动物细胞培养用生物反应器设计原理

动物细胞培养用生物反应器设计和放大的关键问题是细胞破损与供氧和混合的矛盾,在分析细胞破损机理基础上,提出了动物细胞培养生物反应器的设计原理——设计模型和有关设计条件,从而清楚地确立了细胞死亡速度与培养基组成、反应器设计和操作参数间的定量关系,以及反应器设计应遵循的保证细胞生长和满足传质要求的条件。还对强化传质和抑制细胞破损这一矛盾作了简要分析和讨论。     

氧对膜生物反应器短程硝化的影响

为了研究膜生物反应器的短程硝化性能以及氧对短程硝化的影响,通过对比耗氧率和供氧率,提出了膜生物反应器短程硝化的控制优化建议。在膜生物反应器硝化过程中,DO小于1 mg/L开始出现亚硝氮积累;DO降到0.5 mg/L,出水氨氮浓度与亚硝氮浓度之比接近1∶1;DO调控在0.5-1 mg/L范围内,有利于前置硝化反应器与后续厌氧氨氧化反应器衔接。膜生物反应器中污泥浓度可达20 g/L,耗氧能力可达19.86 mg O2/(L·s),但最大供氧能力仅为0.369 mg O2/(L·s),供氧成为反应器运行的制约瓶颈,"低DO高流量"曝气是继续提高短程硝化效能的控制策略。     

植物生物反应器优化策略与最新应用*

随着分子生物学和植物基因工程的迅猛发展以及分子医药和现代农业等学科的交叉融合,植物生物反应器已成为分子医药农业的核心内容。利用植物生物反应器生产抗体、疫苗和功能性食品,具有规模化、成本低、安全性高、周期短等优势。2022年2月,加拿大卫生部批准了新型冠状病毒疫苗Covifenz^®,这是世界首款植物源人体疫苗,标志着以植物生物反应器为代表的分子医药农业时代的来临。综述植物叶片和种子等代表性的植物生物反应器类型,分析瞬时表达系统和稳定表达系统的构建原理和应用,探讨通过启动子和密码子优化、糖基化过程“人源化”、基因沉默抑制和蛋白酶作用抑制等优化植物生物反应器的策略,总结国内外抗体、疫苗和功能性食品等植物源产品的开发进展,以期为我国植物生物反应器的研究及其在分子医药领域的应用提供参考。     

生物可降解塑料的发酵生产研究进展*

近十几年来,随着化学合成塑料造成环境污染的日趋严重,微生物合成生物可降解塑料的研究受到人们的广泛重视.聚羟基烷酸(polyhydroxyalkanoates,PHA)具有与化学合成塑料相似的性质,能拉丝、压模、注塑等,而且具有合成塑料所没有的特殊性能,如利用其生物相容性可作为外科手术缝线、人造血管和骨骼代用品,术后无需取出.因而在工业、农业、医药和环保等行业都具有广阔的应用前景.     

固定化增殖酵母10m^3生物反应器连续生产酒精的研究

将经过驯化的酒精酵母,用海藻酸钙凝胶包埋法固定化,再用硫酸钴处理。在形成的凝胶中含有微量的甾醇和不饱和脂肪酸,以提高细胞的存活率。反应器系统由三个１０ｍ３稍加改造的普通发酵罐组成。用经过酸化处理的甜菜糖蜜为原料,采用逐步提高糖浓度的方法连续生产高浓度酒精,酒精含量为１０％（Ｖ／Ｖ）以上。发酵过程中通入微量无菌空气。酒精生产能力为５１．７５ｋｇ／ｍ３凝胶·ｈ－１,停留时间为１．８ｈ。反应器内形成的大量ＣＯ２通畅排出。反应器具有良好的操作稳定性。反应器容积生产强度为８．３ｋｇ／ｍ３·ｈ     

光生物反应器脱除空气中CO2的模型研究

微藻光生物反应器具有脱除空气中CO₂能力。从光生物反应器构型、进气流速、混合传质,及微藻光合/呼吸速率等方面,探讨气升式光生物反应器脱除空气中CO₂效果,提出了时间离散化和集中参数法两种分析方法。运用集中参数法建立了气升式柱型光生物反应器脱除CO₂的数学模型,模拟了藻液中溶氧浓度（DO）、pH随时间的变化情况,及进气CO₂浓度影响,预测并验证了光照条件下出气CO₂、O2浓度的变化趋势。模拟结果和实验数据基本吻合,所提出的模型对光生物反应器的优化设计、微藻的高密度培养,及CO2去除能力预测具有参考意义。     

