光生物反应器脱除空气中CO2的模型研究

微藻光生物反应器具有脱除空气中CO₂能力。从光生物反应器构型、进气流速、混合传质,及微藻光合/呼吸速率等方面,探讨气升式光生物反应器脱除空气中CO₂效果,提出了时间离散化和集中参数法两种分析方法。运用集中参数法建立了气升式柱型光生物反应器脱除CO₂的数学模型,模拟了藻液中溶氧浓度（DO）、pH随时间的变化情况,及进气CO₂浓度影响,预测并验证了光照条件下出气CO₂、O2浓度的变化趋势。模拟结果和实验数据基本吻合,所提出的模型对光生物反应器的优化设计、微藻的高密度培养,及CO2去除能力预测具有参考意义。     

利用市政废水和火电厂烟道气大规模培养高油微藻

对高含油量微藻(Scenedesmus dimorphus)培养的生物反应器进行了比较,阐述了市政废水净化处理和火电厂烟道废气利用,研究了S.dimorphus微藻在2种不同的光生物反应器中的生长特性、其移除废水中N.P养分能力及其CO2消耗情况.研究结果表明:S.dimorphus微藻的生长受pH、通气速率、搅拌情况和光照条件等的影响.当通气速率(空气)为6 L/min, S.dimorphus的生长速率达到高峰.通入体积分数33.3% CO2和体积分数 66.7% 空气比通入正常空气或通入比其含有更多CO2的空气更有利于微藻的生长.获得最大微藻生长速率的pH上限是7.5.螺旋状生物反应器比锥型瓶生物反应器更有利于微藻的生长,这主要归功于前者有更高的光利用效率和搅拌效果的改善.S.dimorphus 微藻能利用市政废水中的养分从而移出其中的N.P养分.在6 d的培养中,培养液中的N换算成NO-3从8.3 mg/L下降到3.6 mg/L以下;而P换算成PO3-4则从0.24 mg/L下降到0.03 mg/L 以下.     

微藻固定CO2研究进展

空气中CO2浓度升高所导致的温室效应已成为重大的环境问题,受到人们普遍关注.概述了高效固定CO2微藻藻种的筛选和培养方法,分析了微藻固定CO2的无机碳利用形式和浓缩机制,讨论了高效光生物反应器设计和运行目标,简要介绍了微藻(酶)-膜生物反应器集成新技术.并认为今后的研究方向主要是在进一步探索微藻固定CO2有关机理的基础上,构建高效固定CO2的转基因微藻,开发高效膜生物反应集成系统.     

一种用于微藻培养的新型板式光生物反应器

微藻的闪光效应可以大幅提高微藻的光效率,提高微藻产量。通过在传统的板式光生物反应器中加入斜挡板以增强微藻的闪光效应。以小球藻为模型藻种,考察了新型板式光生物反应器内不同光强和不同进口流速对小球藻生长速率和光效率的影响。结果表明,当进口流速为0.16 m/s时,随着光强的提高,小球藻的细胞浓度逐渐增加,光效率逐渐降低;在500μmol/(m2·s)的光强条件下,小球藻细胞浓度和光效率均随着进口流速的提高而增加。新型板式光生物反应器内小球藻的细胞浓度比传统板式光生物反应器提高了39.23%,表明在传统板式光生物反应器内加入斜挡板可有效增强微藻的闪光效应。     

封闭式光生物反应器研究进展

国际上80～90年代,封闭式光生物反应器是微藻生物技术的重要研究热点,也是微藻生物技术产业化的关键技术之一。本文较全面地介绍了用于微藻大规模培养的封闭式光生物反应器研究现状。将封闭式光生物反应器分为柱式、管式、板式和光导纤维反应器等类型。工业放大前景的管式和板式光生物反应器采取了典型个案分析的方法,列表比较了典型反应器的主要技术参数,并对它们的技术发展趋势进行了归纳总结。     

产油微藻自养培养条件调控

作为新兴生物燃料的生物柴油近年来发展迅速,以微藻为代表的第二代生物能源是解决能源危机的长远之计,但如何提高其产量仍是研究的热点问题。以提高产油自养微藻生物量和油脂含量为目的,在气升式光反应器中运用均匀设计实验方法进行了条件优化试验。分别得出了氮原子浓度、通气速率、二氧化碳体积浓度和光照强度4个因素对小球藻C2生物量积累和油脂含量影响的显著回归方程和反应器优化培养条件。以生物量为指标的优化培养条件是:氮原子浓度0.178 g/L,通气速率5 L/min,二氧化碳体积浓度3%(V/V),光照强度6000 lx。该优化条件下,生物量为2.11 g/L,即生产速率为0.352 g/(L.d),比测试实验中检测到的最高生物量[1.88 g/L,即生产速率为0.313 g/(L.d)]提高了12.2%;以油脂含量为指标的优化培养条件是:进气速率0.400 L/min,二氧化碳体积浓度1.94%(V/V),得到油脂含量为22.4%,比测试实验中检测到的最高油脂量(20.7%)提高7.7%。     

