SA/CS-CaCl2/PMCG微胶囊的生物相容性研究

介绍了一种新型多组份生物微胶囊体系——SA/CS-CaCl₂/PMCG微胶囊。考察了PMCG和SA/CS-CaCl²/PMCG微胶囊体系对大肠杆菌和酿酒酵母生长的影响,并用SA/CS－CaCl²/PMCG生物微胶囊进行了固定化培养大肠杆菌和酿酒酵母的研究。结果表明,与其它合成聚阳离子类似,PMCG组分对细胞生长有明显的抑制作用,但是在制胶囊过程中以及在用SA/CS-CaCl²/PMCG微胶囊对大肠杆菌和酿酒酵母培养过程中,都显示了良好的生物相容性,因此作为整个体系来说,该微胶囊可用于微生物细胞的固定化培养。       

新型生物微胶囊体系的生物相容性研究

一种由硫酸纤维素钠(NaCS)和聚二丙烯基二甲基氯化铵(PDADMAC)形成的新型生物微胶囊已开始被用于生物物质的固定化。根据生物物质生长的情况,考察了这两种固定化材料各自对微生物和动物细胞生长的副作用及由NaCS和PDADMAC形成的微胶囊对微生物细胞生长的影响。实验结果表明这个新微胶囊体系具有良好的生物相容性。     

叉鞭金藻固定化培养的初步研究

以海藻酸钙为载体,初步考察了CaCl2浓度、胶球大小、密度及初始细胞密度等条件：对叉鞭金藻固定化培养的影响,确定了该藻固定化生长的优化条件;当藻细胞密度大于10^6cells/ml,CaCl2浓度为0.15mol/L,在50ml培养液中加入150个微藻胶球时,藻细胞的生长量最大。与游离的叉鞭金藻相比,固定化叉鞭金藻生长速度慢,但生长周期长。     

海藻酸钠明胶协同固定化的研究

目的:研究不同因素对固定化微胶囊的影响以及不同物质向微胶囊扩散的规律。方法:采用海藻酸钠与明胶协同固定化制备微胶囊,考察了海藻酸钠、明胶浓度等因子对微胶囊直径与机械强度的影响,以及牛血清蛋白与葡萄糖向微胶囊扩散的状况,并利用非稳态传递模型计算了这两种物质在微胶囊中的有效扩散系数。结果:随着海藻酸钠质量浓度的升高,微胶囊的直径与机械强度逐渐增大。制备的最优条件是CaCl2浓度为10%,滴定速度为180滴/min,最优浸泡时间为30min。在此条件下,葡萄糖与牛血清蛋白的有效扩散系数分别为4.63×10-5cm2/min、1.01×10-7cm2/min。结论:海藻酸钠明胶协同固定化制备的微胶囊作为一种生物载体,非常适合细胞或酶的固定化。     

盐藻固定化培养的初步研究

以海藻酸钙为载体,考察了CaCl2浓度、胶球大小、密度及初始细胞密度等条件对盐藻固定化培养的影响,确定了该藻生长的优化条件：当藻 细胞密度大于10^6cell/ml,CaCl2浓度为0.15ml/L,注射用针头为6^#,在50ml培养液中加入150个微藻胶球时,藻细胞的生长量最大。     

海藻酸钙凝胶包埋法制备固定化小球藻

采用海藻酸钙凝胶包埋法对普通小球藻进行固定化,考察了海藻酸钠浓度、Ca Cl2浓度、胶球直径和胶球培养密度对固定化小球藻生长的影响,比较了游离和固定化小球藻细胞的生长特性,并测试了固定化小球藻的连续培养性能。结果表明,小球藻适宜的固定化条件为:海藻酸钠浓度2%(W/V)、Ca Cl2浓度1.5%(W/V)、凝胶球直径3 mm、凝胶球培养密度200粒/100 m L;与游离态小球藻相比,固定化小球藻的生长周期较长,在对数期后期和稳定期的生长态势优于游离态细胞,并可实现重复循环利用;连续培养实验显示,在优化条件下制备的固定化小球藻可连续使用200 h左右,有望用于生物催化和生物转化中的连续反应体系。     

