利用响应面方法优化转小鼠金属硫蛋白-I基因聚球藻7002的培养基成分

为实现转小鼠金属硫蛋白基因-I聚球藻7002的高密度培养, 并将其应用于实际的重金属废水处理过程, 首先需要对培养基的成分进行优化。本文利用响应面这一多因素过程优化的有效工具, 通过全因子实验、最陡爬坡实验和中心组合实验, 对转小鼠金属硫蛋白基因-I聚球藻7002培养基的主要成分以及初始pH进行了优化。优化后的培养基组成为: NaHCO3 1.696 g/L, NaNO3 8.57 g/L, 初始pH为8.57, 其他成分同Medium A。优化条件分别在2 L和20 L气升式光生物反应器中得到了验证, 最大细胞浓度分别达到每升4.16 g干重和每升3.12 g干重, 分别比优化前提高了9倍和7倍, 从而为其产业化应用打下基础。     

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%。     

南极细菌Pseudoalteromonas sp.3-3-1-2产胞外多糖条件优化

利用单因子试验和响应面法对南极细菌Pseudoalteromonas sp.3-3-1-2产胞外多糖条件进行了优化。通过单因子试验确定菌株3-3-1-2产胞外多糖的最佳碳源和氮源分别为蔗糖和KNO3,其最佳添加量分别为40 g/L和10 g/L;最适培养温度为15.0℃;最佳培养基盐度和初始p H分别为4.5%和9;并确定了对产糖有显著影响的单因素——碳源(蔗糖)、氮源(KNO3)和温度。通过Box-Behnken进行试验设计和Design-Expert响应面软件分析,得到了菌株3-3-1-2产胞外多糖发酵条件的优化条件:蔗糖43.1 g/L、KNO39.6 g/L和温度17.2℃。在此优化条件下,菌株3-3-1-2发酵液的粗胞外多糖产量可达3.03 g/L。     

响应面法优化黑曲霉产异淀粉酶的培养条件

在液态发酵条件下,采用单因素实验确定了Aspergillus niger PZ331产异淀粉酶的最适碳源和氮源,分别为蔗糖和硝酸铵。在上述基础上利用Plackett-Burman设计对影响产异淀粉酶的因素进行评价,并筛选出硝酸铵、接种量、培养温度3个主要因素;继而利用响应面设计优化了最佳硝酸铵浓度、接种量和培养温度。最终确定了最优培养条件为：蔗糖10 g/L,硝酸铵10 g/L,磷酸氢二钾3 g/L,硫酸亚铁0.01 g/L,硫酸镁1 g/L,起始p H值4.2;接种量2%（孢子浓度为107cfu/m L）,30℃培养72 h,酶活达137.3μ/m L;比基础培养基的提高了1.71倍左右。     

响应面法优化普通小球藻混合营养培养基组成生产生物质

利用响应面法优化了混合营养培养普通小球藻生产生物质的培养基组成.首先采用Plackett-Burman设计对11个相关营养因素的效应进行了评价,并筛选出影响小球藻细胞生长的3个主要因素为KNO3、葡萄糖和NaC1;然后结合Box-Behnken设计建立了以小球藻浓度为响应值的二次回归方程模型,获得优化的培养基组成为KNO31.64g/L、葡萄糖45g/L、NaC1 1.57g/L;模型预测的最大浓度为5.28g/L,验证值为5.68g/L;验证结果表明,所建立模型预测精度较好,可用于优化小球藻的混养培养基组成.优化条件下混养小球藻细胞的蛋白质和色素含量较优化前降低,而可溶性糖和油脂含量提高,脂肪酸以棕榈酸和油酸为主;细胞组分分析结果显示,混养培养所得小球藻生物质具有作为生产微藻生物能源原料的潜力.     