响应面法优化自养小球藻产生物柴油油脂

利用响应面法对小球藻(Chlorella vulgaris)在2L气升式生物反应器中对自养产生物柴油油脂的培养条件进行了优化。首先用Plackett-Burman方法对10个相关影响因素的效应进行评价并筛选出对产油有显著影响的3个因素:KNO3浓度、温度和CO2浓度;再用最陡爬坡实验逼近最大产油区域;最后由中心组合实验及响应面分析确定了影响产油主要因素的最佳条件为:KNO3浓度0.31g/L,温度26.5℃,CO2浓度6.80%,最高产油量达到0.42g/L,比优化前提高了近2倍。优化后,在10L气升式生物反应器中进行了扩大培养。     

转小鼠金属硫蛋白-Ⅰ基因聚球藻7002的生长潜力分析

以野生聚球藻7002为对照,从室温吸收光谱、光合放氧速率、生长动力学参数以及气升式光生物反应器中的生长特性阐述了转小鼠金属硫蛋白-Ⅰ基因聚球藻7002的生长优势和培养潜力.结果表明:转MT聚球藻室温可见光光谱吸收峰比野生藻略高;最大净光合速率和饱和光强比野生藻高,呼吸速率和补偿光强比野生藻低;转MT聚球藻摇瓶培养的最大细胞浓度为野生藻的1.74倍,具有较高的细胞生长速率;气升式光生物反应器有利于转MT基因聚球藻生长潜力的发挥.     

转小鼠金属硫蛋白-Ⅰ基因聚球藻7002的生长潜力分析

以野生聚球藻7002为对照, 从室温吸收光谱、光合放氧速率、生长动力学参数以及气升式光生物反应器中的生长特性阐述了转小鼠金属硫蛋白-Ⅰ基因聚球藻7002的生长优势和培养潜力。结果表明: 转MT聚球藻室温可见光光谱吸收峰比野生藻略高; 最大净光合速率和饱和光强比野生藻高, 呼吸速率和补偿光强比野生藻低; 转MT聚球藻摇瓶培养的最大细胞浓度为野生藻的1.74倍, 具有较高的细胞生长速率; 气升式光生物反应器有利于转MT基因聚球藻生长潜力的发挥。     

磁处理光生物反应器的研制及其应用研究

开发出一种新型气升式外环流磁处理光生物反应器,将其应用于钝顶螺旋藻的高细胞密度培养,并从光合作用的角度对磁致生物效应机理进行了初步探讨。光生物反应器主要由反应器主体（气升管道、下降管、除气室）、在线检测与控制系统,以及磁处理、光照、热交换和供所系统组成。结果表明,采用该生物反应器在０＜Ｈ＜３２０ｋＡ／ｍ的磁场强度范围内培养钝顶螺旋藻,不仅能显著加快藻细胞生长速度,而且可提高最大细胞干重浓度。钝顶螺     

Short-term evaluation of the photosynthetic activity of an alkaliphilic microalgae consortium in a novel tubular closed photobioreactor

A novel lab-scale tubular closed photobioreactor was developed and used for the assessment of the photosynthetic activity of an alkaliphilic microalgae mixed consortium under non-substrate limitation (i.e., bicarbonate excess), controlled irradiance, and mixing conditions. Two prominent haloalkaliphilic strains were identified as members of the consortium: Halospirulina sp. and Picochlorum sp. The photobioreactor (vol?=?0.5 L) consists of two interconnected U-shaped borosilicate glass tubes (internal diameter 2 cm) reaching a surface/volume ratio of 200 m² m^?3. This configuration specifically addressed the issue of the homogeneous light distribution among the microalgae suspended cells cultured by using fixed equidistant cool white light LEDs nearby the surface of the glass tubes. A soft homogeneous pneumatic mixing (i.e., airlift) was implemented in the culture fostering Reynolds numbers around 3000. The photosynthetic activity of the microalgae consortium was evaluated during different short-term kinetic assays by fitting the dynamics of the dissolved oxygen concentration to an oxygenic kinetic model. The photobioreactor operated in a closed loop allowed to control the produced oxygen by the extraction of the cumulated gas in the headspace. The use of this novel photobioreactor allowed the photosynthetic activity of microalgae suspended cells to be assessed, where the dissolved oxygen concentration and irradiance were the main parameters affecting the oxygenic rates under alkaline pH.     