利用粉丝废液固定化红曲发酵生产红曲色素的研究*

对以粉丝生产废液为主要培养基,以聚乙烯醇海藻酸钠双载体固定红曲Monascuspurpureus,采用气升式生物反应器重复发酵生产红曲色素进行了考察研究.试验结果表明:粉丝生产废液经适当补加营养盐可作为发酵生产红曲色素的良好培养基,其最佳发酵条件为:发酵培养基初始pH值为5~6;发酵温度为30℃;固定化细胞粒子接入量为20%,通气量为0.35vvm,发酵周期为50h左右。     

厌氧反应器中颗粒污泥的培育及应用研究进展*

厌氧生物处理技术因其具有有机负荷高、污泥产量低、能耗低等优点被广泛应用于各种废水处理中。厌氧颗粒污泥具有沉降性能好、微生物浓度高、有机负荷高等优点,极大地提高了废水处理效率。尤其在处理含高氨氮废水中,厌氧颗粒污泥的形成对反应器的高效生物脱氮至关重要。但到目前为止,厌氧反应器中的颗粒污泥形成及废水处理效果还缺乏系统的认识。鉴于此,总结了厌氧反应器中颗粒污泥的形成机制,分析了影响厌氧反应器中颗粒污泥形成的因素,论述了厌氧反应器中厌氧颗粒污泥生长的模拟,最后介绍了厌氧颗粒污泥在国内外的主流应用。厌氧反应器中颗粒污泥的形成是综合因素影响的结果,对影响厌氧颗粒污泥形成的每个因素都需要认真对待,可为在厌氧反应器中颗粒污泥的培育和应用提供理论指导和技术支撑。     

生物絮凝剂的最新研究进展及其应用*

从絮凝剂的来源和分子组成两方面对生物絮凝剂进行了系统分类,综述了生物絮凝剂产生菌的筛选模型以及生物絮凝剂在水处理和发酵工业中的应用,详细阐述了目前国内外提出的几种不同的生物絮凝剂絮凝机理,进而在此基础上剖析了目前生物絮凝剂研究工作中仍然存在的问题,并提出生物絮凝剂今后的主要研究方向。     

生物处理策略改善麸皮酚类化合物的生物可及性*

麸皮为谷物加工副产物,麸皮酚类物质具有重要的营养特性和药理效应,但麸皮酚类物质大多以结合态形式存在,生物可及性较低,如何实现麸皮中酚类物质有效释放,提高生物利用度存在挑战。综述了麸皮酚类化合物营养特性及其存在形式,以及酶促降解法、微生物发酵法等生物处理策略在提高酚类生物可及性的研究进展;并指出,麸皮预处理技术耦合混菌发酵技术是驱动麸皮酚类物质高效释放的有效途径。探究混合菌种体系的互作关系及其作用机制,关联预处理麸皮的结构变化与降解增效之间的关系,为麸皮高附加值利用以及相关功能性食品开发提供理论依据。     

Use of computational fluid dynamics as a tool for establishing process design space for mixing in a bioreactor

The concept of "design space" plays an integral part in implementation of quality by design for pharmaceutical products. ICH Q8 defines design space as "the multidimensional combination and interaction of input variables (e.g., material attributes) and process parameters that have been demonstrated to provide assurance of quality. Working within the design space is not considered as a change. Movement out of the design space is considered to be a change and would normally initiate a regulatory post-approval change process. Design space is proposed by the applicant and is subject to regulatory assessment and approval." Computational fluid dynamics (CFD) is increasingly being used as a tool for modeling of hydrodynamics and mass transfer. In this study, a laboratory-scale aerated bioreactor is modeled using CFD. Eulerian-Eulerian multiphase model is used along with dispersed k-ε turbulent model. Population balance model is incorporated to account for bubble breakage and coalescence. Multiple reference frame model is used for the rotating region. We demonstrate the usefulness of CFD modeling for evaluating the effects of typical process parameters like impeller speed, gas flow rate, and liquid height on the mass transfer coefficient (k(L)a). Design of experiments is utilized to establish a design space for the above mentioned parameters for a given permissible range of k(L)a.     

Computational fluid dynamics modeling of mass-transfer behavior in a bioreactor for hairy root culture. II. Analysis of ultrasound-intensified process

Recently, cichoric acid production from hairy roots of Echinacea purpurea was significantly improved by ultrasound stimulation in an airlift bioreactor. In this article, the possible mechanism on ultrasound-intensified hairy root culture of E. purpurea in the bioreactor was elucidated with the help of computational fluid dynamics (CFD) simulation, membrane permeability detection, dissolved oxygen concentration detection, confocal laser-scanning microscopy (LSM) observation, and phenylalanine ammonium lyase (PAL) activity analysis. The CFD model developed in Part I was used to simulate the hydrodynamics and oxygen mass transfer in hairy root bioreactor culture stimulated by ultrasound. A dynamic mesh model combined with a changing Schmidt number method was used for the simulation of the ultrasound field. Simulation results and experimental data illustrated that ultrasound intensified oxygen mass transfer in the hairy root clump, which subsequently stimulated root growth and cichoric acid biosynthesis. Ultrasound increased the hairy root membrane permeability, and a high root membrane permeability of 0.359 h(-1) was observed at the bottom region in the bioreactor. LSM observation showed that the change in the membrane permeability recovered to normal in the further culture after ultrasound stimulation. PAL activity in the hairy roots was stimulated by ultrasound increase and was correlated well to cichoric acid accumulation in the hairy roots of E. purpurea.     

