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13 MPa before the valve and 0.3 MPa after the valve, with a diameter of dn25 – can this be achieved with a control valve?
High pressure differences require special designs for cavitation prevention and noise reduction; it is necessary to contact the manufacturer for confirmation.
The pressure difference is too large; a multi-stage pressure reducing valve can be used.
The pressure difference is 12.7 MPa – that’s quite high; I’ve never encountered such a value before. I’ll keep an eye on it
Control valves for high pressure differences have a rather special structure; as long as the Cv value is provided to the manufacturer, there should be no problems. However, their price is likely to be high. Why not add a flow orifice plate in front of the valve?
No problem. The high differential pressure valves are manufactured in China by the German company Feihua Group; it has a branch in Shanghai, offices in Beijing and Guangzhou, and its Asian headquarters is there. They are just a bit more expensive
Sure, you can find out by checking the valves in the high-pressure system
There are many manufacturers of valves from Meisilonlan; it’s a piece of cake.
First use a pressure reducing valve to lower the pressure, and then a control valve will suffice. Use the process pressure relief valve, hehe
Korean KVT valves can solve this problem! ! !
The Fisher sleeve valve could be considered; our operating pressure is 5.0 Mpa at the front, while it’s almost at atmospheric pressure at the back, so there are no issues with regulation.
Adjustable angle valves also belong to control valves; they can reduce pressure. Extra-high pressure to low pressure pipelines are commonly used.
It can be easily solved using a high-pressure angle control valve
Have you never even heard of IN32MPa/OUT1.3MPa? High-pressure angle control valves and labyrinth control valves are used