光生物反应器培养微藻研究进展

微藻具有固定CO2和净化有机废水的能力,在环保、食品饲（饵）料、医药和生物能源开发等领域备受关注,但规模化培养及其产业化仍是研究的难点,亟待解决。就常用于大规模培养微藻的光生物反应器的特点和结构进行了综述。其中,封闭式微藻光生物反应器能够较好地调控藻种的培养条件、不易遭受污染,藻种的纯度容易控制,但培养规模小,生产成本较高;而开放式微藻光生物反应器无法精确控制藻种生长环境,但生产规模大、产量高、生产成本低,因此应用广泛。最佳的方法是综合两者优点,即首先利用封闭式微藻光生物反应器进行中试放大,大量繁殖藻种,然后投入开放式微藻光生物反应器内进行大规模商业生产,此方法有望成为微藻光生物反应器的发展方向,以期为微藻大规模培养提供参考借鉴。     

微藻养殖中的新型光生物反应器系统

目前世界上微藻的大规模养殖仍普遍采用开放池式生产系统,该系统具有许多不足之处;开发高效、易于控制的新型生产系统是今后开展的趋势。本文对一些新型光生物反应器系统如优化的浅水道工生产系统、密闭管道式、发酵罐式光生物反应器、高密度藻类光生物反应器以及其它类型的光生物反应器进行了较为详细的介绍。     

光照对光生物反应器中微藻高密度光自养培养的影响

光生物反应器是实现微藻高密度培养的重要装置,其设计的关键技术之一是选择合适的光照方式。根据国内外近十年来的相关研究成果,重点介绍了入射光性质(光源、光强、光质和光暗循环)和光能分布对微藻生长的影响,评述了用于微藻高密度培养的光照技术,展望了进一步的研究方向,为高效光生物反应器的设计和优化提供参考。     

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。     

管道式光生物反应器的设计和性能

该文概述了管道式光生物反应器在设计上对性能的要求,对影响光生物反应器培养效率的各种生长条件如光能利用效率、CO2利用效率、环境温度、溶解氧等问题进行了探讨,指出高效并可自动调节的藻液循环混合系统对于高密度海藻培养是非常重要的,提出了能否自动清洗光生物反应器内壁是判断光生物反应器是否可用于工业化生产的关键。     

微藻培养过程的光特性研究进展

微藻培养过程中光的吸收、衰减以及光暗循环等特性是影响微藻的生长速度及其产量的重要因素。本文分析了微藻的光吸收过程、光在微藻培养液中的衰减特性以及微藻培养过程中的光暗循环特性,重点综述了国内外各类光生物反应器中光特性的研究进展,并对其发展方向进行了展望,为微藻培养光生物反应器的设计提供参考依据。     

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。     

聚球藻7002在光生物反应器中的光自养培养

通过对聚球藻7002在光生物反应器中的培养,研究了光强在聚球藻7002培养液中的衰减规律,得到了培养过程光强随藻细胞浓度和光程距离变化的关系式,即I=I₀exp［-(-0.0239+0.0777OD₇₅₀)·L］。并对培养过程特性及培养温度、外加CO₂浓度和光照强度对藻细胞生长的影响进行了较为详细的研究,得到了反应器中较为适宜的聚球藻7002的培养条件,藻细胞培养密度达到3.4g/L(干重),体积产率达到0.57g/(L·d)的较高水平。     

微藻生物柴油的现状与进展

微藻生物柴油能够解决目前使用植物原料发展生物柴油面临的耕地不足、气候变化对产量影响大和引起农作物价格上涨等突出问题。通过转基因技术培育“工程微藻”,繁衍能力高,生长周期短,比陆生植物产油高出几十倍,并且能用海水作为其天然培养基进行工业化生产。介绍了微藻生物柴油的优势,高脂质微藻选育,以及工程微藻研究与下游生产工艺的研究现状和进展。     

