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Numerical Study of Mixed Convection Flow in an Impinging Jet CVD Reactor for Atmospheric Pressure Deposition of Thin Films

机译:撞击式CVD化学反应器中混合空气对流的数值研究。

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摘要

A systematic numerical study has been conducted of the mixed convection flow in a novel impinging jet chemical vapor deposition (CVD) reactor for deposition of thin films at atmospheric pressure. The geometry resembles that of a pancake reactor but the inflow gases enter through a small nozzle to provide high inlet momentum. A finite-volume-based computational procedure is used to integrate the governing flow, energy, and scalar transport equations with high accuracy. The effects of the temperature dependent properties are fully accounted for. The effects of operating pressure, wafer rotation rate, and inlet flow rate of the carrier gas are investigated. The main benefit of the new geometry is the suppression of the buoyancy-driven flow even at atmospheric pressures due to the lower mixed convection parameter. We show that the new geometry can produce thin films of high radial uniformity and also with high growth rate. Comparisons are also made with a conventional stagnation flow reactor for which it is shown that beyond a moderate pressure (~ 0.1 atm), the flow is dominated by natural convection, and the reactor is unsuitable for practical use.
机译:对新型对流喷射化学气相沉积(CVD)反应器中混合对流进行了系统的数值研究,该反应器用于在大气压下沉积薄膜。几何形状类似于煎饼反应器的几何形状,但是流入的气体通过一个小喷嘴进入,以提供较高的入口动量。基于有限体积的计算过程用于高精度地整合控制流,能量和标量传输方程。充分考虑了温度相关特性的影响。研究了工作压力,晶片转速和载气入口流速的影响。新几何结构的主要好处是,即使在大气压下,由于较低的混合对流参数,也可以抑制浮力驱动的流量。我们表明,新的几何形状可以生产出高径向均匀性和高增长率的薄膜。还与常规的停滞式流动反应器进行了比较,结果表明,在中等压力(〜0.1 atm)以上,流动主要由自然对流主导,该反应器不适合实际使用。

著录项

  • 来源
    《Journal of Heat Transfer》 |2004年第5期|p.764-775|共12页
  • 作者单位

    Department of Mechanical and Industrial Engineering, University of Illinois at Urbana-Champaign, 1206 West Green Street, Urbana, IL 61801;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 热力工程、热机;
  • 关键词

  • 入库时间 2022-08-18 00:28:07

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