US1716934A - Oil and water separator - Google Patents

Oil and water separator Download PDF

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Publication number
US1716934A
US1716934A US184864A US18486427A US1716934A US 1716934 A US1716934 A US 1716934A US 184864 A US184864 A US 184864A US 18486427 A US18486427 A US 18486427A US 1716934 A US1716934 A US 1716934A
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oil
tank
water
heater
adjacent
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US184864A
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Hubert J Smith
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D17/00Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/02Separation of non-miscible liquids
    • B01D17/04Breaking emulsions
    • B01D17/042Breaking emulsions by changing the temperature

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  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

June 11, 1929; H. J. SMITH 1,716,934
OIL AND WATER SEPARATOR Filed April 19, 1927 OIL m: V: rm.
75' WITER.
STE/IN.
INVENTOR. Jzuamr J. 5mm
ZMW
HT TOR/V5)- Patented June 11, 1 929.
UNITED STATES HUBERT J. SMITH, 0]? LONG BEACH, CALIFORNIA.
OIL AND WATER SEPARATOR.
Application filed April 19,
In producing oil wells particularly those which have produced for a considerable length of time, a certain quantity of water is removed from the well with the oil. This water may be either salt or fresh, but is usually found to be salt water. Before the oil can be marketed it is necessary to remove the water and heretofore this has been accomplished by various mechanical, chemical, and electrical treatments which were expensive and entailed a considerable amount of additional labor above that required for-the ordinary production of the Well.
An object of my inventionis to provide a simple and inexpensive method and means of separating the oil and water which will not require the expenditure of additional labor.
Another object is to provide an oil and water separator which utilizes the heat of the steam found in or adjacent to every producing well.
A further object is to utilize heat for the separation of oil and water which heat is directly applied to the incoming liquid and which eliminates the danger of losing a large percentage of the more volatile oil constituents.
In the drawing:
F ig. 1 is a longitudinal sectional View of my separator.
Fig. 2 is a sectional view taken on line 2, 2
.of Fig. 1.
Referring more particularly to the draw- The numeral 1 indicates a large tank adapted to re-ceivethe liquid from the well and in the center of this tank I position a heater 2, said heater extending vertically in the tank and is substantially the entire height thereof. My heater 2 comprises a hollow cylinder 3 and a steampipe 4 extends through the wall of the tank 1 and into the heater 2 adjacent the bottom thereof. If desired, steam walls may be placed within the cylinder 3 although I do not find this absolutely essential.
The steam which enters the pipe 4 may be the exhaust from the pumping engine or it may be steam fed directly from the boilers. A valve 5 in the pipe 4 regulates the amount of steam entering the cylinder 3.- -A steam exhaust pipe 6 rises from the top of the cylinder 2 and a valve 7 is set in the pipe 6, said valve being useful in event that steam is used directly from the boilder tending to prevent the free escape of the steam, re-
1927. Serial No; 184,864.
tainingit longer in the cylinder and thus utilizing more of its heat. This valve may be adjusted to suit the particular conditions.
11 from the gas trap, or similar device, said pipe extending downwardly through the tank 1 and extends into an arcuate manifold 12 which partly surrounds the heater 2 adjacent the lower end thereof. Perforations 13 are provided in the manifold 12 through which the oil and water passes and impinges upon the outer surface of the cylinder 3 opposite the point where the steam enters through the pipe 4. Thus it will be seen that as the liquid enters the tank 1 it is brought. into direct contact with a heated surface thus quickly raising the temperature thereof, and this heating of the incoming liquid tends to -materially assist in the separation of the oil and water. The oil being lighter passes upw wardly in the tank through the water, 'as shown at 14, and floats in a layer at the top of the tank, as shown at 15.
An oil drain pipe 16 extends from the tank 1 adjacent the top thereof and within the. oil area 15, the oil draining through this pipe by gravity. A water outlet pipe 17 extends from adjacent the lower edge of the tank 1, said pipe rising to a point adjacent the top of the water layer 14. and drains away by gravity.
I have found it desirable to maintain the temperature of the water in the tank 1 below the boiling point thereof but the exact temperature of this water will vary for the different types of oil which may be produced from different wells. That is, some oils Wlll separate from .the water more readily at a temperature around 150 degrees F., plus or minus, while others Wlll require a temperature of 135 degrees, more or less, but this point will be determined more readily by experimenting with the particular o l found.
It is, of course, desirable to malntain as low a temperature as possible 1n the tank 1 in order that little or none of the lighter stituents of the oil should be lost.
Having described my invention, I cla m:
1. An oil and water separator comprising a tank, a heater in said tank adjacent the con- 7 center thereof and extending substantially thedepth of the tank, oil and water intake means'extending from the Well, said intake means terminating adjacent said heater and adjacent the bottom of the tank, whereby the incoming liquid impinges upon the tank, said heater comprising a hollow cylinder, a steam intake pipe adjacent the bottom of said cylinder, an exhaust pipe extending into the top of said cylinder, an oil and water intake pipe extending from'the well and-terminating adjacent said heater and adjacent the bottom of the tank whereby the incoming liquid is caused to impinge upon said heater.
3. An oil and water separator comprising a tank, a heater in said tank adjacent the center thereof and extending vertically therein, said heater comprising a hollow cylinder, a steam intake pipe adjacent the bottom of said cylinder, an exhaust pipe extend- 1 ing from the top of said cylinder, an oil and water intake pipe extending from the well and terminating adjacent said heater whereby the incoming liquid is caused to impinge upon said heater, a drain pipe extending from said heater, a valve in said drain pipe, anoil outlet pipe extending from the tank adjacent the top thereof,and a water outlet pipe extending from the tank adjacent the bottom thereof.
4. An oil and water separator comprising a tank, a heater in said tank adjacent the center thereof and extending vertically therein, 'a steam intake pipe extending to said heater adjacent the bottom thereof, an oil and water intake pipe, a manifold adjacent the bottom of the heater, said oil and water intake pipe extending to the inanifold, said manifold having perforations therein through which the oil and water passes, and impinges upon the heater, a drain pipe in said heater, an exhaust pipe extending from the heater, an oil drain pipe extending from the tank adjacent the top thereof, and a water outlet pipe extending from the tank and adjacent the bottom thereof.
In testimony whereof, I aflix my signature.
I-IUBERT'J. SMITH.
US184864A 1927-04-19 1927-04-19 Oil and water separator Expired - Lifetime US1716934A (en)

