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MODELING POLYMER VAPOR DEPOSITION: PMDA-ODA POLY(AMIC ACID)

机译:模拟聚合物气相沉积:PMDA-ODA聚合物(丙烯酸)

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Vapor deposited PMDA:ODA poly(amic acid) and polyimide capsules have been produced with desirable material properties (high tensile strength, permeability, and elastic modulus), but the contributions of the process steps and their dependence on external control variables has not been investigated. We have combined numerical simulations with experimental measurements to model the steps of the vapor deposition process including monomer sublimation, vapor transport to the bounce pan, and poly-condensation on the substrate surfaces. The measured sublimation rates of PMDA and ODA monomer at temperatures that yielded stoichiometric poly(amic acid) (10~(-6) Torr deposition) are 1.2 x 10~(-7) gm/s PMDA (at 153℃) and 6.3 x 10~(10) gm/s ODA (at 126?)—a 180:1 PMDA:ODA molar ratio. These provide initial boundary conditions to simulate the thermal environment and vapor transport inside the deposition chamber at 1 x 10~(-2) Torr. A disproportionate loss of PMDA gas during transport to a stationary mandrel is shown by the numerical model to reduce the monomer stoichiometry to 9:1 PMDA:ODA The transport-based loss depends strongly on the geometry of the substrate support, as is shown by modifying the substrate to change the flow pattern, which reduces this ratio to 1:1 PMDA:ODA above the mandrel. A separate model of the kinetics of monomer deposition and polymerization reactions was developed to correlate the gas concentrations above the substrate with the elemental concentrations comprising the film. This basic model was tested with rate constants based on reaction probabilities of one and equal deposition rates for two monomers in the absence of measured values and is sensitive to changes in vapor stoichiometry.
机译:汽相沉积的PMDA:ODA聚(酰胺酸)和聚酰亚胺胶囊具有理想的材料性能(高拉伸强度,渗透性和弹性模量),但是尚未研究工艺步骤的作用及其对外部控制变量的依赖性。我们将数值模拟与实验测量相结合,以对气相沉积过程的各个步骤进行建模,包括单体升华,蒸汽向回弹盘的传输以及基材表面的缩聚。在产生化学计量的聚酰胺酸(10〜(-6)托沉积)的温度下,测得的PMDA和ODA单体的升华速率分别为1.2 x 10〜(-7)gm / s PMDA(在153℃)和6.3 x 10〜(10)gm / s ODA(在126 ??下)— PMDA:ODA摩尔比为180:1。这些提供了初始边界条件,以模拟热环境和在1 x 10〜(-2)Torr下沉积室内部的蒸汽传输。数值模型显示了将单体化学计量比降低到9:1 PMDA:ODA时,PMDA气体在向固定心轴传输过程中的不成比例损失。基于传输的损失在很大程度上取决于基质载体的几何形状,如通过修改所示改变流型,使该比率降低到心轴上方1:1 PMDA:ODA。建立了单体沉积和聚合反应动力学的独立模型,以将基材上方的气体浓度与构成薄膜的元素浓度相关联。在没有测量值的情况下,使用基于一种常数的反应速率和两种单体的相等沉积速率的速率常数测试了该基本模型,并且该模型对蒸气化学计量的变化敏感。

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