欢迎登录材料期刊网

材料期刊网

高级检索

通过模拟法对丙烯化学气相渗透(cvI)制备炭/炭复合材料(C/c)的工艺过程进行研究.基于16种反应物,建立了由34个基元反应组成的均相反应模型.引用双孔隙演化模型、非均相反应模型,对整个丙烯CVI模型进行耦合模拟.模拟结果表明,CVI法C/C复合材料的密度均匀性受沉积气体滞留时间、致密温度和致密时间等因素影响;致密化过程可分为微孔隙快速致密和大孔隙致密两个阶段,丙烯初级热解产物的浓度分布与这两个阶段关系密切;其中大分子气体苯的浓度分布对CVI沉积速度和C/C复合材料密度均匀性的影响明显,当苯浓度分布最高区严重变窄时,表明致密化过程结束,致密表面将出现结壳现象.验证实验与模拟数据吻合较好.

参考文献

[1] Golecki I .Rapid vapor-phase densification of refractory composites[J].Materials Science and Engineering,1997,20:37-124.
[2] W. BENZINGER;K. J. HUETTINGER .CHEMICAL VAPOUR INFILTRATION OF PYROCARBON: Ⅰ. SOME KINETIC CONSIDERATIONS[J].Carbon: An International Journal Sponsored by the American Carbon Society,1996(12):1465-1471.
[3] Li AJ;Deutschmann O .Transient modeling of chemical vapor infiltration of methane using multi-step reaction and deposition models[J].Chemical Engineering Science,2007(18/20):4976-4982.
[4] Hejun Li;Aijun Li;Ruicheng Bai .Numerical simulation of chemical vapor infiltration of propylene into C/C composites with reduced multi-step kinetic models[J].Carbon: An International Journal Sponsored by the American Carbon Society,2005(14):2937-2950.
[5] 张伟刚.化学气相沉积一从烃类气体到固体碳(ZHANG Wei-gang.Chemical vapor deposition-From hydrocarbon gas to solid carbon[M].Beijing:Science Press,2007:1-40.)[M].北京:科学出版社,2007:1-40.
[6] Becker A.;Huttinger KJ. .Chemistry and kinetics of chemical vapor deposition of pyrocarbon - III - Pyrocarbon deposition from propylene and benzene in the low temperature regime[J].Carbon: An International Journal Sponsored by the American Carbon Society,1998(3):201-211.
[7] Hidaka Y;Nakamura T;Tanaka H et al.Shock tube and modeling study of propene pyrolysis[J].International Journal of Chemical Kinetics,1992,24:761-780.
[8] Tsang W .Chemical kinetic data base for combustion chemistry.Part Ⅴ.Propene[J].Journal of Physical and Chemical Reference Data,1991,20:221-273.
[9] Hidaka Y;Nakamura T;Miyauchi A et al.Thermal decomposition of propyne and allene in shock waves[J].lnt J Chem Kinet,1989,21:643-666.
[10] Lim K P;Michel J V .The thermal reactions of CH3[J].Symposium (International) on combustion: proceedings,1994,25:713-719.
[11] Warnatz J;Gardiner W C,Jr.Rate Coefficients in the C/H/O System,Chap.5[M].Combustion Chemistry.Berlin,Heidelberg:Springer,1984
[12] Takahashi J;Momose T;Shida T .Thermal rate constants for SiH4 =SiH3 + H and CH4 + CH3 + H by Canonical Variational Transition State Theory[J].Bulletin of the Chemical Society of Japan,1994,67:74-85.
[13] Narayana Birakayala;Edward A. Evans .A reduced reaction model for carbon CVD/CVI processes[J].Carbon: An International Journal Sponsored by the American Carbon Society,2002(5):675-683.
[14] Mallard W G;Owen J H .Rate Constant for H +H + Ar =H2+Ar from 1300 to 1700 K[J].International Journal of Chemical Kinetics,1974,6(05):753-761.
[15] NIST Chemistry Kinetics Database[OL].http://kinetics.nist.gov/index.php
[16] P. Delhaes .Chemical vapor deposition and infiltration processes of carbon materials[J].Carbon: An International Journal Sponsored by the American Carbon Society,2002(5):641-657.
[17] Brüggert M;Hu Z;Hüttinger K J .Chemistry and kinetics of chemical vapor deposition of pyrocarbon-Ⅵ.Influence of temperature using methane as a carbon source[J].CARBO,1999,37:2021-2030.
[18] 白瑞成,任慕苏,张家宝,李红,刘育太,孙晋良.ICVI工艺因素对C/C复合材料致密化的影响[C].第十五届全国复合材料学术会议论文集,2008:597-601.
上一张 下一张
上一张 下一张
计量
  • 下载量()
  • 访问量()
文章评分
  • 您的评分:
  • 1
    0%
  • 2
    0%
  • 3
    0%
  • 4
    0%
  • 5
    0%