US2020171410A1PendingUtilityA1
Oil and Gas Well Primary Separation Device
Assignee: STUART PETROLEUM TESTERS INCPriority: Apr 19, 2013Filed: Feb 10, 2020Published: Jun 4, 2020
Est. expiryApr 19, 2033(~6.7 yrs left)· nominal 20-yr term from priority
Inventors:Glen Hendrix
B01D 19/0031E21B 43/34E21B 43/35
63
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Claims
Abstract
A primary separation apparatus for separating natural gas from high pressure, high velocity production streams comprising a liquid dispersion of water, sand, natural gas, and isolation plug cuttings.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . An apparatus ( 100 ) for separating natural gas from high pressure, high velocity production streams comprising a liquid dispersion of water, sand, natural gas, and isolation plug cuttings, said apparatus comprising:
a housing ( 102 ) having a first end and a second end, and an interior cavity ( 108 ) extending therebetween; an inlet port ( 110 ) disposed at said first end of said housing; a flow sleeve ( 142 ) disposed within said interior cavity of said housing and extending from said first end to said second end of said housing; a first screen ( 144 ) disposed within said flow sleeve and in fluid communication with said inlet port, wherein an annulus ( 143 ) is formed between an outer diameter of said first screen and an inner diameter of said flow sleeve; a baffle ( 150 ) within said interior cavity at said second end of said housing, wherein said baffle is arranged and designed to enhance separation of said production stream into its constituents; a liquid drain ( 138 ) in a lower portion of said housing; a second screen ( 178 ) coupled to an upper portion of said housing; and a gas outlet ( 168 ).
2 . The apparatus of claim 1 , further comprising a plurality of perforations in said first screen ( 144 ) having a diameter of at least about ⅛ inch up to about 3 inches.
3 . The apparatus of claim 1 , said flow sleeve further comprising one or more ports ( 145 a , 145 b ) located proximate a second end of said flow sleeve.
4 . The apparatus of claim 1 , further comprising a plurality of perforations in said second screen ( 178 ) having a diameter of at least about 20 microns up to about 1 inch.
5 . The apparatus of claim 1 , wherein said baffle ( 150 ) is sized to have an outer diameter that is less than an inner diameter of said housing ( 102 ) thereby forming an upper passageway ( 152 ) and a lower passageway ( 154 ) there between.
6 . The apparatus of claim 1 , further comprising a pressure gauge ( 137 ) coupled to said inlet port ( 110 ) and arranged and designed to monitor pressure entering said inlet port.
7 . The apparatus of claim 1 , further comprising a pressure gauge ( 139 ) coupled to said main housing ( 102 ) and arranged and designed to monitor pressure within said interior cavity ( 108 ) of said main housing.
8 . The apparatus of claim 1 , wherein said first and second screens are removable from said housing for replacement or cleaning.
9 . A flowback system comprising:
a fracturing tree ( 10 ) disposed on a producing well from which a high pressure, high velocity production stream comprising a liquid dispersion of water, sand, natural gas, and drilled plug cuttings flows; a primary separator ( 100 ) configured for receiving said production stream through a fluid line ( 12 ) from said fracturing tree, the primary separator comprising:
an isolation plug cutting separator comprising a first screen ( 144 ) having a plurality of perforations and extending axially within a flow sleeve ( 142 ), wherein said perforations are configured having a diameter such that drilled plug cuttings remain within said first screen;
a gas separator comprising a second screen ( 178 ) having a plurality of perforations configured having a diameter such that gas particles flow outwardly through the perforations and sand and other small sediment remains within said second screen;
a three-phase separator ( 16 ) configured for receiving gas particles separated in said gas separator and exiting said primary separator through a gas line ( 14 ); and a fluid-sand clean-up line ( 18 ) configured for removing separated liquid and solid matter exiting said primary separator.
10 . The flowback system of claim 9 , wherein said plurality of perforations in said first screen ( 144 ) are configured having a diameter of at least about ⅛ inch up to about 3 inches.
11 . The flowback system of claim 9 , wherein said plurality of perforations in said second screen ( 178 ) are configured having a diameter of at least about 20 microns up to about 1 inch.
12 . The flowback system of claim 9 , the primary separator further comprising a liquid drain ( 138 ) through which liquid and solid matter may flow out of said primary separator into said fluid-sand clean-up line ( 18 ).
13 . The flowback system of claim 9 , the primary separator further comprising a gas outlet ( 168 ) through which gas particles may flow out of said primary separator into said gas line ( 14 ).
14 . A method of processing a production fluid containing a mixture of fracking fluids, drilled isolation plug cuttings, oil and natural gas, water, and sand or other sediment and small solid matter using a single separation device, the method comprising:
flowing said production fluid into said separation device ( 100 ) through an inlet port ( 110 ) and through a first screen ( 144 ), thereby trapping drilled isolation plug cuttings within said first screen and filtering fluids and smaller solid matter radially outward through perforations of said first screen; impinging filtered fluids and smaller solid matter on a flow baffle ( 150 ), thereby further separating gas particles from said filtered fluids; flowing separated gas particles through a second screen ( 178 ), thereby trapping remaining sand and other small sediment within said second screen, wherein said separated gas particles then exit said separation device; and evacuating remaining separated fluids and solid matter through a liquid drain ( 138 ) at a bottom portion of said separation device.
15 . The method of claim 14 , further comprising flowing said production fluid through said separation device at a rate of between about two and twenty barrels per minute, thereby optimizing separation mechanisms dependent on gravity and retention time.
16 . The method of claim 14 , further comprising processing said separated gas particles, after exiting said separation device, in a three-phase separator ( 16 ).
17 . The method of claim 14 , further comprising transferring said separated fluids and solid matter, after exiting said separation device, through a fluid-sand clean-up line ( 18 ).Join the waitlist — get patent alerts
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