生物脱硫菌根癌土壤杆菌UP-3的固定化研究

生物脱硫催化剂固定化研究对生物脱硫技术的推广应用具有重要的意义。该文以筛选出的具有脱硫能力的根癌土壤杆菌UP-3为固定化研究对象,二苯并噻吩(DBT)为生物催化脱硫的模型化合物,主要考察了菌株UP-3的培养条件、固定化方法和载体、固定化操作条件和固定化细胞的使用条件。结果表明：以桑特斯培养基在30℃下培养28h的根癌土壤杆菌UP-3具有最佳活性。采用3wt％海藻酸钠水溶液为包埋载体,液菌比为20：1,在4℃下1wt％CaCl2水溶液中固定化24h,得到的固定化细胞脱硫性能最好。在30℃下,反应6d可将浓度为625mg／L的DBT降解60％以上。     

保加利亚乳杆菌微胶囊化工艺研究

目的制备保加利亚乳杆菌微胶囊,提高菌株的酸、热耐受性及降低菌体的分离成本。方法以保加利亚乳杆菌(Lactobacillus bulgaricus)为研究对象,海藻酸钠(SA)为壳材、CaCl2为固化剂,制备保加利亚乳杆菌微胶囊;包埋率、颗粒平均化程度、机械强度等为考核指标,研究保加利亚乳杆菌微胶囊化的工艺。结果当海藻酸钠浓度为0.75%、CaCl2浓度为3%、电压为600V、泵速为1.96mL/min、震动频率为80Hz时,微胶囊化包埋效果最佳,经固定化后的菌微胶囊保持了良好的保加利亚乳杆菌的活性,微囊化保加利亚乳杆菌经过2次连续发酵后的产酸量分别达到59.4g/L和55.8g/L。结论本研究为工业化生产乳酸提供了一条具有经济价值的途径。     

PVA-卡拉胶混合载体固定化大肠杆菌-酵母菌混合体系生产谷胱甘肽

提出了ＰＶＡ－卡拉胶混合载体固定化微生物细胞的技术,确定了较好的制备工艺,并用该载体对大肠杆菌－酵母菌混合体系进行了固定化研究。结果表明：在ＰＶＡ浓度１０％,卡拉胶浓度０．５％,成型剂的ｐＨ值６．４,菌体量０．５ｇ／ｇ固定化细胞,固化时间３６ｈ的条件下,固定化细胞具有较好的机械强度和较高的酶活力。     

海藻酸钠/壳聚糖微胶囊固定化大肠杆菌的研究

本文以大肠杆菌ＤＨ5α为模型体系 ,探索了大肠杆菌ＤＨ5α用海藻酸钠 壳聚糖 (ＡＣＡ)微胶囊培养的可行性 ,并观察了微囊化大肠杆菌ＤＨ5α细胞生长与物料渗透性能 ,通过将ＡＣＡ微胶囊移植到实验组小鼠体内 ,考察了ＡＣＡ微胶囊作为口服药物载体的可能性。1　材料和方法1.1　材料壳聚糖 ,本实验室改性所得 ;海藻酸钠 ,ＫｅｌｃｏＤｉｖｏｆＭｅｒ ｃｋＣｏ .Ｉｎｃ .ＵＳＡ ;其它试剂均为国产分析纯。大肠杆菌ＤＨ5α ,长春生物制品所 ;ＬＢ培养基 ,华美生物制品公司提供。昆明系小白鼠 18～ 2 0ｇ ,解放军大连高等医学专科学校实验动物中…     

Ethanol production from nonsterilized carob pod extract by free and immobilized Saccharomyces cerevisiae cells using fed-batch culture

The production of ethanol from carob pod extract by free and immobilized Saccharomyces cerevisiae cells in batch and fed-batch culture was investigated. Fed-batch culture proved to be a better fermentation system for the production of ethanol than batch culture. In fed-batch culture, both free and immobilized S. cerevisiae cells gave the same maximum concentration (62 g/L) of final ethanol at an initial sugar concentration of 300 g/L and F = 167 mL/h. The maximum ethanol productivity (4.4 g/L h) was obtained with both free and immobilized cells at a substrate concentration of 300 g/L and F = 334 mL/h. In repeated fed-batch culture, immobilized S. cerevisiae cells gave a higher overall ethanol concentration compared with the free cells. The immobilized S. cerevisiae cells in Ca-alginate beads retained their ability to produce ethanol for 10 days. (c) 1994 John Wiley & Sons, Inc.     

