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。     

光生物反应器中螺旋藻培养条件的优化

利用正交实验对搅拌式光生物反应器中钝顶螺旋藻(Spirulina platensis Geitl)的培养条件即搅拌速度、通气量和光照强度进行优化.实验结果表明:当培养温度为30℃时,通过正交实验所获得的最佳培养条件为搅拌转速120 r·min-1,通气量80 L·h-1,光照强度5000lx.在最佳培养条件下,收获时螺旋藻的干重为1.922 g·L-1.根据回归模型得到相应的优化条件为:光照强度5000lx,通气量150L·h-1,搅拌转速111.70r·min-1,收获量(干重)的预测值为2.293 g·L-1.另外,10%的接种量有利于螺旋藻的生长.     

平板式光生物反应器培养液混合强度对螺旋藻生长的影响

目的：探讨平板式光生物反应器内培养液混合对螺旋藻生长的影响规律。方法：在平板式光生物反应器中进行钝顶螺旋藻（Spirulina platensis）户内和户外培养,通过改变通入反应器内气体的流量来控制培养液的混合强度,测定藻细胞的面积产量和叶绿素含量。结果：在一定的混合强度范围内,藻细胞的面积产量随着混合强度的增加而增加;室内培养时,混合强度的改变不会影响藻细胞的光合反应特性,户外高密度培养时,培养液混合强度的改变会造成藻细胞光合反应特性的变化。结论：强化培养液的混合可以提高螺旋藻产量。     

紫球藻的培养与利用（综述）

紫球藻为单细胞红藻,其细胞富含红藻多糖、多不饱和脂肪酸(主要为AA和EPA）及藻胆蛋白等高价值生物活性物质,在医药和精细化工领域有广泛的应用前景。本文综述紫球藻的生物学特性、生物活性物质、培养与培养特性等方面的研究概况。     

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。     

微拟球藻富油藻株筛选及柱状光生物反应器培养评价研究

研究以亲脂性荧光染料BODIPY505/515和流式细胞仪为基础, 从多株诱变海洋微拟球藻(Nannochloropsis oceanica)中筛选到4株候选富油藻株(MT-1,2,3,4), 并利用柱状光生物反应器对诱变株的产油能力进行了综合评价。结果表明, 藻株筛选时最佳BODIPY505/515使用浓度为0.87 μg/mL, 染色时间为10min; 4株诱变株产油性能较野生株有较大提高, 其中MT-4油脂积累达到了干重的66%, 油脂产率比野生型藻株提高了45%, 达到了27.32 mg/(L·d)。4株诱变株的脂肪酸组成合适, 其中C16和C18之和占78%以上, 且主要以饱和脂肪酸和单不饱和脂肪酸为主; 多不饱和脂肪酸只占总脂肪酸的6%—8%, 非常适合生物柴油生产。研究提供了一种针对海洋微拟球藻富油藻株快速、有效的筛选方法, 并以此为基础筛选得到4株极具生物柴油生产潜力的候选藻株, 有望用于规模化生产。     

超声波降解紫球藻胞外多糖研究

通过测定溶液粘度,判断超声波降解紫球藻(Porphyridium cruentumi)胞外多糖的效果。运用均匀设计对超声波降解紫球藻胞外多糖的影响因素(处理振幅、时间、脉冲)进行优化,获得超声波处理的最佳条件:振幅39%、处理时间245s和脉冲9.5s。在最佳条件下,胞外多糖的粘度为2.98mm²/s,与预测值一致。采用DPS软件对实验结果进行二次多项式分析与拟合,并对模型和回归系数进行显著性检验,建立了以胞外多糖粘度为目标的回归方程式。     

