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Step-down pressure of demin water line

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Wizard74

Chemical
Oct 1, 2002
18
I am looking for options to reduce the demin water pressure from a 8 barg header to about 5 barg for a downstream process unit. The downstream unit has been designed to work with a low pressure rating and there is a relief valve set at 5.5 barg. Anybody got any sugestions on what can be used to do that? Thanks.
 
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A control valve with a downstream pressure controller?
 
Thanks, TD2K. Is a control valve inevitable for a liquid service?
 
I'm not quite sure what you are asking. I could assume the 8 barg and 5.5 barg pressure ratings are design pressures since you have a PSV set at 5.5 barg on the LP system.

Do you need to reduce the operating pressure? Are you trying to prevent the PSV from opening?

I don't know what your flowrate is to the lower pressure system but a control valve would be a pretty common solution. The dP across an RO will vary as the flow rate changes. The dP is likely too low for a hydraulic recovery turbine. We really need some more information on your system and what you are trying to achieve.
 
Sorry for the lack of information. The primary objective is to prevent the RV from lifting. So I guess a control valve will be a solution.
 
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