US1602190A - Method of dehydrating petroleum emulsions - Google Patents
Method of dehydrating petroleum emulsions Download PDFInfo
- Publication number
- US1602190A US1602190A US79095A US7909526A US1602190A US 1602190 A US1602190 A US 1602190A US 79095 A US79095 A US 79095A US 7909526 A US7909526 A US 7909526A US 1602190 A US1602190 A US 1602190A
- Authority
- US
- United States
- Prior art keywords
- gas
- oil
- well
- emulsifying agent
- delivered
- 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
Links
Images
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/34—Arrangements for separating materials produced by the well
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
Definitions
- Patented ct. 5, 1926 Patented ct. 5, 1926.
- Our invention relates to the art of pump ing oil wells and more particularly to the art of pumping wells by the use ofY a hydrocarbon gas or vapor.
- a gas into Vthe oil in the well, this gas forming ine bubbles which lighten the column of oil, thus allowing the natural rock pressure to force .the mixture of oil and gas upwardly to a point above the surface of the ground.
- emulsions are usually formed and these emulsions are often of lsuch a nature that they resist the ordinary methods of treatment. If the emulsion produced consists of extremely fine bubbles of gas or water, ⁇ the ordinary settling methods employed in separating emulsions are not s uflicient to cause separation and the mulsion so formed is often of such a nature that it cannoty be readily separated by the ordinary electrical or chemical treatment.
- Figure l' is. a diagrammatic assembly of the apparatus.
- Figure 2 is a vertical section of the atl omizer.
- 1 is a steel casing secured in an oil well and extending downwardly to a point near the bottom thereof
- 2 is a tubing suspended inside thecasing 1 the casing 1 being provided with a stuiing box 3 which p acker is provided, this packer making a t1ght jolnt between the casing 1 and the tubing 2 at a point in the well preferably just above the oil sands, a small opening 5 being l y charges into a gas and liquid separator l0, 1n which the gas and any entrained liquid are separated, the gas being delivered to a pipe 1l, the oil being delivered to suitable storage (not shown) through a pipe 12 and the water being delivered to a suitable drain (not shown) through a pipe 13.
- the gas and' liquid separator isV also well known in the art and its specific construction need not be described.
- a pump 2O is provided, this pump compressing the gas delivered through the pipe 11 to a desired degree and delivering it to a separator 30.
- the separator 30 the gasoline carried by the gas is separated and is delivered under' compression to suitable storage through a pipe 31. Any excess of dry gas, that is to say, gas from which the gasoline has been separated, may be delivered to suitable storage (not shown) through a pipe 32.
- a portlon of the dry gas is carried through a pipe 33 to an atomizer 40.
- This atomizer consists of a constricted tube 41 and a noz"zle 42 which projects thereinto.'
- a suitable de-emulsifying agent such for example as a soap solution, is delivered under pressure to the atomizer 40 through a pipe 43 having a valve 44.
- rllhe atomizer nozzle 42 and the constricted tube 41 are so construct-ed that the de-emulsifying agent which is preferably in liquid form is delivered in an extremelyfine state of suspension into the stream of dry gas passing through the tube 41.
- the dry gas containing the de-emulsiying agent in the form of a very finely divided mist -then asses through a pipe 45 and into theD interior of the casing 1- near the top thereof. This gas carrying the de-emulsifyingagent in mistlike form isyunder approximately the pressure produced in the pump 20.
- a y.Sure may Vamount to several hundred pounds per square inch so that the interior of the casing 1 outside the tubing 2 is full of gas under this pressure containing the de-emulsifying agent.
- This gas passes through the opening 5 into the interior of the tubing Q' and acts as the lifting agent, forming fine bubbles in the body of oil in the tubing and thereby decreasing the specific gravity of the oil column carried in the tubing 2 to such a degree that the natural rock press, sure of the well forces the mixed oil and gas column upwardly into the separator 10.
- a method of pumping an oil Well which comprises: introducing into the oil in the Wella gas containing a de-emulsifying agent.
- a method of pumping an ⁇ oil Well which comprises: introducing into the oil in the Well a gas containing a de-emulsifying agent in suspension.
- a method of pumping an oil Well which comprises: placing an eduction tube in the well, which eduction tube extends downwardly into the Oil in the Well; introducing a gas containing a de-emulsifying agent into said eduction tube below the oil level; delivering the oil from said eduction tube into a separator in which the gas and liquid are separated; compressing said gas to increase the pressure thereof; and introducing into said compressed gas a de-emulsifying agent, said compressed gas containing said deemulsifyingv agent then being delivered to said eduction tube.
