accumulation of sulfate and sulfide, and to save light energy in a 4-1 photosynthetic fed-batch reactor. This relation was correlated with the inreasing cell mass concentration. A model which describes the cell growth by considering the light attenuation effects due to scattering and absorption, and to crowding effect of the cells, was established beforehand with the results from the experiments. Based on these optimal operating conditions and the cell growth model, automatic controls of feed rate and illuminance were carried out alternatively to the traditional application of computer to fermentation with on-line measurement, realtime response and adjustment of process variables.List of Symbols F ml/min Flow rate of gas mixture - hV lux Average illuminance - Q mmol/(l h) Removal rate of hydrogen sulfide - X mg protein/l Cell mass concentration as protein - X ₀ mg protein/l Initial cell mass concentration - X _m mg protein/l Maximum cell mass concentration - _a h^–1 Apparent specific growth rate