Abstract Process and apparatus are provided for preparing finely-divided silicon dioxide in good yield by reaction of silicon fluoride in the vapor phase with water vapor, combustible gas and free oxygen-containing gas in a flame reaction zone to form hydrogen fluoride and silicon dioxide entrained in a gaseous reaction mixture; withdrawing the gaseous reaction mixture from the flame reaction zone; and then immediately and rapidly cooling the gaseous reaction mixture and entrained silicon dioxide to a temperature below 700° C. by passing the gaseous reaction mixture in a turbulent flow at a Reynolds number above 300 under constraint through a straight narrow passage in alignment with the gas flow, the passage having a diameter within the range from about 20 to about 150 mm and smooth walls constituting a cooling surface.
A process for preparing finely-divided silicon dioxide in good yield which comprises reacting a silicon fluoride in the vapor phase with water vapor, combustible gas and free oxygen-containing gas in a flame reaction zone to form hydrogen fluoride and silicon dioxide entrained in a gaseous reaction mixture; withdrawing the gaseous reaction mixture from the flame reaction zone; and then immediately and rapidly cooling the gaseous reaction mixture and entrained silicon dioxide to a temperature below 700° C. by passing the gaseous reaction mixture in turbulent flow at a Reynolds number above 300 under constraint through a plurality of passages all of which consist of straight passages in alignment with the gas flow, the passages having a diameter within the range from about 20 to about 150 mm and smooth walls constituting cooling surfaces.
Claim 2
Dependent Claim
133 words
A process for preparing finely-divided silicon dioxide in good yield which comprises reacting a silicon fluoride in the vapor phase with water vapor, combustible gas and free oxygen-containing gas in a flame reaction zone to form hydrogen fluoride and silicon dioxide entrained in a gaseous reaction mixture; withdrawing the gaseous reaction mixture from the flame reaction zone; and then immediately and rapidly cooling the gaseous reaction mixture and entrained silicon dioxide to a temperature below 700° C. by passing the gaseous reaction mixture in turbulent flow at a Reynolds number above 300 under constraint through a plurality of passages all of which consist of straight passages in alignment with the gas flow, the passages having a diameter within the range from about 20 to about 150 mm and smooth walls constituting cooling surfaces.
Claim 3
Dependent Claim
14 words
A process according to claim 1 in which the silicon fluoride is silicon tetrafluoride.
Claim 4
Dependent Claim
12 words
A process according to claim 1 in which the passages are tubular.
Claim 5
Dependent Claim
15 words
A process according to claim 1 in which the passages are defined by parallel plates.
Claim 6
Dependent Claim
25 words
A process according to claim 1 in which the gaseous reaction mixture passes through the passages in a transit time of less than ten seconds.
Claim 7
Dependent Claim
25 words
A process according to claim 1 in which the gaseous reaction mixture passes through the passages in a transit time of less than one second.
Claim 8
Dependent Claim
17 words
A process according to claim 1 in which the cooling surface is cooled by circulating boiling water.