I would like to ask about using absbr1 from the radfrac module in Aspen simulations to model an absorption tower without a condenser or reboiler

2020-03-21View Original

Thread Content

The impact of tray pressure drop on the product: Taking the absorption of chloromethane by 98% concentrated sulfuric acid, as well as the water present in gas streams, as an example – how to absorb as much water as possible from the gas phase (by adjusting the pressure drop in the tower or trays)

Reply #22020-03-21

Flue gas feed: Chloromethane: 43.2 kmol/h Water: 27 kmol/h Air: 30 kmol/h

Reply #32020-03-21

Also, since energy conservation and emission reduction are a priority, distillation is not considered for now; it will only be used if there is no other choice

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.

I would like to ask about using absbr1 from the radfrac module in Aspen simulations to model an absorption tower without a condenser or reboiler

Thread Content

Related Threads in This Forum

← Previous

Next →

Submit a Project

Disclaimer

Quick Links