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

Expansion joint calculation

2018-06-09View Original

Thread Content

In shell-and-tube heat exchangers, the shell side often features a structure in which a tube section is connected between two semi-wave expansion joints; this serves both to compensate for the temperature difference between the shell and tube sides and to act as a flow guide tube. As shown in the figure, when calculating the expansion joint for such a structure, should the length entered be “L” as shown in the diagram?"
Reply #22018-06-10
This post was last edited by wanlirn on 2018-6-10 09:38. In our case, it’s about removing the length L of the intermediate cylinder. Some experts believe that it cannot be calculated using expansion joints; this is especially true for large heat network heaters with saddles installed inside the intermediate cylinder (and there is some logic to that). It should be calculated according to Section 4 in 20582
Reply #32018-06-10
Generally, there is no saddle seat in this section

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.