生物反应器培养转基因鱼腥藻的研究

在反应器中研究了转人TNF-α基因鱼腥藻7120(Anabaena sp．PCC7120,pDC-TNF)的培养。结果表明气升式反应器适合于转基因鱼腥藻的培养。气升式反应器中通气量和光照是主要的影响因素,观察到1L罐中最适通气量为60～75L／h,最适光照强度为1200lx,此时在25℃混养,光照时间／黑暗时间为12h／12h,15d生物量干重大于3g／L,TNF表达水平约占总可溶蛋白的22％,达到了摇瓶培养水平。实验发现添加维生素B1 300μg／L、B12 200μg／L和生物素4μg／L时,生产周期为12d,缩短20％,表达水平相同。培养过程通入含有5％CO2的空气,能促进生长,缩短生产周期,但收获生物量不受影响。从添加维生素和通入CO2的培养结果证明反应器中培养时,光照是限制性因素,当反应器系统一定时,最终生物量有一个最大值,如需进一步提高产量,必须设法改变光照系统。     

絮凝酵母SPSC01连续培养最适生长条件的研究

采用均匀设计实验法对气升式内环流生物反应器中絮凝酵母SPSC01的高密度培养条件进行了研究,确定了各因素与目标函数之间的关系,并通过综合调优,获得该菌株的最佳培养条件：温度30℃;通气量0714vvm;培养基组成为：双酶法制备的玉米糖化液,糖浓度为220g/L,添加4 mL/L玉米浆和3g/L（NH4）2HPO4;稀释速率控制为0.02h－1。在上述条件下进行絮凝酵母的连续培养,培养液中的酵母细胞密度达到了20g(d.w)/L以上。     

好氧反硝化细菌N22’种子培养基的优化

目的:优化好氧反硝化细菌N22’的种子培养基,提高对数期末期细菌浓度。方法:采用Plackett-Burman设计对影响N22’细菌浓度的因素进行评估并筛选出具有显著效应的因素KNO3(X3)、KH2PO4(X4)和K2HPO4(X5),经过最陡爬坡实验接近3个因素的最大响应区域后,应用Box-Behnken设计和响应面分析法确定3个因素的最优水平。结果:优化后的种子培养基:柠檬酸钠6g,KNO32.72g,KH2PO41.35g,K2HPO41.12g,MgSO4·7H2O 0.25g,CaCl20.025g/L,FeSO4·7H2O 0.025g,EDTA0.125g/L;蒸馏水1 000mL,初始pH值7.0。优化后发酵液对数期末期细菌浓度达到1.684 0×1012cfu/mL,比优化前1.632 7×1011cfu/mL提高了9.31倍。结论:Plackett-Burman设计结合响应面分析方法优化了菌株N22’的种子培养基。     

利用响应面法优化α-糖苷酶抑制剂发酵培养基

【目的】采用响应面法对戈壁三素链霉菌PW409发酵合成α-糖苷酶抑制剂的培养基进行优化。【方法】采用Plackett-Burman法筛选影响α-糖苷酶抑制剂产生的关键因素,用最陡爬坡试验逼近关键因素的最大响应区域,采用Box-Behnken设计以及响应面分析法,得到各因素的最佳浓度,通过液相色谱-串联质谱法(LC-MS/MS)对发酵液中α-糖苷酶抑制剂进行定量分析。【结果】发酵培养基中可溶性淀粉、KNO3和K2HPO4的浓度对α-糖苷酶抑制剂的产量影响较大。优化后的培养基组成为:可溶性淀粉9.01 g/L,KNO3 11.0 g/L,K2HPO4 0.32 g/L,MgSO4.7H2O 0.50 g/L,FeSO4.7H2O 0.01 g/L,pH 7.5。【结论】在此优化条件下,链霉菌PW409发酵液对麦芽糖苷酶的半数抑制浓度IC50为22 mg/L,抑制活性较优化前提高了近10倍。发酵液中的1-脱氧野尻霉素含量可达7.84 mg/L,较优化前提高了668倍,米格列醇的含量可达0.94 mg/L,较优化前提高了10倍。     

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.     

