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

Hydrocracking operation

2019-11-23View Original

Thread Content

During the hydrocracking production process, if the C4 content in light naphtha is high, how should the reaction section and the distillation section be operated?
Reply #22019-11-28
The reaction section is hardly needed; simply increasing the top temperature of the butane removal tower is sufficient
Reply #32019-12-04
The top and bottom temperatures of the butane removal unit include the feed temperature; efforts should be made to remove butane-4 from the butane removal section, and there should be no major issues if a reaction takes place

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.