Patent ID: 9120678
Filing Date: 2015-09-01
Classification: C01B,C01P,C03B,C03C,Y10T

Abstract:
1. A method for producing a synthetic amorphous silica powder, comprising, in the recited order: a granulating step for producing a siliceous gel, drying the siliceous gel to turn it into a dry powder, pulverizing particles of the dry powder, and then classifying the pulverizedly obtained particles to thereby obtain a silica powder; a spheroidizing step based on a thermal plasma for delivering, at a supplying rate of 3.5 to 17.5 kg/hr, particles of the silica powder obtained in the granulating step into an argon-oxygen plasma in a plasma torch from a starting material supplying tube in a manner to heat the particles at a temperature from 2,000° C. to a boiling point of silicon dioxide, thereby melting the particles, in which the argon-oxygen plasma is generated by introducing argon as a working gas from a gas introducing tube at a flow rate of 60 to 100 L/min into the plasma torch, while applying a high frequency wave at a frequency of 2 to 3 MHz and at a power of 120 to 1000 kw to the plasma torch, and by gradually introducing oxygen at a flow rate of 30 to 125 L/min into the plasma torch after the plasma is stabilized; a cleaning step for removing particles of silica powder attached to surfaces of the spheroidized silica powder particles after the spheroidizing step by repetitively conducting ultrasonic cleaning such that the spheroidized silica powder particles after the spheroidizing step and ultrapure water are put into a cleaning vessel, and filtration by using a filter until the particles of the silica powder are fully filtered out; and a drying step for drying the silica powder particles after the cleaning step such that the powder is firstly put into a container for drying, and then the container for drying is brought into a drier, in which drying is conducted by flowing nitrogen or argon at a flow rate of 1 to 20 L/min through within the drier, and by holding the powder at a temperature of 100° C. to 400° C. for 3 to 48 hours; wherein the spheroidizing step is conducted by adjusting a value of A/B (W·hr/kg) to 1.0×10 an average particle diameter D a quotient of 1.00 to 1.35 obtained by dividing a BET specific surface area of the powder by a theoretical specific surface area calculated from the average particle diameter D a real density of 2.10 to 2.20 g/cm3; an intra-particulate porosity of 0 to 0.05; a circularity of 0.75 to 1.00; and an unmolten ratio of 0.00 to 0.25.