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

A stream of steam is led from the main steam pipe on the public conduit rack to a location over 200 meters away

2017-06-19View Original

Thread Content

Is it reasonable to divert steam from the main steam pipe on the public utility corridor to the tube side of the heat exchanger, which is located over 200 meters away? The steam shut-off valve is a globe valve and is placed on the corridor at a height of over 9 meters, at the point where the main pipe emerges
Reply #22017-06-19
Are there any other valves besides the main valve? Such as automatically controlled valves.
Reply #32017-06-19
Main valve — 240m long pipeline — globe valve (next to the heat exchanger) — solenoid valve (next to the heat exchanger) — heat exchanger inlet
Reply #42017-06-19
A U-bend is added in front of the heat exchanger to connect to the drain valve for drainage
Reply #52017-06-19
The size of the U-bend required for thermal compensation should be calculated based on the specifications of the pipeline, right?
Reply #62017-06-19
The stop valve at nine meters that you’re referring to is on the main steam pipe branch in the common main corridor, right? This should still be reasonable! A further valve needs to be added before it enters your heat exchanger!
Reply #72017-06-19
If frequent switching is required, a valve operation platform can be installed 9m below. Steam-using equipment is often kept in operation; valves are installed near such equipment, with a steam trap placed before the inlet valve.
Reply #82017-06-19
I feel a gate valve should be added at the root where it emerges.
Reply #92017-06-20
A valve should be added to the outlet at the root.
Reply #102017-06-20
It is necessary for the supervisor to introduce the key points; it’s not a matter of whether it’s reasonable or not
Reply #112017-06-20
The steam branch pipe extends from the top of the main pipe, and the isolation valve is placed on the horizontal pipe, as close to the main pipe as possible. I’ve never heard of stop valves being used as cut-off valves; they’re all gate valves. Depending on the pressure, consider whether to use a heated pipeline; otherwise, you’ll just have to deal with the on-site workers cursing you behind your back. This gate valve does not require a platform, and it is generally used very rarely. In other words, there’s no need to consider whether it can be operated during the design phase.

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.