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Chemical vapor deposition of silicon carbide in a hot wall reactor.

机译:在热壁反应器中化学气相沉积碳化硅。

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The chemical vapor deposition (CVD) of silicon carbide (SiC), prepared in a hot wall tubular reactor at atmospheric pressure, has been investigated experimentally and theoretically. The gas mixture of methyltrichlorosilane (MTS), hydrogen and argon was chosen as the precursor gas. In order to explore the behavior of such a CVD process quantitatively, a detailed finite difference model, which describes the coupled hydrodynamics, mass transport and chemical reaction occurring in the reactor during the deposition, has been developed. In the model analysis, the nonisothermal temperature profile within the reactor, based on experimental measurements, was taken into account. The governing equations in the model formulation were developed in the cylindrical coordinate, and solved numerically along with appropriate boundary conditions. The model predicts the profiles of MTS concentration and deposition rate as functions of the processing variables such as reactor temperature profiles, inlet flow rates of the gas mixture, and inlet MTS mole fraction. Experimentally, evaluations of SiC coatings were conducted at 850{dollar}spcirc{dollar}-1200{dollar}spcirc{dollar}C with a laboratory-scale CVD system.; By combining the model calculations with experimental data of the deposition rates, a kinetic rate expression of CVD-SiC from the gas mixture was obtained. The deposition rate has an Arrhenius-type dependence on temperature and is a first-order with respect to the MTS concentration. Estimated activation energy is 254 kJ/mol. Predicted deposition rate profiles by the model incorporated with this developed kinetic mechanism showed excellent agreement with experimental data over a variety of applied deposition conditions.; The flow rate of gas mixture affects the deposition rate and deposition uniformity more at higher temperatures than at lower temperatures. X-ray diffraction analysis indicated that pure {dollar}beta{dollar}-SiC deposits were obtained only when appropriate deposition temperature and the molar ratios of "(H{dollar}sb2{dollar}+Ar)/MTS" were applied.; In addition, parametric analysis showed that the temperature, temperature gradient and the flow rate are important processing parameters in controlling the deposition uniformity. With the model simulation, optimization of the deposition process becomes conceivable.
机译:已经在实验和理论上研究了在热壁管式反应器中制备的碳化硅(SiC)的化学气相沉积(CVD)。选择甲基三氯硅烷(MTS),氢气和氩气的混合气体作为前驱气体。为了定量地研究这种CVD工艺的行为,已经开发了详细的有限差分模型,该模型描述了沉积过程中在反应器中发生的耦合的流体动力学,传质和化学反应。在模型分析中,考虑了基于实验测量值的反应器内的非等温温度分布。在圆柱坐标系中建立了模型公式中的控制方程,并在适当的边界条件下进行了数值求解。该模型根据处理变量(例如反应器温度曲线,气体混合物的入口流速和入口MTS摩尔分数)预测MTS浓度和沉积速率的曲线。实验上,采用实验室规模的CVD系统,在850℃到1200℃下对SiC涂层进行了评估。通过将模型计算与沉积速率的实验数据相结合,从混合气体中获得了CVD-SiC的动力学速率表达式。沉积速率对温度具有阿累尼乌斯(Arrhenius)型依赖性,并且相对于MTS浓度是一阶的。估计的活化能为254 kJ / mol。通过与这种发达的动力学机制结合的模型预测的沉积速率曲线表明,在各种应用的沉积条件下,该数据与实验数据极为吻合。气体混合物的流速在较高温度下比在较低温度下更影响沉积速率和沉积均匀性。 X射线衍射分析表明,仅当采用适当的沉积温度和“(H {sb2 {dol} + Ar)/ MTS”的摩尔比”时,才能获得纯的{beta} {dollar} -SiC沉积物。另外,参数分析表明温度,温度梯度和流速是控制沉积均匀性的重要工艺参数。通过模型仿真,可以想到沉积过程的优化。

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