US2844213A - Water knockout tanks - Google Patents
Water knockout tanks Download PDFInfo
- Publication number
- US2844213A US2844213A US48445355A US2844213A US 2844213 A US2844213 A US 2844213A US 48445355 A US48445355 A US 48445355A US 2844213 A US2844213 A US 2844213A
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- United States
- Prior art keywords
- water
- chamber
- tank
- oil
- distillate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G33/00—Dewatering or demulsification of hydrocarbon oils
- C10G33/06—Dewatering or demulsification of hydrocarbon oils with mechanical means, e.g. by filtration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0208—Separation of non-miscible liquids by sedimentation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0208—Separation of non-miscible liquids by sedimentation
- B01D17/0214—Separation of non-miscible liquids by sedimentation with removal of one of the phases
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/2931—Diverse fluid containing pressure systems
- Y10T137/3003—Fluid separating traps or vents
- Y10T137/3006—Liquids separated from liquid
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/4456—With liquid valves or liquid trap seals
- Y10T137/4463—Liquid seal in liquid flow line; flow liquid forms seal
- Y10T137/4546—Downward partition encircles projecting outlet
Definitions
- This invention relates to improvements in water knockout vessels such as commonly used in the oil industry, and more particularly, but not by way of limitation, to a free water knockout tank designed to maintain a sensitive control of the water level within the vessel and to prevent loss of distillate through failure of proper control thereof.
- the fluid from producing oil wells often comprises a mixture of gas, oil and water.
- the fluid is of an emulsion type which requires the use of heat, with or without chemicals in order to separate the water from the mixture.
- the water in the fluid is known as free water and may be easily separated from the gas-oil mixture by gravity.
- fluids containing free water are transported from an oil well directly to a free water knockout tank wherein a column of the oil-gas-water mixture is collected. Oil and gas are of lighter weight than water and, therefore, will rise to the top of the fluid column in the vessel. This permits the oil and gas to be removed therefrom free of the bulk of the water so that the water will not have to be handled during the remaining processing or separation of the gas-oil mixture.
- Free water removed in the above manner in existing knockout vessels is normally controlled by a liquid level controller which operates on the distillate-water interface. It will be apparent that the sensitivity of the distillate- .water interface level control apparatus is greatly lessened with respect to a top level control operating between liquids and gases and usually will not adequately control the water level within the tank. If the water level is permitted to rise too high within the vessel it will usually.
- the present invention contemplates an improved free water knockout tank designed with upper and lower compartments to permit a positive sensitive water level control at the top level of the water as opposed to level control on the distillate-water interface. It will be apparent that this type of level control will provide a more eflicient operation of the vessel by substantially reducing the possibility of the water level rising too high therein. Further, the two compartment design substantially precludes the possibility of loss of distillate with the discharged water due to failure of the level control device by providing a water seal in the upper chamber to prevent flow of the distallate into the lower chamber.
- Figure 1 is a vertical sectional view of knockout vessel embodying the invention.
- Figure 2 is a vertical sectional view of a modified form of the invention.
- the vessel 10 refers in general to a free water knockout vessel of substantially an upright cylindrical configuration.
- the vessel 10 comprises a shell 12 with closed ends 13 and 14, a substantially horizontal baflle 15 secured therein which separates the vessel 10 into an upper chamber 16 and a lower chamber 18.
- An inlet port 20 is provided in the upper portion of the shell 12 for receiving any suitable inlet means 22 to permit access to the chamber 16 for a purpose as will hereinafter'be set forth.
- An outlet port 24 is also provided in the shell 12 and is preferably disposed in the upper chamber 16 at a position below and diametrically opposite the inlet port 20.
- Any suitable nipple 26 is secured within the outlet port 24 and cooperates with a weir box 28 in a well known manner to permit discharge of fluid from the chamber 16 as will hereinafter be set forth in detail.
- a suitable drain means 30 is provided at the bottom 14 of the shell 12 to permit discharge of liquid from the lower chamber 18 and complements a suitable liquid level control device 32' to control the liquid level within the chamber 18.
- a pipe 34 extends upward from a point spaced above the bottom 14 of the shell 12, through the baflle 15' and into the chamber 16 for communicating liquid from the chamber 16 to the chamber 18.