无机碳源对小球藻自养产油脂的影响

旨在研究小球藻利用无机碳自养产油脂,考察了3种无机碳源 (Na2CO3、NaHCO3和CO2) 及其初始浓度对小球藻产油特性的影响。结果表明,小球藻能利用Na2CO3、NaHCO3和CO2产油;经Na2CO3、NaHCO3和CO2培养10 d后,随着每种无机碳源浓度的增加,小球藻产量均先增加后减少。小球藻经3种无机碳源培养后,其培养液pH值上升。最适宜的Na2CO3和NaHCO3添加量均为40 mmol/L,其生物量分别达到0.52 g/L和0.67 g/L,产油量分别达到0.19 g/L和0.22 g/L。在3种无机碳源中,CO2是最佳无机碳源,当CO2浓度为6％时,小球藻生长最快,生物量达2.42 g/L,产油量最高达0.72 g/L;当CO2浓度过低时,无机碳供应不足,油脂产量低;当CO2浓度过高时,培养液pH偏低,小球藻油脂积累受到抑制。Na2CO3和NaHCO3较CO2更有利于小球藻积累不饱和脂肪酸。     

以异养细胞作为种子的椭圆小球藻产油脂光自养培养优化

异养细胞种子/光自养培养方法是一种可异养培养的能源微藻培养的有效方法,但已有文献尚未从工艺优化角度考察其发展潜力。为了获得较高细胞密度的用于光自养培养的种子和提高光自养培养的细胞密度与油脂产率,对异养细胞种子/光自养培养的培养基和培养条件进行了优化。结果表明,采用优化后的培养基,椭圆小球藻在摇瓶中异养培养的最高藻细胞密度可达11.04 g/L,比在初始培养基条件下提高了28.0%,在5 L发酵罐中异养培养的藻细胞密度达到73.89 g/L;在2 L柱式光生物反应器中光自养培养的藻细胞密度、油脂含量和油脂产率分别达1.62 g/L、36.34%和6.1 mg/(L·h),油脂成分主要为含C16-C18碳链的脂肪酸,是制备生物柴油的理想原料。经过优化,异养细胞种子/光自养培养这一方法能够显著地提高椭圆小球藻产油脂的能力,这进一步表明异养细胞种子/光自养培养方法有望成为可异养的能源微藻的高效培养方式。     

Nitrogen starvation strategies and photobioreactor design for enhancing lipid content and lipid production of a newly isolated microalga Chlorella vulgaris ESP-31: implications for biofuels

Microalgae are recognized for serving as a sustainable source for biodiesel production. This study investigated the effect of nitrogen starvation strategies and photobioreactor design on the performance of lipid production and of CO(2) fixation of an indigenous microalga Chlorella vulgaris ESP-31. Comparison of single-stage and two-stage nitrogen starvation strategies shows that single-stage cultivation on basal medium with low initial nitrogen source concentration (i.e., 0.313 g/L KNO(3)) was the most effective approach to enhance microalgal lipid production, attaining a lipid productivity of 78 mg/L/d and a lipid content of 55.9%. The lipid productivity of C. vulgaris ESP-31 was further upgraded to 132.4 mg/L/d when it was grown in a vertical tubular photobioreactor with a high surface to volume ratio of 109.3 m(2)/m(3) . The high lipid productivity was also accompanied by fixation of 6.36 g CO(2) during the 10-day photoautotrophic growth with a CO(2) fixation rate of 430 mg/L/d. Analysis of fatty acid composition of the microalgal lipid indicates that over 65% of fatty acids in the microalgal lipid are saturated [i.e., palmitic acid (C16:0) and stearic acid (C18:0)] and monounsaturated [i.e., oleic acid (C18:1)]. This lipid quality is suitable for biodiesel production.     

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%。     

Microalgal biomass production and on-site bioremediation of carbon dioxide, nitrogen oxide and sulfur dioxide from flue gas using Chlorella sp. cultures

The growth and on-site bioremediation potential of an isolated thermal- and CO?-tolerant mutant strain, Chlorella sp. MTF-7, were investigated. The Chlorella sp. MTF-7 cultures were directly aerated with the flue gas generated from coke oven of a steel plant. The biomass concentration, growth rate and lipid content of Chlorella sp. MTF-7 cultured in an outdoor 50-L photobioreactor for 6 days was 2.87 g L?1 (with an initial culture biomass concentration of 0.75 g L?1), 0.52 g L?1 d?1 and 25.2%, respectively. By the operation with intermittent flue gas aeration in a double-set photobioreactor system, average efficiency of CO? removal from the flue gas could reach to 60%, and NO and SO? removal efficiency was maintained at approximately 70% and 50%, respectively. Our results demonstrate that flue gas from coke oven could be directly introduced into Chlorella sp. MTF-7 cultures to potentially produce algal biomass and efficiently capture CO?, NO and SO? from flue gas.     

