螺旋藻连续培养与动力学模型

在内循环气升式光生物反应器中 ,研究了钝顶螺旋藻 (SpirulinaplatensisGeitler)细胞的连续生长及其对碳源底物的利用特性。结果表明 :随着稀释率的增大 ,反应器中碳源浓度和细胞浓度分别呈上升和下降趋势 ,它们之间的关系可用Monod类型的方程很好地加以关联。细胞产率和碳消耗速率与稀释率的关系存在峰值现象 :在本实验条件下 ,最大细胞产率为 0 .36 2g/(L·d) ,最大碳消耗速率为 0 .177g/(L·d) ,此时稀释率为 0 .45 /d ,细胞浓度为OD560 =1.2 82 ,细胞对碳的得率系数为 2 .0 5 0g/g。所提出的连续培养动力学模型与实验数据拟合较好     

甲醇抑制时重组毕赤酵母发酵的特性研究

本文对毕赤酵母进行了恒化培养研究。以甲醇为唯一碳源时,在稀释率较低时(D<0.048 h^-1),连续培养系统操作很稳定。但在稀释率高时(D>0.048h^-1),连续培养系统的定态点不止一个,实验不能维持,故采用比生长速率恒定的分批流加培养进行研究。结果表明,毕赤酵母的生长符合Andrew普遍化底物抑制模型。综合考虑水蛭素的生成、底物的消耗,在生产中维持甲醇浓度为限制性浓度(0.5 g/L),且维持比生长速率为0.02 h^-1时,水蛭素Hir65的比生成速率达到最大值0.2 mg/(g·h)且甲醇的比消耗速率为0.04 g/(g·h)。     

真养产碱杆菌二级连续培养系统中稀释率对聚β－羟基丁酸合成的影响

在研究真养产碱杆菌WSH3一级连续培养动力学的基础上,采用二级连续培养系统对不同稀释率下聚β－羟基丁酸的生产进行了研究。结果表明：在一级连续培养系统中,当稀释率为0．2lh^-1时,细胞干重最大值达27．1g／L;二级培养系统中,稀释率为0．14h^-1时细胞干重最大值为47．6g／L;在稀释率为0．12h^-1时,PHB的生产强度达到最大值为2．50g／(L.h)．但胞内PHB含量仅为47．6％;在稀释率为O．075h^-1时,产物对基质的转化率达到最大值为0．38g／g'此时PHB的生产强度达2．14g,(L·h)和胞内PHB含量±72．1％;随着细胞比生长速率的增长,细胞中PHB含量和单位菌体合成PHB的量不断下降。     

一步法发酵菊芋生产乙醇

利用马克斯克鲁维酵母(Kluyveromyces marxianus)YX01具有菊粉酶生产能力且乙醇发酵性能良好的特点,直接发酵菊粉生成乙醇.在摇瓶中考察了该菌株最适发酵温度,进而在2.5L发酵罐中考察了通气量和底物浓度的影响.实验结果表明:该菌株最适发酵温度为35℃;在通气量为50 mL/min和100 mL/min时菌体生长加快,发酵时间缩短,但在不通气条件下糖醇转化率明显提高;在菊粉浓度235 g/L时,发酵终点乙醇浓度达到92.2 g/L,乙醇对糖的得率为0.436,为理论值的85.5%.在此基础上,使用近海滩涂种植海水灌溉收获的菊芋为底物,以批式补料方式直接发酵菊芋干粉浓度为280 g/L的底物,发酵终点乙醇浓度为84.0 g/L,乙醇对糖的得率为0.405,为理论值的80.0%.这些研究工作,为以菊芋为原料的燃料乙醇技术开发奠定了基础.     

磷对霍山石斛类原球茎悬浮培养细胞生长和多糖合成的影响

在确定了最适接种量和外植体细胞生理时间的基础上,研究了在不同起始磷浓度下,霍山石斛类原球茎生长、碳、氮消耗和多糖积累的动力学特性。以生长30d的类原球茎为材料,在接种量为100g/L时,类原球茎生长的最佳起始磷浓度为2.5mmol/L,培养36d时,类原球茎鲜重达496.5g/L。动力学分析表明,磷是霍山石斛类原球茎生长的限制性因素,胞内磷的积累水平与细胞生长具有相关性,2.5mmol/L的磷酸盐有利于碳、氮等营养物质的吸收;而多糖积累的最佳起始磷浓度为0.312mmol/L,培养36d时,其产量为2.22g/L。     

