The kinetic basis of the role of Ca++ ions for higher yield of citric acid in a repeated-batch cultivation system

The present investigation deals with role of Ca⁺⁺ ions in increasing the yield of citric acid in a repeated-batch cultivation system (working volume 9-1) and its kinetic basis. Five different hyper-producing strains of Aspergillus niger were evaluated for citric acid production using clarified cane-molasses as basal substrate. Among the cultures, NG^GCB101 (developed by u.v./chemical mutation in our labs) gave maximum production of citric acid i.e., 87.98 g/1, 6 days after mycelial inoculation. The addition of CaCl₂ to the culture medium promoted the formation of small rounded fluffy pellets (1.55 mm, diameter), which were desirable for citric acid productivity. CaCl₂ at a level of 2.0 M, added during inoculation time, was optimized for commercial exploitation of molasses. During repeated-batch culturing, a yield of citric acid monohydrate of 128.68 g/1 was obtained when the sampling vs. substrate feeding was maintained at 4-1 (44.50% working volume). The incubation period was reduced from 6 to only 2 days. The values of kinetic parameters such as substrate consumption and product formation rates revealed the hyperproducibility of citric acid by the selected Aspergillus niger NG^GCB101 (LSD = 0.456a, HS). Case studies are highly economical because of higher yield of product, lower energy consumption and the use of raw substrate without any additional supplementation.     

Improved development of human embryonic stem cell-derived embryoid bodies by stirred vessel cultivation

Human embryonic stem cells (hESCs) represent an important resource for novel cell-based regenerative medical therapies. hESCs are known to differentiate into mature cells of defined lineages through the formation of embryoid bodies (EBs) which are amenable to suspension culture for several weeks. However, EBs derived from hESCs in standard static cultures are typically non-homogeneous, leading to inefficient cellular development. Here, we systematically compare the formation, growth, and differentiation capabilities of hESC-derived EBs in stirred and static suspension cultures. A 15-fold expansion in total number of EB-derived cells cultured for 21 days in a stirred flask was observed, compared to a fourfold expansion in static (non-stirred) cultures. Additionally, stirred vessel mediated cultures have a more homogeneous EB morphology and size. Importantly, the EBs cultivated in spinner flasks retained comparable ability to produce hematopoietic progenitor cells as those grown in static culture. These results demonstrate the decoupling between EB cultivation method and EB-derived cells' ability to form hematopoietic progenitors, and will allow for improved production of scalable quantities of hematopoietic cells or other differentiated cell lineages from hESCs in a controlled environment.     

A mechanistic model for gas–liquid mass transfer prediction in a rocking disposable bioreactor

Rocking disposable bioreactors are a newer approach to smaller-scale cell growth that use a cyclic rocking motion to induce mixing and oxygen transfer from the headspace gas into the liquid. Compared with traditional stirred-tank and pneumatic bioreactors, rocking bioreactors operate in a very different physical mode and in this study the oxygen transfer pathways are reassessed to develop a fundamental mass transfer (k_La) model that is compared with experimental data. The model combines two mechanisms, namely surface aeration and oxygenation via a breaking wave with air entrainment, borrowing concepts from ocean wave models. Experimental data for across the range of possible operating conditions (rocking speed, angle, and liquid volume) confirms the validity of the modeling approach, with most predictions falling within ±20% of the experimental values. At low speeds (up to 20 rpm) the surface aeration mechanism is shown to be dominant with a of around 3.5 hr⁻¹, while at high speeds (40 rpm) and angles the breaking wave mechanism contributes up to 91% of the overall (65 hr⁻¹). This model provides an improved fundamental basis for understanding gas–liquid mass transfer for the operation, scale-up, and potential design improvements for rocking bioreactors.     