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。     

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。     

用管式光生物反应器培养螺旋藻的研究

微藻大规模培养主要有敞开式大池培养和封闭式光生物反应器培养两种主要方式。管式光生物反应器是封闭式光生物反应器的主要类型之一。与其它类型相比,管式光生物反应器放大较易,成本较低。国外关于管式光生物反应器已有不少研究［１～３］但关于管式光生物反应器产率与光强和光暗比的关系等方面的研究尚未得出明确的结论。国内管式光生物反应器的研究较少［４］,尚未见有关管式光生物反应器中微藻悬浮液流变特性基础参数和产率影响因素的报道。螺旋藻是丝状体蓝藻,螺旋藻蛋白质含量高,其蛋白质所含必需氨基酸丰富,是国内外大规模商业…     

Swirling flow implementation in a photobioreactor for batch and continuous cultures of Porphyridium cruentum

Light is the main limiting factor in photoautotrophic-intensive production of microorganisms, and improvement of its use is an important concern for photobioreactor design and operation. Swirling flows, which are known to improve mass and photon transfers, were applied to annular light chambers of a photobioreactor and studied by simulation and microalgal culture. Two hydrodynamic conditions were compared: axial flow generating poor radial mixing, and tangential flow generating three-dimensional swirling motion. Batch and continuous cultures of the Rhodophyte Porphyridium cruentum were performed in a 100-L, 1.5-m(2), fully controlled photobioreactor with eight light chambers. The inlet design of these chambers was modified to create the hydrodynamic conditions for comparison. Various intensities of swirling motion were used, characterized by the velocity factor (VF), defined as the ratio between annular chamber flow and inlet aperture sections. Experiments were performed within the range of photon flux densities (PFD) optimizing the yield of light energy transformation into living substance for the species and the temperature used. Culture kinetics with swirling flows generated by apertures of VF = 2, 4, and 9 were compared with pseudoaxial VF = 2 chosen as reference. Batch cultures with VF = 4 swirling flow showed no significant difference, whereas continuous cultures proved more discriminating. Although no significant difference was obtained for VF = 2, a 7% increase of steady-state productivity and a 26% decrease in time required to reach this steady state were obtained with VF = 4 swirling flow. This beneficial effect of swirling flow could have accounted for increased mixing. Conversely, VF = 9 swirling flow resulted in a 9% decrease of steady-state productivity and a 9% increase in the time required to reach this steady state, a negative effect that could have accounted for increased shear stress. CO(2) bioconversion yield at steady state showed a 34% increase for VF = 4. These results suggest that swirling motion makes microalgal cultures more efficient, provided that the resulting adverse effects remain acceptable. Experimental investigation was completed by a theoretical approach in which simulation of continuous cultures of P. cruentum was based on the hydrodynamic conditions achieved in the photobioreactor. Although the results obtained with pseudoaxial flow were correctly predicted, simulations with swirling flow showed a marked enhancement of productivity not observed experimentally. The influence of side effects induced by increased mixing (particularly hydrodynamic shear stress) was considered with respect to modeling assumptions. Comparison of experimental results with theoretical simulation provided a better understanding of the mixing effect, a key factor in improving the efficiency of such bioprocesses.     

Outdoor continuous culture of Porphyridium cruentum in a tubular photobioreactor: quantitative analysis of the daily cyclic variation of culture parameters

The present work reports on the daily cyclic variation of oxygen generation rates, carbon consumption rates, photosynthetic activities, growth rates and biochemical composition of the biomass in a pilot plant continuous outdoor culture of the microalgae Porphyridium cruentum. A linear relationship between the external irradiance and the average irradiance inside the culture was found. In addition, the oxygen generation and carbon consumption rates were found to be a function of the average irradiance inside the culture. A reduction in photosynthetic activity of the cells at noon and recovery in the afternoon was also observed. Therefore, the cells showed a short-term response of parameters such as oxygen generation rate as well as carbon consumption rate with external and average irradiance; a model of photosynthesis rate considering photoinhibition is proposed. This model is a useful tool for the operation and scaleup of tubular photobioreactors, and can be used for determining CO₂ requirements of the system. The higher the photosynthesis rates, the lower the carbon losses, ranging from 25% at noon to 100% during the night. The growth rate showed a linear relationship with the daily mean average irradiance inside the culture with a long-term response. Likewise, a linear relationship among the oxygen generation rate and the growth rate was obtained. With respect to the biochemical composition of the biomass, the cells showed a long-term response of metabolic routes to mean daily culture conditions. During the illuminated period, energy was stored as carbohydrates and synthesis of proteins was low. During the night, the stored carbohydrates were consumed. The fatty acid dry weight (DW) content decreased during the daylight period, whereas the fatty acid profile, as total fatty acids, was a function of growth rate. A short-term variation of exopolysaccharides synthesis with solar irradiance was also observed, i.e. the higher the external irradiance the higher the excretion of exopolysaccharides as a protection against adverse culture conditions.     