Oxygen transfer effects in serine alkaline protease fermentation by Bacillus licheniformis: use of citric acid as the carbon source

The effects of oxygen transfer on serine alkaline protease (SAP) production by Bacillus licheniformis on a defined medium with C_c = 9.0 kg m⁻³ citric acid as sole carbon source were investigated in 3.5 dm³ batch bioreactor systems. The concentrations of the product (SAP) and by-products, i.e., neutral protease, amylase, amino acids, and organic acids were determined in addition to SAP activities. At Q_o/V = 1 vvm air flow rate, the effect of agitation rate on DO concentration, pH, product, and by-product concentrations and SAP activity were investigated at N = 150, 500, and 750 min⁻¹; these are named as low-(LOT), medium-(MOT), and high oxygen transfer (HOT) conditions. LOT conditions favor biomass concentration; however, substrate consumption was highest at HOT conditions. MOT was optimum for maximum SAP activity which was 441 U cm⁻³ at t = 37 h. The total amino acid concentration was maximum in LOT and minimum in MOT conditions; lysine had the highest concentration under all oxygen transfer conditions. Among organic acids, acetic acid had the highest concentration and its concentration increased with oxygen transfer rate. The oxygen transfer coefficient increases with the agitation rate and the oxygen consumption rate increased almost linearly with the biomass concentration.     

Influence of dissolved oxygen concentration on intracellular pH for regulation of Aspergillus niger growth rate during citric acid fermentation in a stirred tank bioreactor

In this paper we report the regulation of Aspergillus niger growth rate during citric acid fermentation in a stirred tank bioreactor. For this, the influence of dissolved oxygen concentration in a medium on intracellular pH values and consequently on overall microbial metabolism was emphasized. Intracellular pH of mycelium grown under different concentrations of dissolved oxygen in the medium was determined. Sensitivity of proteins toward proton concentration is well recognized, therefore pH influences on the activities of key regulatory enzymes of Aspergillus niger were determined at pH values similar to those detected in the cells grown under lower dissolved oxygen concentrations. The results have shown significantly reduced specific activities of hexokinase, 6-phosphofructokinase and glucose-6-phosphate dehydrogenase in more acidic environment, while pyruvate kinase was found to be relatively insensitive towards higher proton concentration. As expected, due to the reduced specific activities of regulatory enzymes under more acidic conditions, overall metabolism should be hindered in the medium with lower dissolved oxygen concentration which was confirmed by detecting the reduced specific growth rates. From the studies, we conclude that dissolved oxygen concentration affects the intracellular pH and thus growth rate of Aspergillus niger during the fermentation process.     

Mechanism of nitrate uptake into Chara corallina cells: lack of evidence for obligatory coupling to proton pump and a new NO3−/NO3− exchange model

Abstract. Nitrate uptake into Chara corallina cells at different external pH (pH_o) after different NO₃⁻ pretreatment conditions has been investigated. Following NO₃⁻ pretreatment (0.2 mol m⁻³ NO₃⁻) there was little effect of pH_o on subsequent net NO₃⁻ uptake into Chara cells. After N deprivation (2 mmol m⁻³ NO₃⁻) there was a pronounced effect of pH_o on nitrate uptake, the maximum rate occurring at pH_o 4.7. There was no consistent relationship between OH⁻ efflux and NO₃⁻ uptake in short term experiments (< 1 h). NO₃⁻ efflux was also sensitive to pH_o, the maximum rate occurring at ∼ pH_o 5.0. An inhibitor of the proton pump, DES, immediately stimulated NO₃⁻ uptake into cells pretreated with NO₃⁻ and prevented the time-dependent decrease in NO₃⁻, uptake into Chara cells that had been previously treated with low N (2 mmol m⁻³ NO₃⁻). NO₃⁻ efflux was found to be very sensitive to DES with K_i= 0.7 mmol m⁻³. At the optimum pH_o for NO₃⁻ uptake the effect of DES on membrane potential (ψ_m) were slight, and only apparent after 30 min. The results are interpreted in context of current models relating NO₃⁻ uptake and H⁺ pump activity. A new model for NO₃⁻ uptake is proposed which involves NO₃⁻/NO₃⁻ exchange at steady state.     

