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Numerical simulation of effects of reactor dimensions on isothermal CVI process of C/SiC composites

机译:反应器尺寸对C / SiC复合材料等温CVI工艺影响的数值模拟

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A two-dimensional axisymmetrical mathematical model taking into account the transport phenomena of momentum, energy and mass in conjunction with the infiltration induced changes of the preform structure were implemented to simulate the effects of the reactor dimension on the isothermal CVI process of C/SiC composites. The effects of the reactor inlet dimension and the reactor diameter on the concentration distribution and the time-dependent densification behaviors of C/SiC composites were studied. The reactor inlet dimension was found to impose trivial effects on the ICVI process of C/SiC composites. Calculation results show that the mean MTS molarity in preform and the global density increase firstly and then decrease with the elevating reactor diameter at any given infiltration time though the MTS molarity gradients drops gradually with the elevating reactor diameter. The preferable reactor diameter is implied to be 90 mm for the preform taken. Calculation results of the densification behavior of C/SiC composites during the ICVI process imply that the reactor diameter does not evidently influence both the rules of densification and the absolute values of the density. (C) 2008 Elsevier B.V. All rights reserved.
机译:建立了考虑动量,能量和质量的传输现象以及渗透引起的瓶坯结构变化的二维轴对称数学模型,以模拟反应器尺寸对C / SiC复合材料等温CVI工艺的影响。研究了反应器入口尺寸和反应器直径对C / SiC复合材料浓度分布和时间依赖性致密化行为的影响。发现反应器入口尺寸对C / SiC复合材料的ICVI工艺产生了微不足道的影响。计算结果表明,在任何给定的渗透时间内,预成型坯的平均MTS摩尔浓度和整体密度先随反应器直径的增大而增大,然后随反应器直径的增大而逐渐减小,但随反应器直径的增大而减小。对于所采用的预型件,优选的反应器直径暗示为90mm。 ICVI过程中C / SiC复合材料的致密化行为的计算结果表明,反应器直径不会明显影响致密化规则和密度的绝对值。 (C)2008 Elsevier B.V.保留所有权利。

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