For the cooling of flue gas, when using htri for calculations, is it necessary to enter a fouling coefficient?

2011-01-21View Original

Thread Content

Thank you,,, how should I fill in the components of the smoke? .

Reply #22011-01-21

We are also working on a smoke recovery system, but we haven’t used this software for calculations.

Reply #32011-01-22

Treat smoke as a substance; simply fill in its physical properties.

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.

For the cooling of flue gas, when using htri for calculations, is it necessary to enter a fouling coefficient?

Thread Content

Related Threads in This Forum

← Previous

Next →

Submit a Project

Disclaimer

Quick Links