Studies on immobilized Saccharomyces cerevisiae. III. Physiology of growth and metabolism on various supports

In earlier communications general analyses of rapid ethanol fermentation by Saccharomyces cerevisiae immobilized on inert supports were described. In this article physiology of growth and metabolism (parameters like rates of CO(2) evolution and O(2) uptake, respiratory quotient, and generation time) of Saccharomyces cerevisiae immobilized on different supports are reported. Values of the ratio of specific oxygen uptake rate for immobilized cells to free cells have been found to be 0.732, 0.781 and 0.785 for carrier A, carrier B, and covalently crosslinked controlled pore glass (CPG, specific surface area of 439 m(2) g(-1)), respectively. Rates of specific CO(2) evolution for immobilized cells to free cells for these supports are 0.784, 0.822, and 0.783, respectively. Marked reduction in generation time of Saccharomyces cerevisiae on all the supports has been observed. No change in size (4.8-5 mum) and specific growth rate (mu(m) = 0.275 h(-1)) of cells leaving the reactor has been observed.     

Improvement of the stability of glucose oxidase via encapsulation in sodium alginate–cellulose sulfate–poly(methylene-co-guanidine) capsules

Encapsulation of glucose oxidase (GOD) in polyelectrolyte complex capsules and its influence on properties of the enzyme is reported. The immobilization of GOD in the capsules made of sodium alginate (SA), cellulose sulfate (CS), poly(methylene-co-guanidine) (PMCG), CaCl₂ and NaCl (GOD–SA–CS/PMCG capsules) was achieved using a one-step highly reproducible encapsulation protocol which was monitored by a Electrospray Ionization-Mass Spectrometry (ESI-MS). A leakage of the enzyme from the capsules was negligible. Encapsulated GOD exhibited higher thermostability, wider range of pH optimum and improved storage stability in comparison with free GOD. The 92% retained activity by the encapsulated GOD after 45 biooxidation cycles was markedly higher than that of the GOD entrapped in calcium pectate gel beads showing no activity after 12 cycles. Optimization of conditions of oxygen supplementation resulted in increased oxygen availability within the GOD–SA–CS/PMCG capsules. Oxygen supplementation was accompanied with a mild decrease in the mechanical resistance of the SA–CS/PMCG capsules.     

Continuous production of glutathione using immobilized microbial cells containing ATP generating system

Acetate kinase reaction in Escherichia coli cells and glycolytic pathway in Saccharomyces cerevisiae cells were utilized as ATP generation systems for glutathione synthetic processes. These two ATP generation systems were well coupled with glutathione synthetase reactions and glutathione was produced by coimmobilized E. coli cells with dextran-bound ATP or by immobilized S. cerevisiae cells. The glycolytic pathway in S. cerevisiae cells was further utilized for the biosynthetic processes of other useful compounds.     

Improvement of the stability of glucose oxidase via encapsulation in sodium alginate–cellulose sulfate–poly(methylene-co-guanidine) capsules

Encapsulation of glucose oxidase (GOD) in polyelectrolyte complex capsules and its influence on properties of the enzyme is reported. The immobilization of GOD in the capsules made of sodium alginate (SA), cellulose sulfate (CS), poly(methylene-co-guanidine) (PMCG), CaCl₂ and NaCl (GOD–SA–CS/PMCG capsules) was achieved using a one-step highly reproducible encapsulation protocol which was monitored by a Electrospray Ionization-Mass Spectrometry (ESI-MS). A leakage of the enzyme from the capsules was negligible. Encapsulated GOD exhibited higher thermostability, wider range of pH optimum and improved storage stability in comparison with free GOD. The 92% retained activity by the encapsulated GOD after 45 biooxidation cycles was markedly higher than that of the GOD entrapped in calcium pectate gel beads showing no activity after 12 cycles. Optimization of conditions of oxygen supplementation resulted in increased oxygen availability within the GOD–SA–CS/PMCG capsules. Oxygen supplementation was accompanied with a mild decrease in the mechanical resistance of the SA–CS/PMCG capsules.     

Hydrolysis of lactose by immobilized microorganisms.