- the pipe 34 is provided with a plurality of equalizer apertures 35 disposed below the baflie 15.
- the pipe 34 terminates at its upper end within a riser 36 and at a point spaced below the-weir box 28.
- the riser 36 is vertically spaced within the chamber and may be supported therein by any suitable means, such as brackets (not shown). It will be apparent that any a free water 10 in a vertical position.
- the fluid discharging from oil wells is usually a mixture of gas, oil and water, with the water in a free state, and is transferred from the well directly into a water knockout tank such as the vessel 10 described herein.
- the infiuent enters the vessel 10 through the inlet means 22 for disposition within the upper chamber 16.
- the influent will fall by gravity to the bottom of the chamber 16 to form a fluid column.
- the oil and gas in the emulsion is of lesser specific gravity than the water, and will therefore rise to the top of the column to form a distillate 40 above the free water 42. This separation process forms an interface 43 between the two liquids.
- the free water 42 will be forced upward in the annulus 45 between the pipe 34 and the riser pipe 36 and will fall through the pipe 34 into the lower chamber 18 providing a reservoir 44.
- the displaced air or gas within the chamber 18 will discharge through the equalizer ports 35 and flow upward through the pipe 34 and riser 36.
- the gas and distillate will be discharged from the chamber 16 through the outlet nipple 26 to storage or the like.
- the top of the pipe 34 in relation to the weir box 28 will control the respective heights of the distillate and water in much the same manner as is well known in a conventional treater or separator assembly.
- the level of the free water 44 in the chamber 18 will be controlled by the level control device 32 in the usual manner.
- the liquid in the chamber 18 is substantially water; the control of the water level therein will provide a more sensitive action than would be possible if the level control apparatus were acting at the top level of the interface 43 between water and oil.
- the level control will not only be more sensitive, but will also be more reliable, thus providing a more efficient operation of the knockout vessel 10.
- no distillate will be lost or discharged with the water through the drain 30 beacuse the water 42 in the upper chamber 16 will form a seal between the distillate 40 in chamber 16 and precludes discharge into the pipe 34.
- FIG. 2 depicts a modified form of the present invention wherein a cylindrical tank 50 and a smaller tank 52 are horizontally disposed in a spaced relationship.
- the well stream enters the tank 50 through an inlet means 54 and impinges against an angled deflector plate 56 which may be secured within the tank 50 in any well known manner (not shown).
- Water, emulsion and distillate are separated in the tank 50 by gravity and fall to the bottom thereof to form a reservoir 57.
- the liquids will flow around the water box 58, and the liquid level is controlled by a weir plate 60 in a well known manner.
- the liquid surface is protected by a perforated plate 62.
- the water as hereinbefore stated, is the heaviest constituent in the emulsion and will settle by gravity to the bottom of the tank 50 and will flow downward into a chamber 61 in the tank 52 through a pipe 64 which connects the tanks 50 and 52. The water will then flow upward through a second connecting pipe 66 which provides communication between the chamber 61 and the interior of the water box 58.
- a pipe 68 extends upwardly in the water box 58 to a point below the top edge of the weir plate 60 for controlling the level of the oil-water interface 70 in a manner well known in the industry. Water will flow downward into a chamber 72 in the tank 52.
- the chamber 72 is separated from the chamber 61 by a plate 74 which is secured to the inner periphery of the tank 52 in any well known manner (not shown).
- a suitable level control 76 cooperates with a suitable motor valve (not shown) to control the outgoing water through a water outlet 78.
- An outlet means 80 communicates with a gage glass (not shown) to provide an exterior sight glass. If the motor valve fails open, the chamber 72 is drained of water and gas will blow through an opening 82 in the water box 58 to the motor valve.
- the water in the chamber 61 forms a seal to prevent loss of distillate through the drain 78.
- the gas and oil remaining in the upper portion of the tank 50 is discharged through an outlet means 84 for transfer to storage, or the like.
- the present invention provides a novel free water knockout vessel 6?. which maintains a sensitive and reliable water level control to substantially eliminate disadvantages inherent in such devices lacking such efficient controlling.
