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.
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.