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The feed to a vapor–liquid separator may also be a liquid that is being partially or totally flashed into a vapor and liquid as it enters the separator. A slug catcher is a type of vapor–liquid separator that is able to receive a large inflow of liquid at random times. It is usually found at the end of gas pipelines where condensate may be ...
Finger type slug catcher at the Qadirpur Gas Field. Slug catchers are designed in different forms, A vessel type slug catcher is essentially a conventional vessel. This type is simple in design and maintenance. A finger type slug catcher consists of several long pieces of pipe ('fingers'), which together form the buffer volume. The advantage of ...
On Trent the fluids from Tyne were routed to a slug catcher then comingled with Trent gas from the Trent Production Separator. The combined gas stream was routed across the bridge to the TC platform. Here it passed successively to a Separator, LP Compressor, Cooler, Separator, HP Compressor, Cooler and Discharge Scrubber.
Onshore gas terminals may have facilities for removal of liquids from the incoming gas stream. Liquids may include natural gas liquids (NGL), produced water, and glycol (MEG or TEG). Separation of liquid from gas is done in slug catchers, which either comprise an array of pipes or a large cylindrical vessel. A variety of treatment processes are ...
A pig receiver and slug catcher. Vapour from the slug catcher is cooled and chilled in a gas-to-gas heat exchanger, then by a refrigerant system, and a Joule-Thomson pressure reduction valve before the, now two-phase, mixture passes to a separator.
Slug catcher and Front End Compression Area Qadirpur CCR-2. Qadirpur gas field is one of the major gas reserves of Pakistan. The field is located at a distance of 8 kilometres (5.0 mi) from Ghotki in Sindh Province.
Fluids from the satellite platforms (ST2 and ST3) are exported to the central complex. Upon arrival they are routed to a slug catcher, gas is routed to the inlet of the appropriate Glycol Contactor. Liquids are routed to the Condensate Separator and then the Condensate Coalescer prior to export through the gas pipeline. [10]
The ENI terminal was integrated into the Perenco Terminal in 2011, thereby diverting the Hewett, LAPS and at one time Thames gas and condensate from the slug catchers and compression in the Eni terminal to the Perenco terminal upstream of the dehydration and dew point control plant.
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