Abstract
AbstractEnergy requirements for individual operations in the continuous caustic soda refining process are discussed. The electrical power requirements for the process are determined basically by the throughput rate which fixes centrifuge motor sizes. The electrical power requirements are not subject to significant reduction without a basic change in the process. However, the steam usage may be reduced by as much as 75% by proper heat‐recovery methods. The selection of process streams for most effective heat recovery is discussed.
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.