US2023332059A1PendingUtilityA1
High Pressure Oil Treatment Process
Est. expiryNov 5, 2039(~13.3 yrs left)· nominal 20-yr term from priority
C10G 53/02C10G 33/00B01D 3/148B01D 3/007B01D 17/045C10G 2300/1033B01D 19/0063B01D 19/0005
60
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Claims
Abstract
A method and apparatus for separating production fluids using a system designed to minimize the heating requirements through thermodynamic efficiency and reduce equipment costs.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . A method for separating production fluids comprising:
sending production fluids into a fluid separator to generate a first gas output, a first oil output, and a first water output; heating the first oil output in an oil heater to generate a heated second oil output; generating a gas slipstream from the first gas output; and stripping the light hydrocarbons by combining the gas slipstream with the heated second oil output in a gas stripping column to generate a dead third oil output and a second gas output.
2 . A method for separating production fluids of claim 1 further comprising sending the first water output to a coalescer to generate a third gas output, a second water output, and a coalescer oil output.
3 . A method for separating production fluids of claim 1 further comprising flashing off light hydrocarbons from the third oil output to generate a fourth oil output and a flash off gas.
4 . A method for separating production fluids of claim 2 further comprising combusting the light hydrocarbon flash off.
5 . A method for separating production fluids of claim 1 , wherein the slipstream is generated using a flow control valve on the first gas output.
6 . A method for separating production fluids of claim 1 , wherein the dead third oil output is suitable for sale in an oil pipeline.
7 . A method for separating production fluids of claim 1 , further comprising flashing off light hydrocarbons of the first oil output before heating it.
8 . A method for separating production fluids of claim 1 , wherein the oil heater raises the first oil temperature to 170 F.
9 . A method for separating production fluids of claim 1 , further comprising maintain a constant oil level in the gas stripping column.
10 . A method for separating production fluids of claim 1 , further comprising combining the coalescer oil into the first oil output.
11 . A method for separating production fluids of claim 1 , further comprising sending the third oil output into a flash tank to generate a fourth oil output and a third gas output.
12 . A method for separating production fluids of claim 1 , further comprising pumping the heated second oil output into flash pot, wherein gas is separated off of the heated second oil output before it enters the gas stripping column.
13 . A method for separating production fluids of claim 1 , further comprising regulating the pressure on the gas stripper column at or below sales gas pressure.Join the waitlist — get patent alerts
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