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Kinetic modeling of tungsten silicide chemical vapor deposition from WF6 and Si2H6: Determination of the reaction scheme and the gas-phase reaction rates

机译:WF6和Si2H6沉积硅化钨化学气相的动力学模型:反应方案和气相反应速率的确定

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Kinetic studies were carried out on tungsten silicide (WSix) chemical vapor deposition from WF6/Si2H6 in a hot-wall type tubular reactor, focusing on the axial distributions of step coverage and composition ratio. The growth-rate profile within the tubular reactor showed exponential decay, which suggests first-order reaction kinetics. The silicon content of the film increased downstream in the reactor, but the step coverage quality was independent of axial position. The reactive sticking probabilities obtained from the step coverage profile were about 0.33. Two reaction models were investigated to explain these experimental results. The first model is a parallel deposition model, in which W-containing species and Si-containing species are depositing separately. The other model is a consecutive reaction model, in which W-species and Si-species react in the gas phase to form intermediate species containing W and Si. Considering these plausible kinetic mechanisms, consecutive reactions in the gas phase to form W and Si containing species were found to be the controlling factor in the WF6/Si2H6 process. These gas-phase homogeneous reaction-rate constants of the WF6/Si2H6 process were obtained from axial distribution of film composition ratio based on this kinetic model, and the activation energy is about 25 kJ/mol. (c) 2007 Elsevier Ltd. All rights reserved.
机译:在热壁式管式反应器中对WF6 / Si2H6的硅化钨(WSix)化学气相沉积进行了动力学研究,重点是台阶覆盖率和组成比的轴向分布。管状反应器内的生长速率曲线显示出指数衰减,这表明一级反应动力学。膜的硅含量在反应器的下游增加,但是台阶的覆盖质量与轴向位置无关。从阶梯覆盖分布图获得的反应性粘附概率约为0.33。研究了两种反应模型以解释这些实验结果。第一个模型是平行沉积模型,其中含W的物种和含Si的物种分别沉积。另一个模型是连续反应模型,其中W物种和Si物种在气相中反应形成包含W和Si的中间物种。考虑到这些可能的动力学机理,发现在气相中连续反应形成含W和Si的物种是WF6 / Si2H6工艺的控制因素。基于该动力学模型,通过膜组成比的轴向分布,获得了WF6 / Si2H6工艺的这些气相均相反应速率常数,其活化能约为25kJ / mol。 (c)2007 Elsevier Ltd.保留所有权利。

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