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

The issue of vapor pressure

2009-03-10View Original

Thread Content

I’m confused: the steam supply pressure is 3 kilograms. After reducing it with a ball valve at the inlet, the pressure drops to 1.2 kilograms. Should the steam temperature be calculated based on 3 kilograms or 1.2 kilograms?
Reply #22009-03-11
The ideal model is adiabatic throttling for pressure reduction, which can be considered an isenthalpic process. The steam temperature at this point can be calculated based on the pressure and temperature before the pressure reduction, as well as the pressure after it
Reply #32009-03-11
The method on the 3rd floor is the correct one; the temperature drops after throttling. Before throttling: P=0.3 MPaG, T=143.73 °C, H=2738.2 KJ/KG – saturated. After throttling: P=0.12 MPaG, T=136.1 °C, H=2738.2 KJ/KG – superheated

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.