Does anyone have a quick method/rule of thumb that can be used as the sizing basis for a slug catcher/separator located on the inlet to a compressor on a natural gas line.
The intent of the vessel is to just avoid any liquid carry-over into the compressor. So far, the idea is to place a control valve on the inlet to the vessel to minimize the slug flow into the vessel. If I have this control valve in place does this mean that any size vessel (16" above) will work?
Any help would be much appreciated.
thank you.
The intent of the vessel is to just avoid any liquid carry-over into the compressor. So far, the idea is to place a control valve on the inlet to the vessel to minimize the slug flow into the vessel. If I have this control valve in place does this mean that any size vessel (16" above) will work?
Any help would be much appreciated.
thank you.