植物生物反应器研究进展

植物生物反应器是近年来生物技术领域新的研究方向,利用农作物进行疫苗、药用蛋白的生产,具有广阔的市场前景和商业价值。研究证明,用各种农作物为载体的植物生物反应器产品可通过种子、果实或块茎表达,便于贮藏、运输和利用。它拓宽了传统农业概念,成为现代生物农业重要的研究方向之一,推动了生物经济快速健康的前进,促进农业可持续发展。综述植物生物反应器的研究与应用现状,并对转基因作物作为植物生物反应器的发展前景作分析和展望。     

Photobioreactors for cultivation and synthesis: Specifications,challenges, and perspectives

Due to their versatility and the high biomass yield produced, cultivation of phototrophic organisms is an increasingly important field. In general, open ponds are chosen to do it because of economic reasons; however, this strategy has several drawbacks such as poor control of culture conditions and a considerable risk of contamination. On the other hand, photobioreactors are an attractive choice to perform cultivation of phototrophic organisms, many times in a large scale and an efficient way. Furthermore, photobioreactors are being increasingly used in bioprocesses to obtain valuable chemical products. In this review, we briefly describe different photobioreactor set‐ups, including some of the recent designs, and their characteristics. Additionally, we discuss the current challenges and advantages that each different type of photobioreactor presents, their applicability in biocatalysis and some modern modeling tools that can be applied to further enhance a certain process.     

新型生物反应器结构研究进展

生物反应器是生物工程的核心设备,其结构的合理性直接决定反应器生物加工的效率。生物反应器的研究一直是生物工程的核心问题之一。随着青霉素的工业化生产,机械搅拌式生物反应器应运而生,此后,随着动植物细胞培养,高等真菌培养,藻类培养等生物过程的发展,人们相应开发了大量的生物反应器,其中以机械搅拌式生物反应器和气升式样生物反应器尤为突出,本文总结了近年来文献报道的新型生物反应器,主要阐述了机械搅拌式和气升式两类生物反应器结构的研究进展,对目前国内外报道的11种新型反应器典型结构进行了总结与分析。     

Optimizing microalgal production in raceway systems

The industrial exploitation of microalgae is characterized by the production of high‐value compounds. Optimization of the performance of microalgae culture systems is essential to render the process economically viable. For raceway systems, the optimization based on optimal control theory is rather challenging, because the process is by essence periodically forced and, as a consequence, optimization must be carried out in a periodic framework. In this article, we propose a simple operational criterion for raceway systems that when integrated in a strategy of closed‐loop control allows attaining biomass productivities very near to the theoretical maximal productivities. The strategy developed was tested numerically using a mathematical model of microalgae growth in raceways. The model takes into account the temporal variation of the environmental variables temperature and light intensity and their influence on microalgae growth. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29: 543–552, 2013     

Effect of daytime CO2 supplement on productivity and biochemical composition of Scenedesmus armatus under outdoor cultivation

The cultivation of Scenedesmus armatus was carried out under outdoor Thailand climate conditions. The highest actual growth rate occurred at around 9:00 a.m. to 3:00 p.m., with a wide pH range of 6.4 to 11. The supply of CO₂ had slight influence on growth characteristics but did exert some observable effects on nutritional accumulations. Adding CO₂ from 2 to 15% by volume in the aeration (0.2 vvm) caused an increase in lipid and protein from 19.8 to 25.6 and 37.8 to 48.2% w/w, respectively, whereas carbohydrate decreased from 42.5 to 26.2% w/w. Scenedesmus armatus cultivated with 2% CO₂-enriched air provided the highest the average of the average biomass productivity of 91.25 mg L^?1 d^?1, which corresponded to a CO₂ fixation of 165 mg CO₂ L^?1 d^?1 with the average lipid, protein, and carbohydrate productivities of 22.24, 38.34, and 30.67 mg L^?1 d^?1.     

