How is the water supply to the overhead cold water tank in the delayed coking fractionation tower controlled?

2009-03-03View Original

Thread Content

How is the water supply to the overhead cold water tank in the delayed coking fractionation tower controlled? For a single coke drum in delayed coking, its operation is intermittent, which results in periodic changes in the heat source for the distillation column; as a consequence, the cooling load on the overhead of the distillation column is also uneven. As a result, it is difficult to control the water supply to the wet air-cooling tank at the top of the distillation tower: when the amount of oil and gas flowing to the distillation tower is high, the water in the tank tends to evaporate; when the amount is low, the water overflows, and it easily freezes in winter. I would like to ask everyone: How is the water supply to the wet air cooling tank at the top of the distillation tower controlled?

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.

How is the water supply to the overhead cold water tank in the delayed coking fractionation tower controlled?

Thread Content

Related Threads in This Forum

← Previous

Next →

Submit a Project

Disclaimer

Quick Links