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

How to choose between PN16 and PN25 stop valves for steam pipelines with a working pressure of 1.25MPa

2020-03-27View Original

Thread Content

Logically speaking, PN16 is sufficient, but the company uses PN25 in other designs. Is this safer? But haven’t the costs also increased? How to choose a valve?
Reply #22020-03-27
The pressures designed by design institutes are all high. In fact, most of the pressures are 16 kilograms.
Reply #32020-03-27
There needs to be a margin in the design, and the working temperature of steam is high, generally above 200 degrees. Under this temperature condition, the PN16 valve exceeds the applicable range, so PN25 is used.
Reply #42020-03-28
Valve selection is based on actual working conditions such as medium, pressure, temperature, etc., and is not determined by a single parameter. The rated pressure-temperature of the valve can refer to GB/T12224;
Reply #52020-03-28
The 1.25 you mentioned is normal working pressure. If abnormal conditions occur, PN16 will not meet the requirements.
Reply #62020-03-30
Italy's BONOMI GROUP was founded in 1901 and is a famous Italian valve manufacturing company with a century-old history. Main products include: Brass ball valves, pressure reducing valves, compression joints and fittings, stainless steel ball valves, carbon steel ball valves, V-shaped regulating ball valves, butterfly valves, pneumatic actuators, electric actuators and other products. After more than 100 years of steady and sustainable development, Bonomi Group has established three companies: Rubinetterie Bresciane, Valpres and Valbia, and has established seven sales subsidiaries in Germany, the United Kingdom, Russia, North America, India, Brazil and China. All products of the Bonomi Group are 100% made in Italy and are committed to high quality assurance.
Reply #72020-05-20
The working pressure is 1.25MPa, the design pressure may be 1.5MPa, and the pipeline strength test pressure is 1.5 times the design pressure! Therefore, either isolate the valve during the strength test, or simply choose a 2.5MPa valve. Personal understanding, please correct me.

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.