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

How is the air excess factor controlled after waste gas recycling?

2019-01-01View Original

Thread Content

This post was last edited by angryant on 2019-1-2 21:04. Coking is carried out in coke ovens, using coke oven gas as fuel; the air excess factor used to be 1.20~1.25. Now that waste gas recycling systems are installed in coke ovens, have there been any changes in the values of the air excess factor and its calculation formula? Note: (Waste gas recirculation refers to the process in which a portion of the waste gas from the flue ducts is drawn out by a fan and sent back to the regenerative chamber in the upward airflow of the coke oven, with the aim of reducing nitrogen oxides and improving upward heating.) )
Reply #22019-01-02
Production control is maintained at a level of 1.0 to 1.05; for detailed information, refer to an issue of \"China Coking Industry\" published in 2017
Reply #32019-01-02
Could you help find that book or send a screenshot? Thank you in advance.

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.