Iron catalyzed hydrochlorination of silicon tetrachloride to trichlorosilane
In the hydrochlorination reaction, silicon tetrachloride (STC), metallurgical silicon, and hydrogen are converted to trichlorosilane (TCS) at about 540° C. Previously, a pilot-scale reactor was used to study the yield of TCS produced by the hydrochlorination reaction. The yield observed by experimentation compared favorably with a scalable mathematical model developed to predict the rate of TCS conversion. The model predicted that 90% of the final amount of TCS produced was achieved after the reactant gas traveled a quarter of the vertical distance in the reaction section of the reactor. The pilot-scale reactor was shortened to verify the model predictions. In addition, some catalytic effects on the reaction were studied.
1. A reactor for producing trichlorosilane (TCS) from the hydrochlorination of silicon tetrachloride (STC) with hydrogen in the presence of metallurgical silicon (Me-Si) comprising:
a reactor vessel comprising:
a distributor plate at the bottom of the inside reactor vessel;
internals inside the vertical length of the reactor vessel with the internals having a high surface area of iron; and
a matrix on the distributor plate with a high surface area of iron to catalyze reactions on the surface of the matrix.
2. The reactor according to claim 1 , wherein the internals include vertically mounted and horizontally supported unfinished surface carbon steel chains.
3. The reactor according to claim 2 , wherein the internals include iron in the form of an iron rich steel or steel alloy selected from the group consisting of: carbon steel, 304 stainless steel and 316 stainless steel.
4. The reactor according to claim 3 , wherein the iron content in steel is greater than about 61 wt %.
5. The reactor according to claim 1 , wherein the matrix is a matrix of carbon steel and stainless steel placed on the distributor plate that allows Me-Si to contact the matrix.
6. The reactor according to claim 1 , wherein the matrix includes iron in the form of an iron rich steel or steel alloy selected from the group consisting of: carbon steel, 304 stainless steel and 316 stainless steel.
7. The reactor according to claim 6 , wherein the iron content in steel is greater than about 61 wt %.
8. The reactor according to claim 1 , wherein the matrix on the distributor plate is iron diffusers with a surface area to volume ratio of about 500 m −1 to about 10,000 m −1 .
9. The reactor according to claim 1 , wherein when silicon is added to the reactor vessel, the iron area in the fluidized bed reactor to silicon weight ratio is between about 0.02-0.15 m 2 /kg.
10. The reactor according to claim 1 , wherein the reactor height is approximately 0.9 to 2.9 meters.
11. A reactor for producing trichlorosilane (TCS) from the hydrochlorination of silicon tetrachloride (STC) with hydrogen in the presence of metallurgical silicon (Me-Si) comprising:
a reactor vessel comprising:
walls formed of steel having at least 61 wt % iron;
a distributor plate at the bottom of the inside reactor vessel;
internals being vertically mounted and horizontally supported unfinished surface carbon steel chains with the internals formed of steel having at least 61 wt % iron; and
a matrix on the distributor plate with iron diffusers with a surface area to volume ratio of 540 to 8583 m −1 and an iron content of at least 61 wt % to catalyze reactions on the surface of the matrix.
12. The reactor according to claim 11 , wherein the reactor height is approximately 0.9 to 2.9 meters.
13. The reactor according to claim 11 , wherein when silicon is added to the reactor vessel, the iron area in the fluidized bed reactor to silicon weight ratio is between about 0.02-0.15 m 2 /kg.
14. A method for producing trichlorosilane (TCS) from the hydrochlorination of silicon tetrachloride (STC) with hydrogen in the presence of metallurgical silicon (Me-Si) comprising:
providing a fluidized bed reactor reaction vessel having internals with a high surface area of iron and having a matrix on a distributor plate with a high surface area of iron to catalyze reactions on the surface of those reactor parts;
introducing metallurgical silicon into the fluidized bed reactor such that the iron area in the fluidized bed reactor to silicon weight ratio is between about 0.02-0.15 m 2 /kg;
introducing hydrogen gas and silicon tetrachloride into the fluidized bed reactor; and
discharging trichlorosilane, the product of a hydrochlorination reaction of silicon tetrachloride, hydrogen, and metallurgical silicon, from the fluidized bed reactor.
15. The method according to claim 14 , wherein when silicon is added to the reactor vessel, the iron area to silicon weight ratio is between about 0.10-0.15 m 2 /kg.