Cells of Lactobacillus bulgaricus, Escherichia coli, and Kluyveromyces (Saccharomyces) lactis immobilized in polyacrylamide gel beads retained 27 to 61% of the beta-galactosidase activity of intact cells. Optimum temperature and pH and thermostability of these microbial beta-galactosidases were negligibly affected by the immobilization. Km values of beta-galactosidase in immobilized cells of L. bulgaricus, E. coli, and K. lactis toward lactose were 4.2, 5.4, and 30 mM, respectively. Neither inhibition nor activation of beta-galactosidase in immobilized L. bulgaricus and E. coli appeared in the presence of galactose, but remarkable inhibition by galactose was detected in the case of the enzyme of immobilized K. lactis. Glucose inhibited noncompetitively the activity of three species of immobilized microbial cells. These kinetic properties were almost the same as those of free beta-galactosidase extracted from individual microorganisms. The activity of immobilized K. lactis was fairly stable during repeated runs, but those of E. coli and L. bulgaricus decreased gradually. These immobilized microbial cells, when introduced into skim milk, demonstrated high activity for converting lactose to monosaccharides. The flavor of skim milk was hardly affected by treatment with these immobilized cells, although the degree of sweetness was raised considerably.     

Effect of environmental growth conditions on plasmid stability, plasmid copy number, and catechol 2,3-dioxygenase activity in free and immobilized Escherichia coli cells

In order to better understand the high plasmid stability in immobilized recombinant E. coli cells, the effects of dilution rate on the pTG201 plasmid stability, the copy number, and the catechol 2,3-dioxygenase (encoded by XyIE gene) production were, at first, studied in free E. coli W3101 continuous cultures in minimal media. It was found that decreasing specific growth rate increased the plasmid copy number and the catechol 2,3-dioxygenase activity but the stability decreased. In continuous culture with immobilized cells, an increase was shown in plasmid copy number and catechol 2,3-dioxygenase activity probably due to the distribution of growth in the gel beads. Besides mechanical properties of gel beads which may allow limited cell divisions, the increase in plasmid copy number is involved in enhanced plasmid stability in immobilized cells. In the same way, an experiment conducted in LB medium dealing with competition between pTG201-free and pTG201-containing E. coli B cells was described. It was shown that the competition was not more pronounced in gel bead compared to a free system. The effects of nutritional limitations on pTG201 plasmid stability and catechol 2,3-dioxygenase activity during chemostat cultivations in free and immobilized E. coli B cells were also investigated. It was found that immobilization of cells increased the stability of pTG201 even under glucose, nitrogen, or phosphate limited cultures. However in the case of magnesium depleted culture, pTG201 was shown to be relatively instable and a decrease in viable cell number during the immobilized continuous culture was observed. By contrast to the free system, the catechol 2,3-dioxygenase activity increased in immobilized cells under all culture conditions used.     

固定化啤酒酵母细胞催化有机硅酮不对称还原

研究了固定化啤酒酵母细胞催化三甲基硅乙酮不对称还原反应,系统探讨了振荡速度、底物浓度、固定化细胞浓度、pH值和反应温度对反应速度、产率和产物光学纯度的影响。结果表明,上述因素对固定化啤酒酵母细胞催化三甲基硅乙酮不对称还原反应均有较显著的影响。振荡速度以150r/min为宜,底物浓度和固定化细胞浓度分别为14mmol/L和0.15g/mL较佳,适宜的pH值为7.3,最佳反应温度为25℃～30℃。在该优化反应条件下,反应最大产率和产物的光学纯度分别高达84.9%和90.2%ee。     

Coexistence of S. cerevisiae and E. coli in chemostat under substrate competition and product inhibition

A mixed culture of Saccharomyces cerevisiae and Escherichia coli was established in a stable coexistence steady state in a chemostat under constant operating conditions. The species competed for glucose, the growth-limiting resource, and produced acetate and ethanol. The acetic acid was shown to be very inhibitory to E. coli in pure culture at pH 5 while ethanol inhibition was only marginal. No significant inhibition of S. cerevisiae growth was observed by either acetate or ethanol. Pure culture parameters were measured and used in the analysis. Linearized stability analysis for the case when both organisms produce the inhibitor showed that a transition through three stable outcomes was possible as the feed concentration is lowered. Experimental studies verified these predictions, and successive transitions from a yeast growth steady state, to a coexistence steady state, and to an E. coli growth steady state were obtained by lowering the glucose concentration in the feed from 10 to 5 to 2.5 g/L, respectively. This dynamic behavior is distinct from the outcomes of other competition-inhibition combinations and experimentally demonstrates for the first time that coexistence is possible due to substrate competition and product inhibition.