- a method of pumping an oil Well which comprises: placing an eduction tube in the Well which eduction tube extends downwardly into the oil in the Well; introducing a gas containing a de ⁇ emulsifying agent into said eduction tube below the oil level; delivering the oil from said eduction tube into a separator in which the gas and liquid are separated; compressing said gas to increase the pressure thereof; separating from said compressed gas any liquid condensed therein; and introducing into said compressed gas a cle-emulsifying agent, said compressed gas containing said de-emulsifying agent then being delivered to said eduction tube.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Geology (AREA)
- Mining & Mineral Resources (AREA)
- Physics & Mathematics (AREA)
- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Fats And Perfumes (AREA)
Description
Patented ct. 5, 1926.
UNITED -STATES.
PATENT OFFICE.
HAROLD C. EDDY, OF LOS ANGELES, CALIFORNIA, AND GORDON B. HANSON, OF HOUS- TON, TEXAS, ASSIGNORS TO PETROLEUM RECTIFYING COMPANY OF CALIFORNIA, OF LOS ANGELES, CALIFORNIA, A. CORPORATION OF CALIFORNIA.
METHOD F DEHYDRATING PETROLEUM EMULSIONS.
Application led January 4, 1926. Serial No. 79,095.
Our invention relates to the art of pump ing oil wells and more particularly to the art of pumping wells by the use ofY a hydrocarbon gas or vapor. In the productionl of oil it is quite common to cause the oil to flow from the well by injecting a gas into Vthe oil in the well, this gas forming ine bubbles which lighten the column of oil, thus allowing the natural rock pressure to force .the mixture of oil and gas upwardly to a point above the surface of the ground.
. It is 'quite common to use air for this purpose, this method of causing oil to iiow being .known as the air lift method.
It is also quite common to use natural gas for this purpose, .and in many cases the well, itself produces sufficient gas for this purpose.
Where air or gas is used to pump a well in this manner, particularly .Where there is some water present, emulsions are usually formed and these emulsions are often of lsuch a nature that they resist the ordinary methods of treatment. If the emulsion produced consists of extremely fine bubbles of gas or water,` the ordinary settling methods employed in separating emulsions are not s uflicient to cause separation and the mulsion so formed is often of such a nature that it cannoty be readily separated by the ordinary electrical or chemical treatment.
It is an object of our invention to provide means in connectioh with theair or gas lift method of pumping wells which' will pre- 35, vent'the formation of emulsionsA which arel diicult to separate.
Further objects and advantages will be made evident hereinafter. 0n the drawings:
Figure l'is. a diagrammatic assembly of the apparatus.
Figure 2 is a vertical section of the atl omizer.
Referring to the drawings which show diagrammatically a novel assembly of well ,known apparatus adapted to carry on our process, 1 is a steel casing secured in an oil well and extending downwardly to a point near the bottom thereof, 2 is a tubing suspended inside thecasing 1 the casing 1 being provided with a stuiing box 3 which p acker is provided, this packer making a t1ght jolnt between the casing 1 and the tubing 2 at a point in the well preferably just above the oil sands, a small opening 5 being l y charges into a gas and liquid separator l0, 1n which the gas and any entrained liquid are separated, the gas being delivered to a pipe 1l, the oil being delivered to suitable storage (not shown) through a pipe 12 and the water being delivered to a suitable drain (not shown) through a pipe 13. The gas and' liquid separator isV also well known in the art and its specific construction need not be described.
A pump 2O is provided, this pump compressing the gas delivered through the pipe 11 to a desired degree and delivering it to a separator 30. In the separator 30 the gasoline carried by the gas is separated and is delivered under' compression to suitable storage through a pipe 31. Any excess of dry gas, that is to say, gas from which the gasoline has been separated, may be delivered to suitable storage (not shown) through a pipe 32. A portlon of the dry gas is carried through a pipe 33 to an atomizer 40. This atomizer consists of a constricted tube 41 and a noz"zle 42 which projects thereinto.'
A suitable de-emulsifying agent, such for example as a soap solution, is delivered under pressure to the atomizer 40 through a pipe 43 having a valve 44. rllhe atomizer nozzle 42 and the constricted tube 41 are so construct-ed that the de-emulsifying agent which is preferably in liquid form is delivered in an extremelyfine state of suspension into the stream of dry gas passing through the tube 41. The dry gas containing the de-emulsiying agent in the form of a very finely divided mist -then asses through a pipe 45 and into theD interior of the casing 1- near the top thereof. This gas carrying the de-emulsifyingagent in mistlike form isyunder approximately the pressure produced in the pump 20. This presmakes atight joint around the tubing 2. A y.Sure may Vamount to several hundred pounds per square inch so that the interior of the casing 1 outside the tubing 2 is full of gas under this pressure containing the de-emulsifying agent. This gas passes through the opening 5 into the interior of the tubing Q' and acts as the lifting agent, forming fine bubbles in the body of oil in the tubing and thereby decreasing the specific gravity of the oil column carried in the tubing 2 to such a degree that the natural rock press, sure of the well forces the mixed oil and gas column upwardly into the separator 10.
