Abstract
The drawbacks of the production of sodium disilicate in glass-melting tank furnaces are described, and the expedience of melting soluble glass in an annular cyclone chamber using industrial sulfate waste is demonstrated. A method for the calculation of the flow-through part of the cyclone chamber for a preset output is proposed. The results of the calculations of a cyclone chamber and a whole aggregate with an output of 40 tons/day are provided, including the environmental, technical, and economical parameters of the production of sodium disilicate and liquid glass based it.
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