Safety Relief Valve Lifting
Safety Relief Valve Lifting
(OP)
I am at a plant working on a few product transfer lines. I transfer from building to building crossing out side containment areas. As part of an environmental project, I had automatic valves installed at each building. Before the operator transfers, he must test the line for leaks by charging it for 5 mins. He shuts one valve, pumps until it is full, then shuts the second valve. During our PHA it was determined that we needed Safety Relief Valves on each line. I had these installed which are set to discharge at 165 psi. There are five lines total, of which one relief valve keeps lifting slightly only discharging about a quart of product. I thought it was a bad relief valve so i swapped it for another. That one again lifted. It seems to only be happening in the very beginning of the charge. I removed the failing relief valve and installed a tell-tale pressure indicator on the same flange. The highest pressure shown on the gauge was 70 PSIG. I do not understand, both relief valves were sized for 165 PSIG. The product temperature is about 62 deg C.
I was thinking I needed an expansion tank to absorb the air that could be trapped in the product transfer line when the operator began charging.
But then why is it not shown on the pressure indicator?
Any Ideas?
I was thinking I needed an expansion tank to absorb the air that could be trapped in the product transfer line when the operator began charging.
But then why is it not shown on the pressure indicator?
Any Ideas?





RE: Safety Relief Valve Lifting
What product is this?
Is there air in the line, or product at vapor pressure?
Does a pump start in order to pressure these lines?
Does a valve open quickly to pressure these lines?
Is this the first relief valve after the pump?
"People will work for you with blood and sweat and tears if they work for what they believe in......" - Simon Sinek
RE: Safety Relief Valve Lifting
It is a capital mistake to theorise before one has data. Insensibly one begins to twist facts to suit theories, instead of theories to suit facts. (Sherlock Holmes - A Scandal in Bohemia.)
RE: Safety Relief Valve Lifting
The pump is used to pressurize the line. The valves that are being opened and closed at the terminal points are air operated and are not that quick but I would say have typical operating speeds.
This relief valve is the one and only one on the line and it just so happens to be the longest line. (Initially I thought the steam tracing was causing the expansion during the 5 min pressurization test, but I no longer think that)
If it is rapid transient pressure response, I am assuming an expansion tank would compensate for this?
RE: Safety Relief Valve Lifting
Good luck,
Latexman
RE: Safety Relief Valve Lifting
Open the valves, start the pump, clear the line of air.
Close the downstream valve, or if the relief goes off, stop the pump, then close the downstream valve.
If the pump is off, restart the pump.
Bring to pressure. Close the upstream valve. Stop the pump, if you need to (it gets hot, cavitates, or somthing).
Hold for 5 minutes.
Open both valves and start the pump.
Let us know how that went.
Independent events are seldomly independent.
RE: Safety Relief Valve Lifting
Good luck,
Latexman
RE: Safety Relief Valve Lifting
I checked the sequence of operation. It is in fact operating as you suggested. Both valves are open and the pump begins transferring to clear the air in the line. Then the downstream valve shuts followed by the upstream valve.
I do have another hypothesis. On the relief valve that is acting up, we installed a longer leg off of the transfer line and then put the flange for the relief valve. This was done to clear piping in the way. I am assuming this is trapping air that is in the line. As the line fills the pressure increases enough to push the air past the seat of the valve. (I was told that safety valves are rated for air or hydraulics but not both) Since the air is thinner it is able to escape followed by some product until the PRV seats. This seemed logical, but when I called the PRV vendor they told me that if the air pressure was within 10% of the set pressure, then possibly that is what is happening. But they don't believe that it the case here as we only see 70 psig.
What do you guys think? Are there any general rules of thumb on this?
I can send a picture of the install.
RE: Safety Relief Valve Lifting
RE: Safety Relief Valve Lifting
RE: Safety Relief Valve Lifting
Air in the line will dramatically complicate the issues, as volumes expand and contract quickly enough to accelerate liquid in the line and the resulting pressure spikes can become large and fast as they come to a halt, 10% or not.
