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

Regarding the error in the external pressure calculation for copper pipes in SW6

2026-03-11View Original

Thread Content

Gentlemen! In sw6, a stuffing box type heat exchanger is selected for the structure, and T2 tubes are used as the heat exchange tubes; the following error occurs during the strength calculation. 1. The axial stress δt of the heat exchange tube is not up to standard ; 2. External pressure strain coefficient B curve temperature out of range ; The actual design temperature of 100°C is not high, but this situation occurs – how should it be handled? Has anyone else encountered this problem? Help! ! !
Reply #22026-04-07
Send the design files next time we meet. 1. The allowable stress for T2 is really low – it’s only 25 MPa at 100°C. The calculations show that it does not meet the requirements; the structure needs to be modified. Perhaps increasing the number of heat exchange tubes could help? 2. According to JB/T4755-2006, the temperature on the T2 external pressure curve shall be ≤65℃. It is recommended to change the material

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.