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

Selection of the hook ring type for floating-head heat exchangers

2017-03-18View Original

Thread Content

According to the heat exchanger standard GB151, floating-head heat exchangers come in two types of hook rings: Type A and Type B. Upon comparison, Type B has many advantages, while Type A has only the advantage of lower processing requirements. Questions: 1. How should one choose between the two types of hook rings? What are the selection principles? 2. If everyone chooses Type B due to its many advantages, then why is Type A still included in the standards? Moreover, why is the Type A structure still retained in the new version of GB/T151-2014? Could any expert provide a convincing explanation? Thank you. The attached figure shows a comparison of the two types of hook loops as defined in the GB/T151-2014 standard
Reply #22017-03-19
Type B saves material and is easy to assemble; we use it all the time
Reply #32017-03-19
Hehe, for small diameters, type A is still used more often
Reply #42017-03-19
Why is small diameter used so often? What’s the reason? What general diameter is suitable for type A?

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.