Reduction of CO2 by a high-density culture of Chlorella sp. in a semicontinuous photobioreactor

The microalga incorporated photobioreactor is a highly efficient biological system for converting CO2 into biomass. Using microalgal photobioreactor as CO2 mitigation system is a practical approach for elimination of waste gas from the CO2 emission. In this study, the marine microalga Chlorella sp. was cultured in a photobioreactor to assess biomass, lipid productivity and CO2 reduction. We also determined the effects of cell density and CO2 concentration on the growth of Chlorella sp. During an 8-day interval cultures in the semicontinuous cultivation, the specific growth rate and biomass of Chlorella sp. cultures in the conditions aerated 2-15% CO2 were 0.58-0.66 d(-1) and 0.76-0.87 gL(-1), respectively. At CO2 concentrations of 2%, 5%, 10% and 15%, the rate of CO2 reduction was 0.261, 0.316, 0.466 and 0.573 gh(-1), and efficiency of CO2 removal was 58%, 27%, 20% and 16%, respectively. The efficiency of CO2 removal was similar in the single photobioreactor and in the six-parallel photobioreactor. However, CO2 reduction, production of biomass, and production of lipid were six times greater in the six-parallel photobioreactor than those in the single photobioreactor. In conclusion, inhibition of microalgal growth cultured in the system with high CO2 (10-15%) aeration could be overcome via a high-density culture of microalgal inoculum that was adapted to 2% CO2. Moreover, biological reduction of CO2 in the established system could be parallely increased using the photobioreactor consisting of multiple units.     

Mixed culture of oleaginous yeast Rhodotorula glutinis and microalga Chlorella vulgaris for lipid production from industrial wastes and its use as biodiesel feedstock

A mixed culture of oleaginous yeast Rhodotorula glutinis and microalga Chlorella vulgaris was performed to enhance lipid production from industrial wastes. These included effluent from seafood processing plant and molasses from sugar cane plant. In the mixed culture, the yeast grew faster and the lipid production was higher than that in the pure cultures. This could be because microalga acted as an oxygen generator for yeast, while yeast provided CO(2) to microalga and both carried out the production of lipids. The optimal conditions for lipid production by the mixed culture were as follows: ratio of yeast to microalga at 1:1; initial pH at 5.0; molasses concentration at 1%; shaking speed at 200 rpm; and light intensity at 5.0 klux under 16:8 hours light and dark cycles. Under these conditions, the highest biomass of 4.63±0.15 g/L and lipid production of 2.88±0.16 g/L were obtained after five days of cultivation. In addition, the plant oil-like fatty acid composition of yeast and microalgal lipids suggested their high potential for use as biodiesel feedstock.     

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。     

Ectoine Production by Halomonas boliviensis: Optimization Using Response Surface Methodology

Two cultivation steps were used for production of biomass and ectoine by Halomonas boliviensis, respectively. The optimization of some nutrient parameters in each step was investigated by using response surface methodology. Twenty and 12 experiments were performed to attain optimal conditions for biomass and ectoine production, respectively. The model predicted a maximum biomass concentration of 3.34 g/L on optimization of NH₄Cl, K₂HPO₄, and MgSO₄•7H₂O concentrations during the first cultivation, while a maximum ectoine concentration of 1.27 g/L was predicted on optimizing NaCl and monosodium glutamate concentrations in the second cultivation. The experimental values obtained (3.36 g biomass/L and 1.25 g ectoine/L) were in good agreement with the predicted values. The optimized conditions were also used for two-step 1.5-L fed-batch fermentations. In the first step, biomass concentration of 28.7 g/L was obtained while in the second step biomass concentration increased to 63 g/L. Ectoine concentration of 9.2 g/L was obtained, and the overall ectoine productivity was 6.3 g/L/day, being among the highest reported so far.