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ENHANCED MASS TRANSPORT THROUGH PERMEABLE POLYMER MICROCIRCULATORY NETWORKS

机译:通过渗透性聚合物微循环网络增强质量的运输

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One of the obstacles of culturing functioning vital tissues in vitro is to obtain a substantial biomass at a physiological cell density ( > 10~8 cells/cm~3). At this high density, the diffusion length of metabolites is limited to ~100um. As a matter of fact, in real tissue, almost all the cells are located within 100μm distance from the capillaries [1]. Studies [2, 3] also confirmed that the cells in the artificial tissue cannot be properly cultured when they are further than 400um from the external nutrient source. Therefore, to culture three dimensional artificial tissue with substantial biomass, vascularization is necessary to enhance the metabolites transport.The short diffusion length of the metabolites requires high capillary density ( > 100/mm~2) in vascularization. To meet this need, we have developed a novel high resolution and high speed 3D microfabrication technique, the projection microstereolithography[4] to explore microcirculatory networks with high density ( > 150/mm~2). Using this technology we designed and fabricated the microreactors as shown in Figure 1. In our samples, 800um PEG microcapillaries with 20um inner radius and 40um outer radius with pitch of 96um are fabricated. Two rings as inlet and outlet are connected to external supply of culture medium. We designed the parameters of the vascularized microbioreactor based on the simulations of oxygen and carbon dioxide transport and metabolism in hepatocytes. As shown in Figure 2, the capillaries are arranged in a hexagonal way. According to the geometric symmetry, the final simulation domain is divided into 2 regions, the polymer capillary wall and the tissue. We assumed that a culture media with dissolved oxygen is pumped through the capillaries at 1.5mm/s rate and diffuses through the capillary wall, into the hepatocytes. The consumption of oxygen follows Michaelis-Menten kinetics [5, 6] and the metabolic rate of carbon dioxide is assumed to be proportional to that of oxygen by a fixed quotient (-0.81) which is addressed and studied by other groups [7]. The carbon dioxide diffuses into the capillaries and can be carried away through the flow of the culture medium. Our simulation indicates that the bottleneck of effective oxygen transport is the permeability of the polymer materials. The oxygen concentration drops off about 90% after diffusing through the capillary wall. It is predicted that the diffusion length at the inlet is 74um and 48um at the outlet; the rapid drop of carbon dioxide concentration also happens across the capillary wall. The predicted carbon dioxide concentration in the tissue is ~80nmol/cm~3; this value is much smaller than the toxic value (100mmHg or 3umol/cm~3) reported by David Gray and coworkers [8]. In Figure 2, we present the effect of the permeability of the capillary polymer materials on the diffusion length of oxygen and the concentration of carbon dioxide in the tissue. Our study indicates the existence of an optimal permeability for the capillary network, at which the overall diffusion length of oxygen is maximized. Interestingly, we also found a maximum concentration of carbon dioxide in the cultured tissue as the permeability of the polymer material changes. We attribute it to the competition between the tissue thickness and the permeability. Higher permeability increases the cultured tissue thickness, and also increases the ability of capillary to empty carbon dioxide. Not only is this model applicable for oxygen and carbon dioxide, but also for the transport of other metabolites. As an ongoing experimental effort, our fluorescent microscopy measurement validated the diffusion transport of fluorescent species from the capillary (Figure 3). Experiments are also in progress on the oxygen diffusion from the capillaries will cell cultures of high density on the PEG scaffold by introducing proper indicators. In summary, we have established a method to design and manufacture vascularized microcirculatory network to enhance t
机译:体外培养功能性重要组织的障碍之一是在生理细胞密度(> 10〜8细胞/ cm〜3)下获得大量生物质。在这种高密度下,代谢物的扩散长度被限制在〜100um。事实上,在实际组织中,几乎所有细胞都位于距离毛细血管100μm的距离内[1]。研究[2,3]还证实,当来自外部营养源的距离超过400um时,人造组织中的细胞无法正确培养。因此,要培养具有大量生物量的三维人工组织,必须进行血管化以增强代谢物的运输。代谢物的短扩散长度要求血管化中的毛细血管密度高(> 100 / mm〜2)。为了满足这一需求,我们开发了一种新颖的高分辨率和高速3D微制造技术,即投影微立体光刻技术[4],以探索高密度(> 150 / mm〜2)的微循环网络。使用该技术,我们设计并制造了微反应器,如图1所示。在我们的样品中,制造了800um内径为20um,外径为40um,间距为96um的PEG微毛细管。两个环作为入口和出口连接到培养基的外部供应。我们基于氧和二氧化碳在肝细胞中的运输和代谢的模拟,设计了血管化微生物反应器的参数。如图2所示,毛细管以六边形的方式排列。根据几何对称性,最终的模拟域分为聚合物毛细管壁和组织两个区域。我们假设溶解有氧气的培养基以1.5mm / s的速度泵送通过毛细血管,并通过毛细血管壁扩散到肝细胞中。氧气的消耗遵循Michaelis-Menten动力学[5,6],并且二氧化碳的代谢速率被假定与固定比率(-0.81)的氧气成比例,其他小组对此进行了研究和研究[7]。二氧化碳扩散到毛细管中,并可以通过培养基流带走。我们的模拟表明,有效氧传输的瓶颈是聚合物材料的渗透性。在通过毛细管壁扩散后,氧气浓度下降了约90%。可以预测,入口处的扩散长度为74um,出口处的扩散长度为48um。二氧化碳浓度的迅速下降也发生在整个毛细管壁上。预计组织中的二氧化碳浓度为〜80nmol / cm〜3;该值远小于David Gray及其同事报道的毒性值(100mmHg或3umol / cm〜3)[8]。在图2中,我们介绍了毛细管聚合物材料的渗透性对组织中氧气扩散长度和二氧化碳浓度的影响。我们的研究表明,毛细管网络存在最佳渗透率,在该渗透率下,氧气的总扩散长度最大。有趣的是,我们还发现,随着聚合物材料渗透性的变化,培养组织中二氧化碳的最大浓度。我们将其归因于组织厚度和渗透性之间的竞争。较高的渗透性增加了培养的组织厚度,并且还增加了毛细管排空二氧化碳的能力。该模型不仅适用于氧气和二氧化碳,还适用于其他代谢物的运输。作为正在进行的实验工作,我们的荧光显微镜测量验证了荧光物质从毛细管的扩散传输(图3)。通过引入合适的指示剂,关于从毛细管中的氧扩散将在PEG支架上进行高密度细胞培养的实验也在进行中。综上所述,我们建立了一种设计和制造血管化微循环网络的方法,以增强

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