2008
DOI: 10.1016/j.cej.2008.02.027
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Development of an original model for the synthesis of silicon nanodots by Low Pressure Chemical Vapor Deposition

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Cited by 6 publications
(13 citation statements)
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“…However, this choice does not limit the interest of the model because silylene is the main unsaturated species created in the gas phase. Moreover, it is also well known that the contribution to deposition of polysilanes of an order higher than 2 is negligible in LPCVD conditions [15,24].…”
Section: Homogeneous Reactionsmentioning
confidence: 99%
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“…However, this choice does not limit the interest of the model because silylene is the main unsaturated species created in the gas phase. Moreover, it is also well known that the contribution to deposition of polysilanes of an order higher than 2 is negligible in LPCVD conditions [15,24].…”
Section: Homogeneous Reactionsmentioning
confidence: 99%
“…Numerous authors have developed numerical models of CVD reactors calculating silicon deposition rates from silane and the homogeneously born species for given operating conditions [15,[21][22][23]. However, to date, none of these researchers has studied the first stages of deposition with the exception of a previous study by our group [24]. By comparing experimental and calculated NC deposition rates using the Computational Fluid Dynamics (CFD) code Fluent, it has been observed that the classical kinetic laws of the literature largely over-estimate deposition rates for these ultrathin layers.…”
Section: Introductionmentioning
confidence: 99%
“…Si NDs are synthesized in a Tokyo Electronic Limited (TEL) industrial vertical tubular hot wall LPCVD reactor which contains 170 silicon wafers 8' in diameter as detailed elsewhere 3 . We use the CFD Fluent software (Fluent 6.1.18) to solve the governing equations of mass, momentum, and reactive species transport and predict gas flow and species concentration versus position in the reactor.…”
Section: Fluent Simulation Of the Industrial Processmentioning
confidence: 99%
“…But we wish here to analyse from one simulation to another the influences of the carrier gas and dilution ratio on the deposition rates obtained along the load. Clearly, the objective here is to sharply decrease the total deposition rate in maintaining a uniform value along the load, so as to increase the deposition duration to values greater than 60 s. With such run durations, the unsteady regime corresponding to the filling-in of the reactor and to establishment of reactive mass transfers will become negligible in comparison with the steady state regime 3 . Silane dilution ratios comprised between 75 and 95 vol.…”
Section: Fluent Simulation Of the Industrial Processmentioning
confidence: 99%
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