- the provision of a free water reservoir completely separate from the gas and distillate substantially precludes the loss of distillate if failure of the water control apparatus occurs.
- a free water knockout vessel comprising upper and lower horizontally disposed cylindrical tanks, means for admitting a gas-oil-water mixture to the upper tank wherein free water is separated by gravity from the oil and gas components, means for controlling the liquid level of the emulsion in the upper tank, a water box in the upper tank, a vertical bafile in the lower tank to provide a left hand and a right hand chamber therein, flow pipe means to communicate free water from the upper tank to the left hand chamber, flow pipe means to communicate water from the left hand chamber to the water box, flow pipe means to control the water level in the water box and to transport the water to the right hand chamber, means to control the Water level in the right hand chamber, drain means in the right hand chamber to discharge water therefrom, means in the upper tank to discharge the gasoil distillate therefrom, said water in the left hand chamber providing a seal to prevent loss of gas-oil distillate from the vessel.
- a free water knockout vessel comprising upper and lower horizontally disposed cylindrical tanks, a water box in the upper tank, a vertical bafile secured within the lower tank to provide two chambers therein, means for admitting a gas-oil-water mixture to the upper tank wherein free water is separated by gravity from the oil and gas components, means for communicating the separated free water to the water box by passage through one chamber of the lower tank, means for communicating the water from the water box to the second chamber in the lower tank, drain means in the second chamber for discharging the water therefrom, said water in the first chamber providing a seal to preclude accidental loss of gas-oil distillate with the free water discharged from the vessel, and means in the upper tank to discharge the gas-oil distillate therefrom,
Description
y 22, 1958 I s. A. WIL ON 2,844,213
WATER KNOCKOUT TANKS Filed Jan. 27, 1955 2 Sheets-Sheet 1 IN V EN TOR.
5. A. Wilson 1 BY ,5 ATTORNEY July 22, 1958 s. A. WILSON wmsmmocxour'rmxs- 2 Sheets-Sheet 2 Filed Jan. 27, 1955 INVENTOR. 5.- A. W//.s0n
Q BY ATTORNEY United States Patent WATER KNOCKOUT TANKS Samuel A. Wilson, Minden, La., assignor to National Tank Company, Tulsa, Okla., a corporation of Nevada Application January 27, 1955, Serial No. 484,453 2 Claims. c1. 1832.7)
This invention relates to improvements in water knockout vessels such as commonly used in the oil industry, and more particularly, but not by way of limitation, to a free water knockout tank designed to maintain a sensitive control of the water level within the vessel and to prevent loss of distillate through failure of proper control thereof.
It is well known in the oil industry that the fluid from producing oil wells often comprises a mixture of gas, oil and water. Sometimes the fluid is of an emulsion type which requires the use of heat, with or without chemicals in order to separate the water from the mixture. In many other instances, however, the water in the fluid is known as free water and may be easily separated from the gas-oil mixture by gravity. For example, fluids containing free water are transported from an oil well directly to a free water knockout tank wherein a column of the oil-gas-water mixture is collected. Oil and gas are of lighter weight than water and, therefore, will rise to the top of the fluid column in the vessel. This permits the oil and gas to be removed therefrom free of the bulk of the water so that the water will not have to be handled during the remaining processing or separation of the gas-oil mixture.
Free water removed in the above manner in existing knockout vessels is normally controlled by a liquid level controller which operates on the distillate-water interface. It will be apparent that the sensitivity of the distillate- .water interface level control apparatus is greatly lessened with respect to a top level control operating between liquids and gases and usually will not adequately control the water level within the tank. If the water level is permitted to rise too high within the vessel it will usually.
flow therefrom with the distillate. Another disadvantage of present water knockout tanks is that in the event of liquid control failure, all the distillate may be lost. .For instance, if the water valve should fail in an open position the distillate would be discharged from the tank with the water. p
The present invention contemplates an improved free water knockout tank designed with upper and lower compartments to permit a positive sensitive water level control at the top level of the water as opposed to level control on the distillate-water interface. It will be apparent that this type of level control will provide a more eflicient operation of the vessel by substantially reducing the possibility of the water level rising too high therein. Further, the two compartment design substantially precludes the possibility of loss of distillate with the discharged water due to failure of the level control device by providing a water seal in the upper chamber to prevent flow of the distallate into the lower chamber.