Establishing the scalable manufacture of primary human T-cells in an automated stirred-tank bioreactor

Advanced cell and gene therapies such as chimeric antigen receptor T-cell immunotherapies (CAR-T), present a novel therapeutic modality for the treatment of acute and chronic conditions including acute lymphoblastic leukemia and non-Hodgkin lymphoma. However, the development of such immunotherapies requires the manufacture of large numbers of T-cells, which remains a major translational and commercial bottleneck due to the manual, small-scale, and often static culturing systems used for their production. Such systems are used because there is an unsubstantiated concern that primary T-cells are shear sensitive, or prefer static conditions, and therefore do not grow as effectively in more scalable, agitated systems, such as stirred-tank bioreactors, as compared with T-flasks and culture bags. In this study, we demonstrate that not only T-cells can be cultivated in an automated stirred-tank bioreactor system (ambr® 250), but that their growth is consistently and significantly better than that in T-flask static culture, with equivalent cell quality. Moreover, we demonstrate that at progressively higher agitation rates over the range studied here, and thereby, higher specific power inputs (P/M W kg⁻¹), the higher the final viable T-cell density; that is, a cell density of 4.65 ± 0.24 × 10⁶ viable cells ml⁻¹ obtained at the highest P/M of 74 × 10⁻⁴ W kg⁻¹ in comparison with 0.91 ± 0.07 × 10⁶ viable cells ml⁻¹ at the lowest P/M of 3.1 × 10⁻⁴ W kg⁻¹. We posit that this improvement is due to the inability at the lower agitation rates to effectively suspend the Dynabeads®, which are required to activate the T-cells; and that contact between them is improved at the higher agitation rates. Importantly, from the data obtained, there is no indication that T-cells prefer being grown under static conditions or are sensitive to fluid dynamic stresses within a stirred-tank bioreactor system at the agitation speeds investigated. Indeed, the opposite has proven to be the case, whereby, the cells grow better under higher agitation speeds while maintaining their quality. This study is the first demonstration of primary T-cell ex vivo manufacture activated by Dynabeads® in an automated stirred-tank bioreactor system such as the ambr® 250 and the findings have the potential to be applied to multiple other cell candidates for advanced therapy applications.     

Effects of chronic exposure to simulated microgravity on skeletal muscle cell proliferation and differentiation

Cell culture models that mimic long-term exposure to microgravity provide important insights into the cellular biological adaptations of human skeletal muscle to long-term residence in space. We developed insert scaffolding for the NASA-designed rotating cell culture system (RCCS) in order to study the effects of time-averaged microgravity on the proliferation and differentiation of anchorage-dependent skeletal muscle myocytes. We hypothesized that prolonged microgravity exposure would result in the retardation of myocyte differentiation. Microgravity exposure in the RCCS resulted in increased cellular proliferation. Despite shifting to media conditions promoting cellular differentiation, 5 d later, there was an increase in cell number of approximately 62%, increases in total cellular protein (52%), and cellular proliferating cell nuclear antigen (PCNA) content (2.7 times control), and only a modest (insignificant) decrease (10%) in sarcomeric myosin protein expression. We grew cells in an inverted orientation on membrane inserts. Changes in cell number and PCNA content were the converse to those observed for cells in the RCCS. We also grew cells on inserts at unit gravity with constant mixing. Mixing accounted for part, but not all, of the effects of microgravity exposure on skeletal muscle cell cultures (53% of the RCCS effect on PCNA at 4-6 d). In summary, the mechanical effects of simulated microgravity exposure in the RCCS resulted in the maintenance of cellular proliferation, manifested as increases in cell number and expression of PCNA relative to control conditions, with only a modest reciprocal inhibition of cellular differentiation. Therefore, this model provides conditions wherein cellular differentiation and proliferation appear to be uncoupled.     