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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2693880A (en) * 1952-01-21 1954-11-09 Otto B Schoenfeld Emulsion separator
US2834464A (en) * 1954-08-23 1958-05-13 Socony Mobil Oil Co Inc Method and apparatus for continuous liquid thermal diffusion
US4594155A (en) * 1982-10-07 1986-06-10 Conway Charles S Immiscible fluid separation apparatus
DE8809056U1 (en) * 1988-07-14 1988-10-06 Schroeder, Heinrich, Dipl.-Ing., 2819 Thedinghausen, De
US5244569A (en) * 1992-02-14 1993-09-14 Paul Di Amico Toxic liquid collector
WO2000045930A1 (en) * 1999-02-05 2000-08-10 Komistek Stephen M Inclined emulsion treater
US20080006304A1 (en) * 2006-07-10 2008-01-10 Mdk Innovations Inc. Flock tank
WO2021141655A1 (en) * 2020-01-09 2021-07-15 Saudi Arabian Oil Company Separation vessel and buoyant thermal energy transfer device for use therein

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2693880A (en) * 1952-01-21 1954-11-09 Otto B Schoenfeld Emulsion separator
US2834464A (en) * 1954-08-23 1958-05-13 Socony Mobil Oil Co Inc Method and apparatus for continuous liquid thermal diffusion
US4594155A (en) * 1982-10-07 1986-06-10 Conway Charles S Immiscible fluid separation apparatus
DE8809056U1 (en) * 1988-07-14 1988-10-06 Schroeder, Heinrich, Dipl.-Ing., 2819 Thedinghausen, De
US5244569A (en) * 1992-02-14 1993-09-14 Paul Di Amico Toxic liquid collector
WO2000045930A1 (en) * 1999-02-05 2000-08-10 Komistek Stephen M Inclined emulsion treater
US20080006304A1 (en) * 2006-07-10 2008-01-10 Mdk Innovations Inc. Flock tank
WO2021141655A1 (en) * 2020-01-09 2021-07-15 Saudi Arabian Oil Company Separation vessel and buoyant thermal energy transfer device for use therein
US11577182B2 (en) * 2020-01-09 2023-02-14 Saudi Arabian Oil Company Separation vessel and buoyant thermal energy transfer device for use therein

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