- sensitive water level control to preclude the possibility of water being discharged with the gas-oil distillate as the distillate leaves the vessel.
2,844,213 Patented July 22, 1958 It is another object of this invention to provide an improved free water knockout vessel for use in the oil industry to separate water from a gas-oil-water mixture in such a manner as to prevent the gas-oil distillate from being lost due to the failure of the level control device.
It is a further object of this invention to provide an improved free water knockout vessel for use in the oil industry which is of a simple design for ease and economy of operation and construction.
Other objects and advantages of the invention will be evident from the following detailed description, read in conjunction with the accompanying drawings, which illustrate my invention.
In the drawings:
Figure 1 is a vertical sectional view of knockout vessel embodying the invention.
Figure 2 is a vertical sectional view of a modified form of the invention.
Referring to the drawings in detailfreference character 10 refers in general to a free water knockout vessel of substantially an upright cylindrical configuration. The vessel 10 comprises a shell 12 with closed ends 13 and 14, a substantially horizontal baflle 15 secured therein which separates the vessel 10 into an upper chamber 16 and a lower chamber 18. An inlet port 20 is provided in the upper portion of the shell 12 for receiving any suitable inlet means 22 to permit access to the chamber 16 for a purpose as will hereinafter'be set forth. An outlet port 24 is also provided in the shell 12 and is preferably disposed in the upper chamber 16 at a position below and diametrically opposite the inlet port 20. Any suitable nipple 26 is secured within the outlet port 24 and cooperates with a weir box 28 in a well known manner to permit discharge of fluid from the chamber 16 as will hereinafter be set forth in detail. A suitable drain means 30 is provided at the bottom 14 of the shell 12 to permit discharge of liquid from the lower chamber 18 and complements a suitable liquid level control device 32' to control the liquid level within the chamber 18. A pipe 34 extends upward from a point spaced above the bottom 14 of the shell 12, through the baflle 15' and into the chamber 16 for communicating liquid from the chamber 16 to the chamber 18. The pipe 34 is provided with a plurality of equalizer apertures 35 disposed below the baflie 15. The pipe 34 terminates at its upper end within a riser 36 and at a point spaced below the-weir box 28. The riser 36 is vertically spaced within the chamber and may be supported therein by any suitable means, such as brackets (not shown). It will be apparent that any a free water 10 in a vertical position.
Operation The fluid discharging from oil wells is usually a mixture of gas, oil and water, with the water in a free state, and is transferred from the well directly into a water knockout tank such as the vessel 10 described herein. The infiuent enters the vessel 10 through the inlet means 22 for disposition within the upper chamber 16. The influent will fall by gravity to the bottom of the chamber 16 to form a fluid column. The oil and gas in the emulsion is of lesser specific gravity than the water, and will therefore rise to the top of the column to form a distillate 40 above the free water 42. This separation process forms an interface 43 between the two liquids. As more fluid enters the chamber 16 the free water 42 will be forced upward in the annulus 45 between the pipe 34 and the riser pipe 36 and will fall through the pipe 34 into the lower chamber 18 providing a reservoir 44. As the chamber 18 is filled with free water, the displaced air or gas within the chamber 18 will discharge through the equalizer ports 35 and flow upward through the pipe 34 and riser 36. The gas and distillate will be discharged from the chamber 16 through the outlet nipple 26 to storage or the like. The top of the pipe 34 in relation to the weir box 28 will control the respective heights of the distillate and water in much the same manner as is well known in a conventional treater or separator assembly. The level of the free water 44 in the chamber 18 will be controlled by the level control device 32 in the usual manner. It will be apparent that the liquid in the chamber 18 is substantially water; the control of the water level therein will provide a more sensitive action than would be possible if the level control apparatus were acting at the top level of the interface 43 between water and oil. The level control will not only be more sensitive, but will also be more reliable, thus providing a more efficient operation of the knockout vessel 10. In the event of control failure, no distillate will be lost or discharged with the water through the drain 30 beacuse the water 42 in the upper chamber 16 will form a seal between the distillate 40 in chamber 16 and precludes discharge into the pipe 34.
