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

Steam condensate pressure

2020-12-15View Original

Thread Content

I would like to ask everyone: for low-pressure steam at 0.4 MPaG, does the condensate flow through the check valve not depend entirely on the back pressure? So there’s not much pressure, or can the maximum pressure reach 0.4 MPaG? I’m not sure if I understand correctly
Reply #22020-12-15
In the absence of other relay pumps, it depends on the back pressure in the pipeline, which is generally low, but it also depends on the specific circumstances!
Reply #32020-12-18
We have a condensate recovery pump behind us; the flash tank of this recovery pump operates at slightly positive pressure, so the pressure drop after the steam trap is very low. The pressure behind the steam trap must be lower than that of the steam; otherwise, the steam trap will not function!

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.