Compensation issues in pipeline design

2011-11-26View Original

Thread Content

In air separation, how is the compensation for temperature variations in pipes and equipment calculated, ranging from over -190 degrees to over 20 degrees? For example, where do we need to install our expansion joints? Where doesn’t it need to be installed? Why? For example, a backup low-temperature liquid storage tank in air separation is connected to a backup pump at its bottom; is it necessary to install expansion joints on the pipes coming out of the tank? How should it be designed?

Reply #22011-11-26

So, does anyone know the coefficient of expansion for 06Gr19Ni10 between -190 degrees and 20 degrees?

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.

Compensation issues in pipeline design

Thread Content

Related Threads in This Forum

← Previous

Next →

Submit a Project

Disclaimer

Quick Links