Figure 2 depicts a modified form of the present invention wherein a cylindrical tank 50 and a smaller tank 52 are horizontally disposed in a spaced relationship. The well stream enters the tank 50 through an inlet means 54 and impinges against an angled deflector plate 56 which may be secured within the tank 50 in any well known manner (not shown). Water, emulsion and distillate are separated in the tank 50 by gravity and fall to the bottom thereof to form a reservoir 57. The liquids will flow around the water box 58, and the liquid level is controlled by a weir plate 60 in a well known manner. The liquid surface is protected by a perforated plate 62. .The water, as hereinbefore stated, is the heaviest constituent in the emulsion and will settle by gravity to the bottom of the tank 50 and will flow downward intoa chamber 61 in the tank 52 through a pipe 64 which connects the tanks 50 and 52. The water will then flow upward through a second connecting pipe 66 which provides communication between the chamber 61 and the interior of the water box 58. A pipe 68 extends upwardly in the water box 58 to a point below the top edge of the weir plate 60 for controlling the level of the oil-water interface 70 in a manner well known in the industry. Water will flow downward into a chamber 72 in the tank 52. The chamber 72 is separated from the chamber 61 by a plate 74 which is secured to the inner periphery of the tank 52 in any well known manner (not shown). A suitable level control 76 cooperates with a suitable motor valve (not shown) to control the outgoing water through a water outlet 78. An outlet means 80 communicates with a gage glass (not shown) to provide an exterior sight glass. If the motor valve fails open, the chamber 72 is drained of water and gas will blow through an opening 82 in the water box 58 to the motor valve. The water in the chamber 61 forms a seal to prevent loss of distillate through the drain 78. The gas and oil remaining in the upper portion of the tank 50 is discharged through an outlet means 84 for transfer to storage, or the like.
From the foregoing, it will be apparent that the present invention provides a novel free water knockout vessel 6?. which maintains a sensitive and reliable water level control to substantially eliminate disadvantages inherent in such devices lacking such efficient controlling. The provision of a free water reservoir completely separate from the gas and distillate substantially precludes the loss of distillate if failure of the water control apparatus occurs. These features not only provide a more efiicient water knockout tank, but reduce the expense of such operation by eliminating costly losses of distillate.
Changes may be made in the combination and arrangement of parts as heretofore set forth in the specification and shown in the drawings, it being understood that any modification in the precise embodiment of the invention may be made within the scope of the following claims without departing from the spirit of the invention.
1 claim:
1. A free water knockout vessel comprising upper and lower horizontally disposed cylindrical tanks, means for admitting a gas-oil-water mixture to the upper tank wherein free water is separated by gravity from the oil and gas components, means for controlling the liquid level of the emulsion in the upper tank, a water box in the upper tank, a vertical bafile in the lower tank to provide a left hand and a right hand chamber therein, flow pipe means to communicate free water from the upper tank to the left hand chamber, flow pipe means to communicate water from the left hand chamber to the water box, flow pipe means to control the water level in the water box and to transport the water to the right hand chamber, means to control the Water level in the right hand chamber, drain means in the right hand chamber to discharge water therefrom, means in the upper tank to discharge the gasoil distillate therefrom, said water in the left hand chamber providing a seal to prevent loss of gas-oil distillate from the vessel.