Photobioreactors for microalgal cultures: A Lagrangian model coupling hydrodynamics and kinetics

Closed photobioreactors have to be optimized in terms of light utilization and overall photosynthesis rate. A simple model coupling the hydrodynamics and the photosynthesis kinetics has been proposed to analyze the photosynthesis dynamics due to the continuous shuttle of microalgae between dark and lighted zones of the photobioreactor. Microalgal motion has been described according to a stochastic Lagrangian approach adopting the turbulence model suitable for the photobioreactor configuration (single vs. two‐phase flows). Effects of light path, biomass concentration, turbulence level and irradiance have been reported in terms of overall photosynthesis rate. Different irradiation strategies (internal, lateral and rounding) and several photobioreactor configurations (flat, tubular, bubble column, airlift) have been investigated. Photobioreactor configurations and the operating conditions to maximize the photosynthesis rate have been pointed out. Results confirmed and explained the common experimental observation that high concentrated cultures are not photoinhibited at high irradiance level. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:1259–1272, 2015     

Hydrogen production by microalgae

The production of H₂ gas from water and sunlightusing microalgae, `biophotolysis', has been a subjectof applied research since the early 1970s. A numberof approaches have been investigated, but most provedto have fundamental limitations or requireunpredictable research breakthroughs. Examples areprocesses based on nitrogen-fixing microalgae andthose producing H<sub>2</sub> and O<sub>2</sub> simultaneously fromwater (`direct biophotolysis'). The most plausibleprocesses for future applied R & D are those whichcouple separate stages of microalgal photosynthesisand fermentations (`indirect biophotolysis'). Theseinvolve fixation of CO₂ into storagecarbohydrates followed by their conversion to H₂by the reversible hydrogenase, both in dark andpossibly light-driven anaerobic metabolic processes. Based on a preliminary engineering and economicanalysis, biophotolysis processes must achieve closeto an overall 10% solar energy conversion efficiencyto be competitive with alternatives sources ofrenewable H₂, such as photovoltaic-electrolysisprocesses. Such high solar conversion efficiencies inphotosynthetic CO₂ fixation could be reached bygenetically reducing the number of light harvesting(antenna) chlorophylls and other pigments inmicroalgae. Similarly, greatly increased yields ofH₂ from dark fermentation by microalgae could beobtained through application of the techniques ofmetabolic engineering. Another challenge is toscale-up biohydrogen processes with economicallyviable bioreactors.Solar energy driven microalgae processes forbiohydrogen production are potentially large-scale,but also involve long-term and economically high-riskR&D. In the nearer-term, it may be possible tocombine microalgal H₂ production with wastewatertreatment.     

Botryococcus braunii: A Renewable Source of Hydrocarbons and Other Chemicals

ABSTRACT:?

Botryococcus braunii, a green colonial microalga, is an unusually rich renewable source of hydrocarbons and other chemicals. Hydrocarbons can constitute up to 75% of the dry mass of B. braunii. This review details the various facets of biotechnology of B. braunii, including its microbiology and physiology; production of hydrocarbons and other compounds by the alga; methods of culture; downstream recovery and processing of algal hydrocarbons; and cloning of the algal genes into other microorganisms. B. braunii converts simple inorganic compounds and sunlight to potential hydrocarbon fuels and feedstocks for the chemical industry. Microorganisms such as B. braunii can, in the long run, reduce our dependence on fossil fuels and because of this B. braunii continues to attract much attention.     

Biotechnology of algal biomass production: a review of systems for outdoor mass culture

Microalgae are very efficient solar energy converters and they can produce a great variety of metabolites. Man has always tried to take advantage of these proporties through algal mass culture. Despite the fact that many applications for microalgae have been described in the literature, these micro-organisms are still of minor economic importance. Industrial reactors for algal culture are at present, all designed as open race-ways (shallow open ponds where culture is circulated by a paddle-wheel). Technical and biological limitations of these open systems have given rise to the development of enclosed photoreactors (made of transparent tubes, sleeves or containers and where light source may be natural or artificial). The present review surveys advances in these two technologies for cultivation of microalgae. Starting from published results, the advantages and disadvantages of open systems and closed photobioreactors are discussed. A few open systems are presented for which particularly reliable results are available. Emphasis is then put on closed systems, which have been considered as capital intensive and are justified only when a fine chemical is to be produced.