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

For a fixed-tube-sheet heat exchanger, the operating pressure in the tube side is -0.015; what value should be used for the design pressure?

2016-11-25View Original

Thread Content

For fixed-tube-sheet heat exchangers, the operating pressure on the tube side is -0.015; how should the design pressure be determined?
Reply #22016-11-26
A negative pressure condition has not been designed for, but I think it’s necessary to set the value in the negative pressure direction. Is 1.25 times appropriate? Also, if the strength design is proper, this negative pressure should be very small!
Reply #32016-11-26
The design pressure can be set at -0.02 MPa
Reply #42016-11-26
Tube side operating pressure: -0.015; material: TA2. Shell side operating pressure: 0.3; material: S31603

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.