hianbotech
Petroleum
- Aug 23, 2004
- 45
Right now, We are designing a Natural Gas Gathering Pipelines from different oil produced clusters. In the actual design we are considering use pig traps in the main trunklines, but we are thinking to use pig valves for some branches (economical reasons). However we have not had experience with these kind of Valves, only vendors references.
The question is knowing the experience with this kind of pig valves in similar services, instead using pig traps (launch and receiving). These valves are safety?. How is the recommended instalation?. There are some pressure restriction for using?.
This kind of specialty item permits a double block & bleed valve that can send or receive pigs, all in one only piece.
You can see the detail in this Weg page:
The conditions of the Gas Pipelines will be: 58-100 psig and 67 - 131°F. The fluid will be Natural Gas. the pipe sizes are between 4 and 10 inches.
An aditionally question regards Gas Pipelines is if there are some criterias to determine when is necessary to have a pigging clean system. I know that its depends of topography, diameter, length of pipelines, gas flows, gas composition and quantity of condensates, etc. But I do not have the guidelines for this issue.
I will apreciate your help on these issues.
Best Regards,
Hianbo
The question is knowing the experience with this kind of pig valves in similar services, instead using pig traps (launch and receiving). These valves are safety?. How is the recommended instalation?. There are some pressure restriction for using?.
This kind of specialty item permits a double block & bleed valve that can send or receive pigs, all in one only piece.
You can see the detail in this Weg page:
The conditions of the Gas Pipelines will be: 58-100 psig and 67 - 131°F. The fluid will be Natural Gas. the pipe sizes are between 4 and 10 inches.
An aditionally question regards Gas Pipelines is if there are some criterias to determine when is necessary to have a pigging clean system. I know that its depends of topography, diameter, length of pipelines, gas flows, gas composition and quantity of condensates, etc. But I do not have the guidelines for this issue.
I will apreciate your help on these issues.
Best Regards,
Hianbo