Abstract A reactor apparatus (10) adapted for continuously producing molten, solar grade purity elemental silicon by thermal reaction of a suitable precursor gas, such as silane (SiH 4 ), is disclosed. The reactor apparatus (10) includes an elongated reactor body (32) having graphite or carbon walls which are heated to a temperature exceeding the melting temperature of silicon. The precursor gas enters the reactor body (32) through an efficiently cooled inlet tube assembly (22) and a relatively thin carbon or graphite septum (44). The septum (44), being in contact on one side with the cooled inlet (22) and the heated interior of the reactor (32) on the other side, provides a sharp temperature gradient for the precursor gas entering the reactor (32) and renders the operation of the inlet tube assembly (22) substantially free of clogging. The precursor gas flows in the reactor (32) in a substantially smooth, substantially axial manner. Liquid silicon formed in the initial stages of the thermal reaction reacts with the graphite or carbon walls to provide a silicon carbide coating on the walls. The silicon carbide coated reactor is highly adapted for prolonged use for production of highly pure solar grade silicon. Liquid silicon (20) produced in the reactor apparatus (10) may be used directly in a Czochralski or other crystal shaping equipment.
A process for directly producing molten silicon by thermal decomposition of silane in a reaction chamber, said process comprising the steps of: (a) maintaining a feed gas comprising said silane and hydrogen in a first temperature range below the thermal decomposition temperature of said silane, (b) maintaining said reaction chamber in a second temperature range above the melting point of silicon; (c) abruptly raising the temperature of said feed gas from said first temperature range to said second temperature range by introducing said feed gas into said reaction chamber from a cooled inlet means having a terminal orifice located outside said reaction chamber through an insulating, porous carbon septum about 0.1 to 1.0 cm thick and having a matching orifice of a diameter in the range of 0.5-3 cm. said septum having one face against said cooled inlet means and having the opposite face exposed to said reaction chamber so that said silane in said feed gas remains undecomposed until entering said reaction chamber; (d) maintaining a substantially smooth, axial, downward flow of said feed gas in the reaction chamber while permitting said silane to undergo thermal decomposition to yield molten silicon; (e) removing unreacted feed gas and by-product gas from the reaction chamber; and (f) recovering molten silicon from the reaction chamber.
Claim 2
Dependent Claim
213 words
A process for directly producing molten silicon by thermal decomposition of silane in a reaction chamber, said process comprising the steps of: (a) maintaining a feed gas comprising said silane and hydrogen in a first temperature range below the thermal decomposition temperature of said silane, (b) maintaining said reaction chamber in a second temperature range above the melting point of silicon; (c) abruptly raising the temperature of said feed gas from said first temperature range to said second temperature range by introducing said feed gas into said reaction chamber from a cooled inlet means having a terminal orifice located outside said reaction chamber through an insulating, porous carbon septum about 0.1 to 1.0 cm thick and having a matching orifice of a diameter in the range of 0.5-3 cm. said septum having one face against said cooled inlet means and having the opposite face exposed to said reaction chamber so that said silane in said feed gas remains undecomposed until entering said reaction chamber; (d) maintaining a substantially smooth, axial, downward flow of said feed gas in the reaction chamber while permitting said silane to undergo thermal decomposition to yield molten silicon; (e) removing unreacted feed gas and by-product gas from the reaction chamber; and (f) recovering molten silicon from the reaction chamber.
Claim 3
Dependent Claim
17 words
The process of claim 1 wherein said carbon septum has an emissivity of at least about 0.90.
Claim 4
Dependent Claim
14 words
The process of claim 1 wherein the second temperature range is approximately 1500°-1800° C.
Claim 5
Dependent Claim
14 words
The process of claim 3 wherein the second temperature range is approximately 1600°-1800° C.
Claim 6
Dependent Claim
14 words
The process of claim 1 wherein the first temperature range is below 1000° C.
Claim 7
Dependent Claim
13 words
The process of claim 1 wherein said cooled inlet means is a tube.
Claim 8
Dependent Claim
17 words
The process of claim 1 wherein said septum is located in the top center of said reactor.
Claim 9
Dependent Claim
24 words
The process of claim 1 wherein said feed gas stream is introduced into said reaction chamber at about 1.0 to 50.0 feet per second.
Claim 10
Dependent Claim
22 words
The process of claim 8 wherein said feed gas stream is introduced into said reaction chamber at about 3.0 to 10.0 fps.