中国红豆杉细胞悬浮体系营养条件的优化

采用均匀设计的试验方法,对中国红豆杉细胞悬浮体系培养条件进行优化,获得了关于细胞生长与培养基内碳源,氮源,磷浓度的回归方程,表明碳氮是影响细胞生长的关键因素。采用中心组合实验设计对培养基成分继续优化,并通过回归分析,结果表明,较优的培养基为碳源33．9g/L,氮源58．2mmol/L,磷浓度为5mmol/L,此工艺在15L反应器中,也取得了良好效果。     

Effect of liquid circulation velocity and cell density on the growth ofParietochloris incisa in flat plate photobioreactors

For more accurately describing the durations of the light and the dark phases of microalgal cells over the whole light-dark cycle, and probing into the relationship between the liquid circulation time or velocity, the aeration rate and cell density, a series of experiments was carried out in 10 cm light-path flat plate photobioreactors. The results indicated that the liquid flow in the flat plate photobioreactor could be described by liquid dynamic equations, and a high biomass output, higher content and productivity of arachidonic acid, 70.10 gm⁻²d⁻¹, 9.62% and 510.3 mg/L, respectively, were obtained under the optimal culture conditions.     

Optimization of culture conditions and continuous production of chitosan by the fungi,Absidia coerulea

The production of chitosan from the mycelia ofAbsidia coerulea was studied to improve cell growth and chitosan productivity. Culture conditions were optimized in batch cultivation (pH 4.5 agitator speed of 250 rpm, and aeration rate of, 2 vvm) and the maximum chitosan concentration achieved was 2.3 g/L under optimized conditions. Continuous culture was carried out successfully by the formation of new growth spots under optimized conditions, with a chitosan productivity of 0.052 gL⁻¹ h⁻¹, which is the highest value to date, and was obtained at a dilution rate of 0.05 h⁻¹. Cell chitosan concentrations reached about 14% in the steady state, which is similar to that achieved in batch culture. This study shows that for the continuous culture ofAbsidia coerulea it is vital to control the medium composition.     

重组巴斯德毕赤酵母发酵生产内切几丁质酶的培养条件优化

探讨重组巴斯德毕赤酵母发酵生产内切几丁质酶的最适培养条件,以期获得最佳的内切几丁质酶活力。以内切几丁质酶活力为指标,通过部分因子试验设计以及响应面法优化确定重组巴斯德毕赤酵母高产内切几丁质酶的最适培养条件。部分因子试验设计筛选的影响重组巴斯德毕赤酵母高产内切几丁质酶的3个关键因子为甲醇、油酸和吐温-80。响应面法优化的上述3个关键因子的最佳浓度分别为0.71%、0.086%和0.31%。重组巴斯德毕赤酵母发酵生产内切几丁质酶的最适培养条件为：酵母膏1%、酵母氮碱（YNB）1.34%、蛋白胨2%、甲醇0.71%、油酸0.086%、吐温-80 0.31%、PTM₁ 0.8%、pH 6.0。在上述培养条件下,重组巴斯德毕赤酵母产内切几丁质酶的活力高达30.92U/mL。与未优化前相比,酶活力提高了1.44倍。研究结果为内切几丁质酶的产业化生产和应用奠定了良好基础。