螺旋藻细胞培养与光能利用的关系

对钝顶螺旋藻(Spirulina platensis Geitler)细胞培养体系的光衰减以及连续培养条件下藻细胞生长对光能的利用特性进行了分析,结果表明改进的Lambert-Beer定律I=I0exp(-αxL)可较好地描述细胞浓度及光程对光衰减的综合影响;引入平均光强和细胞平均比消光量概念,借鉴Monod方程形式,较好地描述了它们与比生长速率之间的关系,并求得最大比生长速率μm、光强半饱和参数kI、光能维持系数m和得率系数YG分别为μm=1.75/d,kI=1.453×10     

酵母抽提物对CHO细胞生长及抗体表达的影响

为了深入认识酵母抽提物在中国仓鼠卵巢(CHO)细胞生长及单克隆抗体表达过程中所发挥的作用,综合考察了传代培养和批式培养过程中,不同浓度酵母抽提物条件下CHO细胞生长、抗体表达以及营养物代谢的情况。传代培养过程中,低浓度(1 g/L)的酵母抽提物能够显著促进CHO细胞的生长,高浓度(5-10 g/L)的酵母抽提物则会显著抑制CHO细胞的生长;同时,传代过程中添加酵母抽提物不会影响种子细胞在批式培养中的表现。批式培养过程中,抗体比生成速率随酵母抽提物浓度的提高而升高,浓度为10 g/L时获得最高抗体产量。通过采用细胞生长阶段低浓度、产物表达阶段高浓度的添加策略,酵母抽提物在动物细胞培养过程中可发挥巨大的应用价值。     

杜仲细胞悬浮培养产黄酮及其动力学研究

本文应用正交设计对杜仲细胞悬浮培养的基本培养基和植物生长物质浓度进行了筛选,并对影响杜仲细胞悬浮培养和总黄酮含量的不同因素进行了考察。结果表明,B5培养基+0.5mg/L NAA+0.6mg/L 6-BA、蔗糖30g/L、初始pH 5.0-5.5、接种量20g(FW)/L以及摇床转速110r/min为杜仲细胞悬浮培养的适宜条件。通过对杜仲悬浮细胞生长和代谢动力学的分析表明：杜仲细胞悬浮培养生长符合Logistic生长模型,最大比生长速率( m)为0.417d-1;细胞基于蔗糖的真正比生长得率(YG)与维持系数(m)分别为0.619g/g和0.0206g/(g·d-1);黄酮合成属部分生长耦联型,可用Luedeking-Piret模型进行描述。研究结果为杜仲细胞大规模悬浮培养生产天然活性成分奠定了基础。     

Kluyveromyces marxianus发酵己糖和戊糖生产乙醇

对利用底物广泛的乙醇发酵菌株马克斯克鲁维(Kluyveromyces marxianus)DL1菌株与工业用乙醇发酵菌株酿酒酵母(Saccharomyces cerevisiae)6525利用己糖(葡萄糖、甘露糖、半乳糖)和戊糖(木糖、阿拉伯糖)的情况进行对比研究。结果发现:以己糖为底物时,K.marxianus DL1均表现出细胞生长快、乙醇得率高的特点;在不通气、糖20 g/L条件下,K.marxianus DL1的最大乙醇质量浓度均比S.cerevisiae 6525高出10%左右,细胞量及乙醇生产强度分别是S.cerevisiae 6525的近2和1.7倍。当以戊糖为底物时,K.marxianus DL1可以利用木糖和阿拉伯糖;在不通气、糖20g/L条件下,K.marxianus DL1利用木糖产木糖醇和乙醇,乙醇终质量浓度可达7.68 g/L,木糖醇质量浓度为9.12 g/L;以阿拉伯糖为发酵底物时,阿拉伯糖醇的产量可达6 g/L左右;而S.cerevisiae 6525不能利用戊糖。马克斯克鲁维酵母比酿酒酵母更适合纤维乙醇生产。     

三种益生菌混合培养及共生机理研究

确定酪酸菌、肠膜芽孢杆菌与粪肠球菌三种菌混合工艺.研究了三种菌混合培养的生长曲线,混合批式传49代、混合连续培养考察三种菌的共存稳定性.三种菌无细胞上清液彼此之间均有促进生长作用,混合培养液的菌数较单独培养增加,在稀释率0.042/h,填充床连续培养11d,三种菌可稳定共存,但批式传49代过程中,肠膜芽孢杆菌有消失现象,而酪酸菌、粪肠球菌均较传代前增加了100倍.平板打孔生长圈法、点种法实验分别表明酪酸菌、肠膜芽孢杆菌对粪肠球菌有显著的促进作用,连续培养较批式传代可更好的研究菌际关系.并得到简单易行的复方益生菌剂组方方法.     