Microalgae bulk growth model with application to industrial scale systems

The scalability of microalgae growth systems is a primary research topic in anticipation of the commercialization of microalgae-based biofuels. To date, there is little published data on the productivity of microalgae in growth systems that are scalable to commercially viable footprints. To inform the development of more detailed assessments of industrial-scale microalgae biofuel processes, this paper presents the construction and validation of a model of microalgae biomass and lipid accumulation in an outdoor, industrial-scale photobioreactor. The model incorporates a time-resolved simulation of microalgae growth and lipid accumulation based on solar irradiation, species specific characteristics, and photobioreactor geometry. The model is validated with 9 weeks of growth data from an industrially-scaled outdoor photobioreactor. Discussion focuses on the sensitivity of the model input parameters, a comparison of predicted microalgae productivity to the literature, and an analysis of the implications of this more detailed growth model on microalgae biofuels lifecycle assessment studies.     

氧化铝气体分布器应用小球藻培养的研究

光生物反应器设计中,气体分布器对微藻生长有较大的影响,尤其是在鼓泡式光生物反应器中更为显著。实验考察了采用氧化铝烧制的多孔气体分布器的5L鼓泡式光生物反应器中通气速率、CO₂ 浓度对小球藻LICME002生物量、叶绿素含量、油脂积累的影响。对该气体分布器下的CO₂浓度和通气速率对小球藻的作用机理进行了初步的探讨。结果表明,CO₂浓度为3%时,该株微藻生物量、叶绿素、油脂积累的最佳;CO₂浓度超过6%时各项指标显著下降。通过对0.1vvm,0.4vvm,0.7vvm、1.0vvm的通气速条件下的各项指标的分析,确定最佳通气条件为0.4vvm。结论显示,在最佳通气速率和CO₂浓度下,微藻生物量能达到1.52g/L,油脂含量达到31.5%。     

微藻培养系统内光现象的研究进展

分析了微藻培养系统内光传递过程的数学模型和光分布影响因素,重点综述了光暗循环对微藻生长影响的实验研究和CFD技术应用研究进展,展望了微藻培养系统内光现象的发展方向,以期为规模化、高效微藻培养光生物反应器的设计、优化和放大提供参考。     

Photosynthetic performance of a helical tubular photobioreactor incorporating the cyanobacterium spirulina platensis

The photosynthetic performance of a helical tubular photobioreactor ("Biocoil"), incorporating the filamentous cyanobacterium Spirulina platensis, was investigated. The photobioreactor was constructed in a cylindrical shape (0.9 m high) with a 0.25-m(2)basal area and a photostage comprising 60 m of transparent PVC tubing of 1.6-cm inner diameter (volume = 12.1 L). The inner surface of the cylinder (area = 1.32 m(2)) was illuminated with cool white fluorescent lamps; the energy input of photosynthetically active radiation(PAR, 400 to 700 nm) into the photobioreactor was 2920 kJ per day. An air-lift system ncorporating 4%CO(2) was used to circulate the growth medium in the tubing. The maximum productivity achieved in batch culture was 7.18 g dry biomass per day [0.51 g . d biomass/L . day, or 5.44 g . d biomass/m(2)(inner surface of cylindrical shape)/day] which corresponded to a photosynthetic (PAR) efficiency of 5.45%. The CO(2) was efficiently removed from the gaseous stream; monitoring the CO(2) the outlet and inlet gas streams showed a 70% removal of CO(2) from the inlet gas over an 8-h period with almost maximum growth rate. (c) 1995 John Wiley & Sons, Inc.     

The air‐lift photobioreactors with flow patterning for high‐density cultures of microalgae and carbon dioxide removal

A photobioreactor containing microalgae is a highly efficient system for converting carbon dioxide (CO₂) into biomass. Using a microalgal photobioreactor as a CO₂ mitigation system is a practical approach to the problem of CO₂ emission from waste gas. In this study, a marine microalga, Chlorella sp. NCTU‐2, was applied to assess biomass production and CO₂ removal. Three types of photobioreactors were designed and used: (i) without inner column (i.e. a bubble column), (ii) with a centric‐tube column and (iii) with a porous centric‐tube column. The specific growth rates (μ) of the batch cultures in the bubble column, the centric‐tube and the porous centric‐tube photobioreactor were 0.180, 0.226 and 0.252 day^?1, respectively. The porous centric‐tube photobioreactor, operated in semicontinuous culture mode with 10% CO₂ aeration, was evaluated. The results show that the maximum biomass productivity was 0.61 g/L when one fourth of the culture broth was recovered every 2 days. The CO₂ removal efficiency was also determined by measuring the influent and effluent loads at different aeration rates and cell densities of Chlorella sp. NCTU‐2. The results show that the CO₂ removal efficiency was related to biomass concentration and aeration rate. The maximum CO₂ removal efficiency of the Chlorella sp. NCTU‐2 culture was 63% when the biomass was maintained at 5.15 g/L concentration and 0.125 vvm aeration (volume gas per volume broth per min; 10% CO₂ in the aeration gas) in the porous centric‐tube photobioreactor.     

