Razif
Chemical
- Dec 15, 2002
- 14
Hi,
I wish to check if there was sufficient backflow protection in the mercaptan injection facilities to a LPG header. Diaphragm pumps are used for the service and each line has 2 dissimilar NRVs at present.
The reason I am reviewing this is that there was an incident where an operations staff observed the mercaptan storage vessel sweating.
I am somewhat pressured into putting in additional backflow protection, but I would like to run through an objective study to check if the above arrangement is already sufficient.
The header pressure is 6-8 barg and the storage vessels are under N2 blanket. I would appreciate some advice. Thanks.
RR
I wish to check if there was sufficient backflow protection in the mercaptan injection facilities to a LPG header. Diaphragm pumps are used for the service and each line has 2 dissimilar NRVs at present.
The reason I am reviewing this is that there was an incident where an operations staff observed the mercaptan storage vessel sweating.
I am somewhat pressured into putting in additional backflow protection, but I would like to run through an objective study to check if the above arrangement is already sufficient.
The header pressure is 6-8 barg and the storage vessels are under N2 blanket. I would appreciate some advice. Thanks.
RR