Pulsation Dampner on Reciprocating Compressor
Pulsation Dampner on Reciprocating Compressor
(OP)
Hello,
We are facing an issue with one of our standard requirements versus what the vendor has been proposing regarding drain connections on the pulsation dampners on a recip machine. The machine is for hydrogen use and is a 3 stage recip machine with intercoolers with a MP and HP hydrogen supply.
The vendor has provided a drain and vent connection on the suction dampners to address any oil carry over issues or liquid that might condense out of the gas as a result of compressor and cooling. However, the vendor does not see a need to provide drain connections on the discharge dampners. The reasoning being that all liquids will be taken care of at the suction side dampner into each of the stages without damange to the machine. Also, prior to sending the gas at the battery limit there are MP and HP coalesers to knockout any oil out of the gas.
I am not sure why our standard would call out for having drain connections on the discharge dampners. I do not see a reason in my opinoin since dampners are not K/O drums or collection drums to being with and plus any liquid carry over will be addressed at the suction dampners to drain oil/liquid if any in the process stream before it enters subsquent stages.
Could someone provide with any advantage or disadvtage of having drains at the discharge dampners. Given this is a hydrogen serverice I would assume it is best to avoid additional connections. But what does the experience out there dictate.
Thanks in Advance
We are facing an issue with one of our standard requirements versus what the vendor has been proposing regarding drain connections on the pulsation dampners on a recip machine. The machine is for hydrogen use and is a 3 stage recip machine with intercoolers with a MP and HP hydrogen supply.
The vendor has provided a drain and vent connection on the suction dampners to address any oil carry over issues or liquid that might condense out of the gas as a result of compressor and cooling. However, the vendor does not see a need to provide drain connections on the discharge dampners. The reasoning being that all liquids will be taken care of at the suction side dampner into each of the stages without damange to the machine. Also, prior to sending the gas at the battery limit there are MP and HP coalesers to knockout any oil out of the gas.
I am not sure why our standard would call out for having drain connections on the discharge dampners. I do not see a reason in my opinoin since dampners are not K/O drums or collection drums to being with and plus any liquid carry over will be addressed at the suction dampners to drain oil/liquid if any in the process stream before it enters subsquent stages.
Could someone provide with any advantage or disadvtage of having drains at the discharge dampners. Given this is a hydrogen serverice I would assume it is best to avoid additional connections. But what does the experience out there dictate.
Thanks in Advance





RE: Pulsation Dampner on Reciprocating Compressor
All piping and equipment exposed to potentially wet gas should be sloped and be able to drain to a low point with a drain valve. Can these drain to somewhere else?
I don't recommend changing any company standards, unless you are an expert in your field. Even then it could be risky. IMO your efforts are best spent in ensuring that you get what your specifications called for.
I hate Windowz 8!!!!
RE: Pulsation Dampner on Reciprocating Compressor