Progress in physicochemical parameters of microalgae cultivation for biofuel production

Microalgae have been exploited for biofuel generation in the current era due to its enormous energy content, fast cellular growth rate, inexpensive culture approaches, accumulation of inorganic compounds, and CO₂ sequestration. Currently, research is ongoing towards the advancement of the microalgae cultivation parameters to enhance the biomass yield. The main objective of this study was to delineate the progress of physicochemical parameters for microalgae cultivation such as gaseous transfer, mixing, light demand, temperature, pH, nutrients and the culture period. This review demonstrates the latest research trends on mass transfer coefficient of different microalgae culturing reactors, gas velocity optimization, light intensity, retention time, and radiance effects on microalgae cellular growth, temperature impact on chlorophyll production, and nutrient dosage ratios for cellulosic metabolism to avoid nutrient deprivation. Besides that, cultivation approaches for microalgae associated with mathematical modeling for different parameters, mechanisms of microalgal growth rate and doubling time have been elaborately described. Along with that, this review also documents potential lipid-carbohydrate-protein enriched microalgae candidates for biofuel, biomass productivity, and different cultivation conditions including open-pond cultivation, closed-loop cultivation, and photobioreactors. Various photobioreactor types, the microalgae strain, productivity, advantages, and limitations were tabulated. In line with microalgae cultivation, this study also outlines in detail numerous biofuels from microalgae.     

Cultivation of a cyanobacterium in an internally radiating air-lift photobioreactor

This study proposes a new design of the internally radiatingphotobioreactor, which combines the advantages of an air-lift bioreactorand an internally radiating system, and an efficient way of supplying lightenergy into the photobioreactor during cell cultivation. For a modelphotosynthetic microorganism, Synechococcus PCC 6301 wascultivated in an internally radiating air-lift photobioreactor. The lightcondition inside the photobioreactor was characterized by the average lightintensity which was calculated from the light distribution model. Sinceexcessive light energy induced photoinhibition at the early growth stage, thestrategy of lumostatic operation was developed in order to maintain thelight condition at an appropriate level during cell cultivation. Based on thecalculation results of the light distribution model, the average light intensitywas regulated at 30, 60, or 90 mol m^-2 s^-1 byincreasing the number of light radiators. The model-based control ofirradiating level enabled us to harvest a larger amount of cells withoutshowing the photoinhibited growth. Other favorable results included thereduction of cultivation time and lower consumption of irradiating power.     

产油嗜碱绿球藻MC-1的烟气适应性

为了降低微藻产油成本和减少温室气体的排放,利用煤炭烟气培养一株具有pH快速漂移和高碱适应特性的产油微藻Chlorococcum alkaliphilus MC-1.首先于15L光生物反应器中分三组(空白组、CO2组和烟气组)进行小体积培养实验,然后在24 m2开放式跑道池中进行放大培养,研究了微藻MC-1对烟气培养的适应性.结果表明,在光生物反应器培养实验中,烟气组的最高生物量浓度、生长速率、藻体总脂含量和CO2固定速率分别为:(1.02±0.07) g/L、(0.12±0.02) g/(L·d)、(37.84±0.58)％和(0.20±0.02) g/(L·d),比CO2组分别提高了36％、33.33％、15.34％和33.33％.在开放式跑道池培养实验中,烟气与纯CO2的培养效果相似,烟气培养下的最高生物量浓度、生长速率、藻体总脂含量和CO2固定速率分别为:147.40 g/m2、14.73 g/(m2·d)、35.72％和24.01 g/(m2·d);烟气培养产出的藻粉中有毒重金属Pb、As、Cd和Cr的含量均低于国家限量标准.实验同时测定了烟气培养下藻液对烟气中CO2、NO和SO2的吸收效果,结果显示,在光生物反应器和开放式跑道池培养中此三种气体的平均吸收率均高于以往研究结果.上述结果说明,该藻能适应烟气培养条件,耦合微藻MC-1产油与烟气减排的室外放大培养是可行的.     

微藻固定燃烧烟气中CO2 的研究进展

空气中CO2浓度升高导致的气候变暖问题已经成为全球性的环境、科学、政治、经济问题。近年来,对可用于直接固定工业废气尤其是燃烧烟气中CO2的捕捉和封存 (CCS) 技术进行了广泛的研究。在这些技术中,微藻生物固定CO2是一种具有大规模应用前景和经济上可行的CCS技术。以下从藻种的筛选、烟气条件对微藻固定CO2的影响、高效光生物反应器的开发和微藻产物的利用等方面对微藻生物固定烟气中CO2的现状和发展以及作者所在实验室在这一领域的研究情况进行了分析和总结,最后对其技术前景进行了展望,以期对微藻固定燃烧烟气中CO