Studies on the Growth Characteristics and Dynamic Model of Spirulina Under Continuous Culture Conditions

The growth behavior, photosynthetic productivity and carbon utilizing characteristics of filamentous cyanobacterium Spirulina platensis Geitler were investigated in continuous cultures in a 10 L internalloop airlift photobioreactor. It was found that the cell density and the amount of carbon in the reactor increased and decreased with dilution rate respectively, and the relationships among them could well be expressed by the modified Monod equation. When dilution rate was 0.45/d, the rate of cell growth and that of carbon assumption reached their maximum points 0.362 g/(L·d) and 0.177 g/(L·d) respectively. The cell growth yield against carbon was 2.050 g/g. The proposed model of continuous growth fitted the experimental data quite well.     

Influence of specific growth rate on biomass yield, productivity, and compostion of Candida utilis in batch and continuous culture.

Candida utilis was grown in batch and continuous culture on prickly pear juice as sole carbon and energy source. In batch culture the maximum specific growth rate (mum) and the substrate yield coefficient (Yps) varied according to sugar concentration. When the fermentation was carried out with 1% sugar, mum and Ys were 0.47/h and 42.6%, respectively. The best yields occurred in a chemostat at the pH range of 3.5 to 4.5 and temperature of 30 C. A beneficial effect on Ys was observed when the dilution rate (D) was increased. At a D of 0.55/h, the productivity was 2.38 g/liter per h. The maintenance coefficient attained a value of 0.09 g of sugar/g of biomass per h. Increases of D produced higher protein contents of the biomass. The information obtained indicates that protein production with Candida utilis, using prickly pear juice, should be carried out a high dilution rates where the Ys and protein content of the cell mass are also higher.     

Influence of specific growth rate on biomass yield, productivity, and compostion of Candida utilis in batch and continuous culture.

Candida utilis was grown in batch and continuous culture on prickly pear juice as sole carbon and energy source. In batch culture the maximum specific growth rate (mum) and the substrate yield coefficient (Yps) varied according to sugar concentration. When the fermentation was carried out with 1% sugar, mum and Ys were 0.47/h and 42.6%, respectively. The best yields occurred in a chemostat at the pH range of 3.5 to 4.5 and temperature of 30 C. A beneficial effect on Ys was observed when the dilution rate (D) was increased. At a D of 0.55/h, the productivity was 2.38 g/liter per h. The maintenance coefficient attained a value of 0.09 g of sugar/g of biomass per h. Increases of D produced higher protein contents of the biomass. The information obtained indicates that protein production with Candida utilis, using prickly pear juice, should be carried out a high dilution rates where the Ys and protein content of the cell mass are also higher.     

Lipid accumulation in <Emphasis Type="Italic">Schizochytrium</Emphasis> G13/2S produced in continuous culture

Lipid and docosahexaenoic acid (DHA) accumulation into Schizochytrium G13/2S was studied under batch and continuous culture. Different glucose and glutamate concentrations were supplemented in a defined medium. During batch cultivation, lipid accumulation, 35% total fatty acids (TFA) occurred at the arithmetic growth phase but ceased when cell growth stopped. When continuous culture was performed under different glutamate concentrations, nitrogen-growth-limiting conditions induced the accumulation of 30–28% TFA in Schizochytrium. As the dilution rate decreased from 0.08 to 0.02 h⁻¹, both cell dry weight and TFA content of the cell increased. Under a constant dilution rate of 0.04 h⁻¹, carbon-limiting conditions decreased the TFA to 22%. Fatty acid profile was not affected by the different nutrient concentrations provided during continuous culture. Consequently, lipid accumulation can be induced through the carbon and nitrogen source concentration in the medium to maximise the TFA and subsequently DHA productivity by this microorganism.     

