Method and apparatus to reduce contamination of particles in a fluidized bed reactor
A method and fluidized bed reactor for reducing or eliminating contamination of silicon-coated particles are disclosed. The metal surface of one or more fluidized bed reactor components is at least partially coated with a hard protective layer comprising a material having an ultimate tensile strength of at least 700 MPa at 650° C.
1. A method of reducing or eliminating contamination of silicon-coated particles due to contact with a surface in a fluidized bed reactor, the method comprising:
providing, in a fluidized bed reactor, a fluidized bed reactor component having a surface facing silicon-coated particles during operation of the fluidized bed reactor, the surface comprising metal that is at least partially coated with a protective layer comprising a material having an ultimate tensile strength of at least 700 MPa at 650° C., wherein the protective layer is
a cobalt-based alloy comprising 25-35% Cr, ≦10% W, ≦10% Ni, ≦5% Mo, ≦3% Fe, ≦2% Si, ≦2% C, ≦1.5% Mn, ≦1% B, ≦0.05% P, ≦0.05% S, and 30.5-75% cobalt, or
a nickel-based alloy comprising 4-30% Mo, 5-25% Cr, 2-15% Co, ≦3.5% Ti, ≦2% Fe, ≦2% Al, ≦1% Mn, ≦1% Si, ≦0.5% Cu, ≦0.1% C, ≦0.1% Zr, ≦0.01% B, and 23.4-89% nickel; and
operating the fluidized bed reactor to make silicon-coated particles.
2. The method of claim 1 , wherein at least 95% of the surface is coated with the protective layer.
3. The method of claim 1 , wherein the metal has a thermal coefficient of expansion, TCE-1, and the protective layer has a thermal coefficient of expansion, TCE-2, wherein TCE-2 and TCE-1 differ by ≦30%.
4. The method of claim 3 , wherein an intermediate coating having a thermal coefficient of expansion, TCE-3, between TCE-1 and TCE-2 is disposed between the metal and the protective layer.
5. The method of claim 1 , wherein the protective layer has a minimum average thickness of 0.1 mm.
6. The method of claim 5 , wherein the protective layer has a thickness that varies across a width and/or along a length of the surface.
7. The method of claim 1 , wherein a portion of the fluidized bed reactor component is constructed entirely of a material having substantially the same chemical composition as the protective layer.
8. The method of claim 7 , wherein the fluidized bed reactor component is a fluidization gas inlet tube, an injection nozzle, a thermocouple, a pressure nozzle, or a sample nozzle.
9. The method of claim 1 , wherein the fluidized bed reactor component is an injection nozzle, a fluidization gas inlet tube, a seed inlet tube, a product withdrawal outlet tube, a probe assembly, a sample nozzle, a pressure nozzle, a thermocouple, an internal heater, or a bubble breaker.
10. A fluidized bed reactor unit for production of polycrystalline silicon, the unit comprising:
a reactor defining a reactor chamber; and
one or more reactor components having a surface facing the reactor chamber, the surface comprising metal that is at least partially coated with a protective layer having an ultimate tensile strength of at least 700 MPa at 650° C., wherein the protective layer is
a cobalt-based alloy comprising 25-35% Cr, ≦10% W, ≦10% Ni, ≦5% Mo, ≦3% Fe, ≦2% Si, ≦2% C, ≦1.5% Mn, ≦1% B, ≦0.05% P, ≦0.05% S, and 30.5-75% cobalt, or
a nickel-based alloy comprising 4-30% Mo, 5-25% Cr, 2-15% Co, ≦3.5% Ti, ≦2% Fe, ≦2% Al, ≦1% Mn, ≦1% Si, ≦0.5% Cu, ≦0.1% C, ≦0.1% Zr, ≦0.01% B, and 23.4-89% nickel.
11. The fluidized bed reactor unit of claim 10 , wherein the metal has a first thermal coefficient of expansion (TCE-1) and the protective layer has a second thermal coefficient of expansion (TCE-2) that differs from TCE-1 by ≦30%.
12. The fluidized bed reactor unit of claim 10 , wherein the reactor component further comprises an intermediate coating having a thermal coefficient of expansion, TCE-3, between TCE-1 and TCE-2, wherein the intermediate layer is positioned between the metal and the protective layer.
13. The fluidized bed reactor unit of claim 10 , wherein the protective layer has an average thickness from 0.1 mm to 1 mm.
14. The fluidized bed reactor unit of claim 13 , wherein the protective layer has a thickness that varies across a width and/or along a length of the surface.
15. The fluidized bed reactor unit of claim 10 , wherein the protective layer comprises a cobalt-based alloy, a nickel-based alloy, or a combination thereof.
16. The fluidized bed reactor unit of claim 10 , wherein a portion of reactor component is constructed entirely of a material having substantially the same chemical composition as the protective layer.
17. A process for the production of granulate polycrystalline silicon particles, the process comprising flowing a silicon-containing gas through a fluidized bed reactor containing a seed particle within a reactor chamber defined by the fluidized bed reactor to effect pyrolysis of the silicon-containing gas and deposition of a polycrystalline silicon layer on the seed particle to form a polycrystalline silicon-coated particle, wherein the fluidized bed reactor comprises one or more reactor components having a surface facing the reactor chamber during reactor operation, the surface comprising metal that is at least partially coated with a protective layer having an ultimate tensile strength of at least 700 MPa at 650° C., wherein the protective layer is
a cobalt-based alloy comprising 25-35% Cr, ≦10% W, ≦10% Ni, ≦5% Mo, ≦3% Fe, ≦2% Si, ≦2% C, ≦1.5% Mn, ≦1% B, ≦0.05% P, ≦0.05% S, and 30.5-75% cobalt, or
a nickel-based alloy comprising 4-30% Mo, 5-25% Cr, 2-15% Co, ≦3.5% Ti, ≦2% Fe, ≦2% Al, ≦1% Mn, ≦1% Si, ≦0.5% Cu, ≦0.1% C, ≦0.1% Zr, ≦0.01% B, and 23.4-89% nickel.
18. The process of claim 17 , wherein at least 95% of the surface is coated with the protective layer, thereby reducing or eliminating contact of the polycrystalline silicon-coated particle with the metal and reducing or eliminating metal contamination of the polycrystalline silicon particle.