LSUUR
Industrial
- Jul 11, 2018
- 7
Hello All
I would like to get advice on problem I am facing.
I have delivered few small packages as attached file, two vessles are there and one is operating, one is stand by.
Fluid is LNG with oil particle.(Operating temp : -146 degC)
When change from operating to stand by(verse is same), we open/close double ball valves(5 inch).
(1 time per month, valves will be opened or closed)
Problem is many claim comes out from customer about valve(seat) leakage, Customer is saying valve quality problem,
Valve company do not agree with quality, they are in doubt for using double valves for LNG application.
Can you advise if double valves shall not be used for LNG application? If so, is there any other options we take?(double valves are in project specification)
I would like to get advice on problem I am facing.
I have delivered few small packages as attached file, two vessles are there and one is operating, one is stand by.
Fluid is LNG with oil particle.(Operating temp : -146 degC)
When change from operating to stand by(verse is same), we open/close double ball valves(5 inch).
(1 time per month, valves will be opened or closed)
Problem is many claim comes out from customer about valve(seat) leakage, Customer is saying valve quality problem,
Valve company do not agree with quality, they are in doubt for using double valves for LNG application.
Can you advise if double valves shall not be used for LNG application? If so, is there any other options we take?(double valves are in project specification)