Packed bed bioreactor with porous ceramic beads for animal cell culture

A packed bed bioreactor was investigated as means for the cultivation of mammalian cells. The packed bed is comprised of porous ceramic particles with pores sufficiently large for cell immobilization as well as for intraparticle convective flow. In this way, the transport of limiting nutrients such as oxygen can be significantly enhanced, allowing maintenance of cell viability and productivity in an environment protective of adverse shear effects. The extent of intraparticle convective medium flow was experimentally quantified relative to the reactor operating conditions, and was found to be the dominant mechanism of nutrient transport to cells immobilized in the particle interior. An approximate linear relationship was obtained between overall reactor productivity and the extent of intraparticle convection. As the latter can be controlled at the single-particle level through total flow rate control, this relationship is a useful scale-up tool for the design of bioreactors. The high cell densities and the high volumetric productivities achieved by using small lab-scale reactors underline the potential of this simple bioreactor configuration for large-scale cell culture applications. (c) 1993 John Wiley & Sons, Inc.     

乳腺生物反应器的研究现状和产业化前景

转基因动物乳腺生物反应器是伴随转基因动物技术而发展起来的一项高新生物技术。利用这项技术,我们可以从动物乳汁中源源不断地获取用于医疗或保健目的的有生物活性的基因产物。这是一种全新的蛋白质生产模式,它将成为许多国家的重要支柱产业之一。本文介绍了乳腺生物反应器的基本概念和基本原理;概述了制备过程中的目的基因选择、载体构建、转基因等技术环节的研究现状;分析了乳腺生物反应器的优势及存在的问题,并就其产业化前景进行了展望。     

鸡输卵管上皮细胞瞬时表达系统(英文)

在开发利用生物反应器生产特定蛋白的研究中,若先用特异组织作原代培养,建立瞬时表达系统,对特定调控元件和融合基因进行分析,可大大缩短研究进程。本文首次报道用鸡输卵管上皮细胞原代培养, 建立瞬时表达系统的方法。输卵管细胞体外培养(Fig.1~3),在二、三周时间内仍能保持分泌卵清蛋白的功能。当分泌功能减弱时,若在培液中添加激素,一般一周后大部分细胞又可恢复分泌功能(Fig.4)。由于卵清蛋白是一种分泌蛋白,通过斑点免疫渗滤法可迅速简便的从培液中检测到(Fig.4)。为了验证培养细胞能否表达外源基因,在原代培养细胞中转染绿色荧光蛋白基因,可在细胞浆中显示绿色荧光(Fig.5),说明这是一个有效而又方便的检测调控元件的瞬时表达系统。     

Effect of membrane bioreactor configurations on sludge structure and microbial activity

The aim of this paper was to determine the effect of two different membrane bioreactor (MBR) configurations (external/immersed) on sludge structure and microbial activity. Sludge structure was deduced from rheological measurements. The high shear stress induced by the recirculation pump in the external MBR was shown to result in decreasing viscosity due to activated sludge (AS) deflocculation. Besides, soluble microbial products (SMP) release was higher in the external MBR (5 mg_COD g_MLVSS⁻¹) than in the immersed configuration (2 mg_COD g_MLVSS⁻¹). Microbial activity was followed from respirometry tests by focusing on the distinction between heterotrophs and autotrophs. An easier autotrophic microbe development was then observed in the immersed MBR compared to the external one. However, the external MBR was shown to allow better heterotrophic microbe development.     

Correlation between fouling propensity of soluble extracellular polymeric substances and sludge metabolic activity altered by different starvation conditions

Soluble extracellular polymeric substances (EPSs) cause membrane fouling in membrane bioreactors (MBRs), correlated with MBR sludge characteristics. Effects of F/M ratios on the evolution of soluble EPSs, fouling propensity of supernatants, and sludge metabolic activity were measured in this study in a two-period sequencing batch reactor (SBR). The experimental results show that fouling propensity was directly correlated with soluble-EPS concentration and composition. Sludge that had entirely lost active cells by long-term starvation released 64.4 ± 0.9 mg/L of humic acids, which caused a rapid increase in membrane resistance (40.67 ± 2.24 × 10¹¹ m⁻¹) during fouling tests. During short-term starvation, induced by incubation at a normal to low F/M ratio of 0.05 d⁻¹, sludge can use previously secreted utilization-associated products (UAPs) to maintain endogenous respiration. Therefore, the strategies of accumulating sludge and prolonging sludge retention time in MBRs may create long-term starvation and promote membrane fouling.