Abstract: A susceptor arrangement for a reactor includes a heater element configured to heat a process gas to be used in the reactor. Also included is an inner susceptor portion located radially inwardly of the heater element and configured to route the process gas therein along a radially inner process gas path. Further included is an outer susceptor portion located radially outwardly of the heater element and configured to route the process gas therein along a radially outer process gas path, wherein the radially inner process gas path and the radially outer process gas path are fluidly coupled and substantially fluidly isolated from the heater element.

Abstract: A susceptor arrangement for a reactor includes a heater element configured to heat a process gas to be used in the reactor. Also included is an inner susceptor portion located radially inwardly of the heater element and configured to route the process gas therein along a radially inner process gas path. Further included is an outer susceptor portion located radially outwardly of the heater element and configured to route the process gas therein along a radially outer process gas path, wherein the radially inner process gas path and the radially outer process gas path are fluidly coupled and substantially fluidly isolated from the heater element.

Abstract: A susceptor arrangement for a reactor includes a heater element configured to heat a process gas to be used in the reactor. Also included is an inner susceptor portion located radially inwardly of the heater element and configured to route the process gas therein along a radially inner process gas path. Further included is an outer susceptor portion located radially outwardly of the heater element and configured to route the process gas therein along a radially outer process gas path, wherein the radially inner process gas path and the radially outer process gas path are fluidly coupled and substantially fluidly isolated from the heater element.

Abstract: A process for preparing polycrystalline silicon comprising the steps of (A) reacting trichlorosilane with hydrogen thereby forming silicon and an effluent mixture comprising tetrachlorosilane and disilane described by formula HnCl6—nSi2 where n is a value of 0 to 6 and (B) co-feeding the effluent mixture and hydrogen to a reactor at a temperature within a range of about 600° C. to 1200° C. thereby effecting hydrogenation of the tetrachlorosilane and conversion of the disilane to monosilanes.

Abstract: A process for preparing polycrystalline silicon comprising the steps of (A) reacting trichlorosilane with hydrogen thereby forming silicon and an effluent mixture comprising tetrachlorosilane and disilane described by formula HnCl6—NSi2 where n is a value of 0 to 6 and (B) co-feeding the effluent mixture and hydrogen to a reactor at a temperature within a range of about 600° C. to 1200° C. thereby effecting hydrogenation of the tetrachlorosilane and conversion of the disilane to monosilanes.