2. A free water knockout vessel comprising upper and lower horizontally disposed cylindrical tanks, a water box in the upper tank, a vertical bafile secured within the lower tank to provide two chambers therein, means for admitting a gas-oil-water mixture to the upper tank wherein free water is separated by gravity from the oil and gas components, means for communicating the separated free water to the water box by passage through one chamber of the lower tank, means for communicating the water from the water box to the second chamber in the lower tank, drain means in the second chamber for discharging the water therefrom, said water in the first chamber providing a seal to preclude accidental loss of gas-oil distillate with the free water discharged from the vessel, and means in the upper tank to discharge the gas-oil distillate therefrom,
References Cited in the file of this patent UNITED STATES PATENTS 2,457,959 Walker Jan. 4, 1949 2,657,760 Glasgow Nov. 3, 1953 2,681,150 Reid June 15, 1954 2,710,071 Kinser et al June 7, 1955 2,738,026 Glasgow et al Mar. 13, 1956 2,786,543 Hayes et al Mar. 26, 1957
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US48445355 US2844213A (en) | 1955-01-27 | 1955-01-27 | Water knockout tanks |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US48445355 US2844213A (en) | 1955-01-27 | 1955-01-27 | Water knockout tanks |
Publications (1)
Publication Number | Publication Date |
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US2844213A true US2844213A (en) | 1958-07-22 |
Family
ID=23924212
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US48445355 Expired - Lifetime US2844213A (en) | 1955-01-27 | 1955-01-27 | Water knockout tanks |
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US (1) | US2844213A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3146458A (en) * | 1960-11-18 | 1964-08-25 | Bethlehem Steel Corp | Underwater storage unit |
US3246493A (en) * | 1963-12-24 | 1966-04-19 | Hupp Corp | Dry cleaning apparatus |
US4723565A (en) * | 1981-08-10 | 1988-02-09 | Delwiche John L | Flow regulating device |
EP0492573A1 (en) * | 1990-12-24 | 1992-07-01 | Phillips Petroleum Company | Alkylation apparatus and method for isolating the catalyst |
US10272365B2 (en) | 2017-08-08 | 2019-04-30 | Randy J. Cumbee | Multi-phase emulsion separator with directed flow channels |
US20210395110A1 (en) * | 2019-07-19 | 2021-12-23 | Abtech Industries, Inc. | Vortex separator for thin-film evaporation unit with angled baffles |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2457959A (en) * | 1942-01-19 | 1949-01-04 | Nat Tank Co | Filtering tank for water disposal systems |
US2657760A (en) * | 1950-01-09 | 1953-11-03 | Nat Tank Co | Horizontal separator |
US2681150A (en) * | 1949-12-24 | 1954-06-15 | Laurance S Reid | Water separator |
US2710071A (en) * | 1951-11-17 | 1955-06-07 | Black Sivalls & Bryson Inc | Horizontal separator for mixed fluids |
US2738026A (en) * | 1953-11-02 | 1956-03-13 | Nat Tank Co | Low temperature separation process and unit |
US2786543A (en) * | 1952-02-13 | 1957-03-26 | Black Sivalls & Bryson Inc | Apparatus for treating liquid mixtures |
-
1955
- 1955-01-27 US US48445355 patent/US2844213A/en not_active Expired - Lifetime
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2457959A (en) * | 1942-01-19 | 1949-01-04 | Nat Tank Co | Filtering tank for water disposal systems |
US2681150A (en) * | 1949-12-24 | 1954-06-15 | Laurance S Reid | Water separator |
US2657760A (en) * | 1950-01-09 | 1953-11-03 | Nat Tank Co | Horizontal separator |
US2710071A (en) * | 1951-11-17 | 1955-06-07 | Black Sivalls & Bryson Inc | Horizontal separator for mixed fluids |
US2786543A (en) * | 1952-02-13 | 1957-03-26 | Black Sivalls & Bryson Inc | Apparatus for treating liquid mixtures |
US2738026A (en) * | 1953-11-02 | 1956-03-13 | Nat Tank Co | Low temperature separation process and unit |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3146458A (en) * | 1960-11-18 | 1964-08-25 | Bethlehem Steel Corp | Underwater storage unit |
US3246493A (en) * | 1963-12-24 | 1966-04-19 | Hupp Corp | Dry cleaning apparatus |
US4723565A (en) * | 1981-08-10 | 1988-02-09 | Delwiche John L | Flow regulating device |
EP0492573A1 (en) * | 1990-12-24 | 1992-07-01 | Phillips Petroleum Company | Alkylation apparatus and method for isolating the catalyst |
US10272365B2 (en) | 2017-08-08 | 2019-04-30 | Randy J. Cumbee | Multi-phase emulsion separator with directed flow channels |
US20210395110A1 (en) * | 2019-07-19 | 2021-12-23 | Abtech Industries, Inc. | Vortex separator for thin-film evaporation unit with angled baffles |
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