HCBBS Forum (English)
Submit Chemical Projects / Find Solutions
Amplify Your Requirements on a Broader Chemical Platform *Engineering · Technology · Equipment · Solutions*
Submit Request

Design pressure of negative pressure tower

2021-04-21View Original

Thread Content

There is now a pressure relief tower, with an operating pressure of 20 KPa (A). Considering the possibility of failures in the vacuum system, the steam at the bottom of the tower cannot be shut off quickly; therefore, a safety valve is necessary. So, what should be the setting for the opening pressure of this safety valve? Also, if a safety valve is not installed, what maximum design pressure can be set for the tower?

Submit a Project

**Looking for Chemical Technology, Equipment & Solutions?** No Registration Required Broader Platform Exposure | Global Chemical Service Provider Connections

Submit Request — Free Consultation

Disclaimer

This is an automated machine translation of the original thread. Some technical terms may have inaccuracies; the original text shall prevail. Click "View Original" at the top right to access the source page, which supports IP-based automatic real-time language translation. Please watch out for contact details and sales inducements to prevent fraud. All content and translations are for reference only, representing solely the poster's personal views. For enquiries, email service@hcbbs.com.