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

The calculation of tank capacity at stations in the \"Design Code for Oil Pipeline Engineering\" is on the low side

2009-03-19View Original

Thread Content

In the calculations for tank capacity in station areas as specified in the \"Design Code for Oil Pipeline Engineering,\" only the filling coefficient for certain oil tanks is set at 0.9 or 0.85. However, in practice, a considerable amount of oil at the bottom of the tanks cannot be removed; in some cases, it’s not even possible to extract the oil that is 3 or 4 meters deep. As a result, the utilization factor of these storage tanks becomes quite low. The tank capacity calculated according to the standards is too small; please share your opinions – are there any better ways to improve the utilization rate of the tanks?
Reply #22009-03-20
As for the oil in pipeline transport storage tanks, how do people usually operate them?

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.