Development of a continuous cell-recycle fermentation system for production of lactic acid by Lactobacillus paracasei

Experimental devices for stimulating productivity of lactic acid fermentation were installed and an electromagnetic flow-meter and a pneumatic diaphragm pump were employed to alleviate the fouling of the membrane and to improve the durability of membrane cell-recycle bioreactors (MCRBs). In this case, the continuous fermentation using a 5 L automatic fermentor lasted stably over 150 h, and could repeat periodically with simple intermittent on-line cleaning and sterilization of the membrane filtration system. Maximum value of OD₆₂₀ of 98.7 was obtained, six times greater than that of the fed-batch fermentation. Meanwhile, maximum productivity of 31.5 g/(L h) was recorded, 10 times greater than that occurred in the fed-batch fermentation. Compared with conventional MCRBs, the MCRB system with a diaphragm pump and tangential flow-rate controlling was more stable and durable. The tangential velocity of membrane module could be monitored and controlled on-line, and the possibility of contamination due to hose rupture could be eliminated.     

重组枯草芽孢杆菌发酵生产乳铁蛋白N叶工艺优化北大核心CSCD

为实现乳铁蛋白N叶的大规模制备,本研究对表达乳铁蛋白N叶的工程菌枯草芽孢杆菌pMA0911-D60Y/Y92D进行了发酵工艺的优化。确定了最佳的培养条件:以葡萄糖为最佳碳源,以胰蛋白胨为最佳氮源,在pH 7.0、温度28℃、发酵25.5 h条件下诱导表达目的蛋白,目的蛋白的IOD值高达68.03%。在10L发酵罐上对重组菌株的发酵条件进行优化,获得如下的最佳发酵工艺,即采用300 r/min转速,0-7 h时,在pH 7.5、30℃条件下培养菌体;7-25 h时,在pH 7.0、28℃条件下诱导表达目的蛋白。发酵结束后,收集细胞并破碎后取上清液用HisTrapHP亲和层析及SuperdexTM200(10/300GL)亲和层析法对细胞上清液进行纯化至均一条带,获得了纯度>94%的重组乳铁蛋白N叶,1 L菌体能制备23.5 mg纯蛋白。本研究为重组牛乳铁蛋白N-叶的高效制备奠定了基础。     

The case for cytosolic NO3– heterostasis: a critique of a recently proposed model

A model recently proposed by Siddiqi & Glass (Plant, Cell, and Environment 25, 1211–1217, 2002) attempts to reconcile discrepancies in the measurement of cytosolic nitrate concentrations ([NO₃^–]_cyt) in plant root cells, specifically between low (～ 4 mm ) homeostatic values reported in studies using ion‐specific microelectrodes on the one hand, and wide fluctuations in [NO₃^–]_cyt reported in other studies, especially those using compartmental analysis by tracer efflux (CATE). Although Siddiqi & Glass concede that cytosolic NO₃^– homeostasis, as determined by microelectrodes, is at odds with certain experimental observations, they nevertheless promote a model that takes microelectrode readings at face value, and assert that the variations seen using CATE methodology are artefacts attributable to contributions from substantial, rapidly exchanging, and highly variable NO₃^– pools putatively residing in organelles such as plastids and the endoplasmic reticulum. We show here that such a model is not tenable, drawing upon experimental evidence from previous studies, and from a more comprehensive model that examines the characteristics and consequences of subcompartmented cytoplasmic exchange in root cells.     

Solid state fermentation for production of α-amylase by a thermotolerant Bacillus subtilis from hot-spring water

The production of extracellular α-amylase by thermotolerant Bacillus subtilis was studied in solid state fermentation (SSF). The effect of wheat bran (WB) and rice husk (RH) was examined. The appropriate incubation period, moisture level, particle size and inoculum concentration was determined. Maximum yields of 159,520 and 21,760 U g⁻¹ were achieved by employing WB and RH as substrates in 0.1 M phosphate buffer at pH 7 with 30% initial moisture content at 24 and 48 h. Particle size and inoculum concentration were found to be 1000 μm, 20% and 500 μm, 15% for WB and RH, respectively. Enzyme yield was 7.3-fold higher with WB medium compared with RH.     

Production and optimization of process parameters for alkaline protease production by a newly isolated Bacillus sp. under solid state fermentation

Production of alkaline protease employing the laboratory isolate, Bacillus sp. under solid state fermentation (SSF) was optimized. The effect of wheat bran and lentil husk was examined. Wheat bran showed highest enzyme production. The appropriate incubation time, inoculum size, moisture level and buffer solution level were determined. Maximum yields of 429.041 and 168.640 U g⁻¹ were achieved by employing wheat bran and lentil husk as substrates in 0.1 M carbonate/bicarbonate buffer at pH 10 with 30 and 40% initial moisture level at 24 h. Inoculum size and buffer solution level were found to be 20 and 25% and 0.5:1 for wheat bran and lentil husk, respectively.