Independent events are seldomly independent.
RE: Safety Relief Valve Lifting
Good luck,
Latexman
RE: Safety Relief Valve Lifting
RE: Safety Relief Valve Lifting
First valve. (?) I don't know which step, or which valve you mean, in the sequence.
Can you turn the pump off before closing the valve.
Can the 3 foot leg be reduced. That's not helping.
Why does this system need that relief valve? Does the pump have the capability to exceed pipe allowable pressure. Were high transient pressures, requiring a relief valve, expected? I'm having a hard time seeing why it must be there, and located there in the rack.
Independent events are seldomly independent.
RE: Safety Relief Valve Lifting
Good luck,
Latexman
RE: Safety Relief Valve Lifting
Anyway, if he's closing one, or any valve, he could probably turn the pump off first, if it's not off already. I imagine that could fix the problem right there.
Independent events are seldomly independent.
RE: Safety Relief Valve Lifting
Good luck,
Latexman
RE: Safety Relief Valve Lifting
It would help me a lot, if we had an actual numbered stepped sequence list that matches a diagram of valves #1 and #2 with the relief event inserted between the proper numbered steps.
Independent events are seldomly independent.
RE: Safety Relief Valve Lifting
Good luck,
Latexman
RE: Safety Relief Valve Lifting
I already scheduled maintenance to make the changes on the inlet leg of the relief valve for the end of the week. I do not see/hear any hammering but I figured it is worth a shot. I had access to a lift today and was able to throttle the air supply to Air Valve #2 to slow down the closing speed. Since all the equipment is tied into a PLC, the program only allows for 2 seconds for the valve to close before it throws a Valve Failure code. I slowed it down as much as I could without generating a failure. If in fact it did help, I'd have to have the program modified. I should know tomorrow night when the next transfer occurs.
Thanks for your help guys.
RE: Safety Relief Valve Lifting
Sequences are usually converted to programatic events, as is so in your case, so the best way to discuss sequences is LIST EACH STEP ... BY THE NUMBERS. Get in the habit now. I say that because actually your sequence still is not totally clear. You seem to say (you don't say exactly) that the pump stops when set pressure is reached, yet you never say it starts again, so I'm not sure if it actually stops, or not.
1) Open V1 & V2
2) Start Pump
3) Flow Confirmed
4) Close V2 relief event???
"The pump continues to run until" (when exactly?)
5) Pressure Set Point Reached
6) Stop Pump
7) Close V1
8) Wait 5 minutes
9) Pressure Set Point Holds
10) Open V1 & V2
Start Pump I'm not sure if pump started, or not. I assume yes.
11) Transfer Product
I assume the relief event occurs immediately after step 4.
If that is true, I agree that your best bet is to slow down that valve.
Independent events are seldomly independent.
RE: Safety Relief Valve Lifting
Wouldn't it be safer to do routing hydrotests every few months using water?
RE: Safety Relief Valve Lifting
Independent events are seldomly independent.
RE: Safety Relief Valve Lifting
m2609 touched on an "issue" that I had briefly thought about before, but I ignored it to help stop the acid from coming out where it shouldn't. Unfortunately, many small issues in this post are starting to add up to big problems. Routinely blowing a steam traced and insulated line because the acid is/may be freezing? There's a problem somewhere. Two valves in normal operation that trap acid in a steam traced and insulated line? One valve will stop flow and prevent backflow. Remove the second valve (and possible the pump's check valve) from normal operation; handle non-normal operation administratively to avoid trapping liquid. I've seen "leak checks" every transfer when the containment of the fluid path is compromized each time, but not a hard-piped line at every transfer? I've never seen that before. Now, a FO valve in acid transfer service. These "issues" are complicating the operation and adding unnecessary risk. Take care of these things and you can probably eliminate the PSV.
Good luck,
Latexman