Kinetic analysis of the growth of Chlorella vulgaris

The energy of the total transmitted light was subtracted from that of the incident light in a culture vessel and the difference was divided by the weight of cells. The value thus obtained was defined as the amount, E(x), of light energy absorbed per unit cell weight per unit time.Batch and continuous cultures of Chlorella vulgaris were carried out at 30 degrees C in the pH range of 6.4-6.7 while restricting illumination. Next the specific growth rate, mu, in the batch culture and the fixed dilution rate, D, in the continuous culture were plotted against E(x). The results showed that the relation between D and E(x) can be expressed in a Michaelis-Menten equation, where the maximal specific growth rate is 0.24 h (-1) and the saturation constant is 6.58 kcal/g . h.Cell concentration calculated by substituting the apparent concentration, X(e), of incubated cells and the apparent maintenance constant, M(e), for this equation agreed with that observed in almost all growth phases. Furthermore, from the change of chlorophyll productivity and the relationship between D and E(x) expressed in this equation, it is assumed that E(x) involves the light energy directly utilized in photosynthesis in the cells and that which is converted into, e.g., heat. This equation also indicated that a maximum in the growth yield existed. Then the growth yield of 0.029 g/kcal obtained at the incident light of 1.46 or 2.63 cal/cm(2) . h was maximum (maximal conversion efficiency of light energy, 15.6%).These results indicate that this method of deriving the equation for the growth rate from this study is a useful procedure for obtaining bioengineering findings.     

Growth characteristics of Candida utilis on volatile substrate in a multistage tower fermentor.

The influence of increasing ethanol concentration in the feed on growth and physiological activity of the yeast Candida utlis was studied. The measurements were made at steady states of continuous culture under constant values of dilution rate, temperature, and pH in all stages of the fermentor; Synthetic ethanol was used as the sole source of carbon and energy in the concentration range 10-100 g/liter. The maximum biomass concentration in the effluent and maximum productivity was achieved at 75 g ethanol/liter in the feed. In respect to ethanol losses in the outlet and biomass yield, the optimum ethanol concentration in the input of the growth medium was found to be about 50 g/liter using a four-stage system.     

STUDIES OF THE GROWTH OF PENICILLIUM CHRYSOGENUM IN CONTINUOUS FLOW CULTURE WITH REFERENCE TO PENICILLIN PRODUCTION

SUMMARY: A filamentous mould was cultured by the continuous flow method in which medium is supplied at a constant rate and the culture volume is kept constant. Flow rates up to 0·1 culture volumes/hr were used. The mycelial dry weight concentration and the yield of mycelium/g of carbon source used were equal to or slightly greater than the maximum obtained in batch culture. With glucose concentrations up to 80 g/1. at a flow rate of 0·05 culture volumes/hr, about 45% of the substrate carbon was converted into mycelial carbon and the remainder oxidized to CO₂.
With unlimited amounts of all nutrients available growth of the mould followed the exponential law, as does bacterial growth, and therefore the mould had a constant doubling time.
The oxygen demand of the mould as function of growth rate was determined.
Conditions were found under which the rate of penicillin production/g of mycelium remained at its maximum value for 1000 hr.     

Physiology of the yeast Kluyveromyces marxianus during batch and chemostat cultures with glucose as the sole carbon source

Growth, substrate consumption, metabolite formation, biomass composition and respiratory parameters of Kluyveromyces marxianus ATCC 26548 were determined during aerobic batch and chemostat cultivations, using mineral medium with glucose as the sole carbon source, at 30 degrees C and pH 5.0. Carbon balances closed within 95-101% in all experiments. A maximum specific growth rate of 0.56 h(-1), a biomass yield on glucose of 0.51 g g(-1), and a maximum specific consumption of oxygen of 11.1 mmol g(-1) h(-1) were obtained during batch cultures. The concentration of excreted metabolites was very low at the culture conditions applied, representing 6% of the consumed carbon at most. Acetate and pyruvate were excreted to a larger extent than ethanol under the batch conditions, and the protein content accounted for 54.6% of the biomass dry weight. Steady states were obtained during chemostats at dilution rates of 0.1, 0.25 and 0.5 h(-1). At the two former dilution rates, cells grew at carbon limitation and the biomass yield on glucose was similar to that obtained under the batch conditions. Metabolite formation was rather low, accounting for a total of 0.005 C-mol C-mol(-1) substrate. At 0.5 h(-1), although the biomass yield on glucose was similar to the value obtained under the above-mentioned conditions, the cultivation was not under carbon limitation. Under this condition, 2-oxoglutarate, acetate, pyruvate and ethanol were the prevalent metabolites excreted. Total metabolite formation only accounted to 0.056 C-mol C-mol(-1) of substrate. A very high protein and a low carbohydrate content (71.9% and 9.6% of biomass dry weight, respectively) were measured in cells under this condition. It is concluded that K. marxianus aligns with the so-called aerobic-respiring or Crabtree-negative yeasts. Furthermore, it has one of the highest growth rates among yeasts, and a high capacity of converting sugar into biomass, even when carbon is not the limiting nutrient. These results provide useful data regarding the future application of K. marxianus in processes aimed at the production of biomass-linked compounds, with high yields and productivities.     

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.