Hydrogenation reactor inlet diffuser

2017-06-22 View Original

Thread Content

I would like to ask fellow sailors: what is an appropriate distance between the bottom of the diffuser at the inlet of the hydrogenation reactor and the top surface of the catalyst? Are there any standard requirements for this?

Reply #2 2017-06-22

Is there a distribution tray at the top of the catalyst bed? No, it’s not necessary; leave 1D of space

Reply #3 2017-06-22

Hello, is 1D an empirical value or is there some standard requirement?

Reply #4 2017-06-23

There must be design requirements for this; generally, the process package is designed accordingly.

Reply #5 2017-06-23

There must be design requirements for this; generally, the process package is designed accordingly.

Reply #6 2017-06-23

1-2m; choose the smaller value for smaller diameters and the larger value for larger diameters. Extra large is specified separately.

Reply #7 2017-06-23

Hello, is it based on experience for 1–2 meters, or are there any standard requirements?

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.

Hydrogenation reactor inlet diffuser

Thread Content

Submit a Project

Disclaimer

Quick Links