Multiscale computational fluid dynamics modeling of thermal atomic layer deposition with application to chamber design

被引:41
作者
Zhang, Yichi [1 ]
Ding, Yangyao [1 ]
Christofides, Panagiotis D. [1 ,2 ]
机构
[1] Univ Calif Los Angeles, Dept Chem & Biomol Engn, Los Angeles, CA 90095 USA
[2] Univ Calif Los Angeles, Dept Elect & Comp Engn, Los Angeles, CA 90095 USA
基金
美国国家科学基金会;
关键词
Atomic layer deposition; Microscopic modeling; Computational fluid dynamics modeling; Kinetic Monte Carlo modeling; Geometry optimization; ALD cycle time optimization; KINETIC MONTE-CARLO; THIN-FILM GROWTH; PREDICTIVE CONTROL; SURFACE-ROUGHNESS; LATTICE-SIZE; SILICON; OPTIMIZATION; DEPENDENCE; ALD; AMINOSILANE;
D O I
10.1016/j.cherd.2019.05.049
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This work develops a first-principles-based three-dimensional, multiscale computational fluid dynamics (CFD) model, together with reactor geometry optimizations, of SiO2 thinfilm thermal atomic layer deposition (ALD) using bis(tertiary-butylamino)silane (BTBAS) and ozone as precursors. Specifically, an accurate macroscopic CFD model of the ALD reactor chamber gas-phase development is integrated with a detailed microscopic kinetic Monte Carlo (kMC) model that was developed in Ding et al. (2019), accounting for the microscopic lattice structure, atomic interactions and detailed surface chemical reactions. The multi scale information exchange and the transient simulation of the microscopic distributed kMC algorithms and the macroscopic CFD model are achieved through a parallel processing message passing interface (MPI) structure. Additionally, density functional theory (DFT)-based calculations are adopted to compute the key thermodynamic and kinetic parameters for the microscopic thin-film growth process. Recognizing the transient non-uniformity and the possibility to reduce the current ALD cycle time, the optimal configuration of reactor geometry is designed and evaluated including a showerhead panel adjustment and geometry modifications on reactor inlet and upstream. It is demonstrated that with suitable reactor chamber design the required BTBAS ALD half-cycle time can be reduced by 39.6%. (C) 2019 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:529 / 544
页数:16
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