It is a well known fact that emulsions are readily broken by certain alkali or soap solutions. A very common agent used for this purpose is a solution of sodium oleate Which may be combined with small quantities of sodium resinate and sodium silicate. By injecting s uch an agent in the form of a ne mist or spray into the gas used in our method, We provide for a very fine division of the de-emulsifying agent and provide for its wide distribution through the body of the rising column of oil in the tubing 2. A very small amount of such de-emulsifying agentis sufficient to counteract the tendency of the oil to emulsify due to the injection of the gas bubbles thereinto.
We claim as our invention:
1. A method of pumping an oil Well which comprises: introducing into the oil in the Wella gas containing a de-emulsifying agent.
2. A method of pumping an `oil Well which comprises: introducing into the oil in the Well a gas containing a de-emulsifying agent in suspension.
3. A method of pumping an oil Well which comprises: placing an eduction tube in the well, which eduction tube extends downwardly into the Oil in the Well; introducing a gas containing a de-emulsifying agent into said eduction tube below the oil level; delivering the oil from said eduction tube into a separator in which the gas and liquid are separated; compressing said gas to increase the pressure thereof; and introducing into said compressed gas a de-emulsifying agent, said compressed gas containing said deemulsifyingv agent then being delivered to said eduction tube.
4;. A method of pumping an oil Well which comprises: placing an eduction tube in the Well which eduction tube extends downwardly into the oil in the Well; introducing a gas containing a de`emulsifying agent into said eduction tube below the oil level; delivering the oil from said eduction tube into a separator in which the gas and liquid are separated; compressing said gas to increase the pressure thereof; separating from said compressed gas any liquid condensed therein; and introducing into said compressed gas a cle-emulsifying agent, said compressed gas containing said de-emulsifying agent then being delivered to said eduction tube.
In testimony whereof, the saidnHAnoLD C. EDDY has hereunto set his hand at Los Angeles, California, this 15th day of December, 1925, and the said GORDON B; HAN- soN'has hereunto set his hand at Houston, Texas, this 23 day of December, 1925.
HAROLD o. EDDY. GORDON B. HANSON.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US79095A US1602190A (en) | 1926-01-04 | 1926-01-04 | Method of dehydrating petroleum emulsions |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US79095A US1602190A (en) | 1926-01-04 | 1926-01-04 | Method of dehydrating petroleum emulsions |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1602190A true US1602190A (en) | 1926-10-05 |
Family
ID=22148396
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US79095A Expired - Lifetime US1602190A (en) | 1926-01-04 | 1926-01-04 | Method of dehydrating petroleum emulsions |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1602190A (en) |
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2678305A (en) * | 1952-01-07 | 1954-05-11 | Juan F Villarreal | Method for breaking water and oil emulsions |
| US2793193A (en) * | 1955-11-25 | 1957-05-21 | Union Oil Co | Sludge treatment |
| US3096819A (en) * | 1959-05-22 | 1963-07-09 | Champion Chemicals Inc | Method and composition for preventing corrosion |
| US3566970A (en) * | 1969-02-13 | 1971-03-02 | Dresser Ind | Method of injecting treating liquids into well tubing |
| US3759324A (en) * | 1972-05-25 | 1973-09-18 | Kobe Inc | Cleaning apparatus for oil well production |
| US4323122A (en) * | 1980-06-02 | 1982-04-06 | Knopik Dwayne L | Process for recovering organic liquids from underground areas |
| US4347899A (en) * | 1980-12-19 | 1982-09-07 | Mobil Oil Corporation | Downhold injection of well-treating chemical during production by gas lift |
| US4376676A (en) * | 1981-10-19 | 1983-03-15 | Gill Carl L | In-line separator for crude oil |
| US4423779A (en) | 1981-11-04 | 1984-01-03 | Livingston Arnold M | Oil recovery system and process |
| US4892477A (en) * | 1987-09-30 | 1990-01-09 | Larry Zimmiond | Apparatus for flaring gas |
| US5343941A (en) * | 1992-12-03 | 1994-09-06 | Raybon Michael L | Apparatus for treating oil and gas wells |
| US5547021A (en) * | 1995-05-02 | 1996-08-20 | Raden; Dennis P. | Method and apparatus for fluid production from a wellbore |
| US5664911A (en) * | 1991-05-03 | 1997-09-09 | Iit Research Institute | Method and apparatus for in situ decontamination of a site contaminated with a volatile material |
| US5707214A (en) * | 1994-07-01 | 1998-01-13 | Fluid Flow Engineering Company | Nozzle-venturi gas lift flow control device and method for improving production rate, lift efficiency, and stability of gas lift wells |
| US5743717A (en) * | 1994-07-01 | 1998-04-28 | Fluid Flow Engineering Company | Nozzle-venturi gas lift flow control device |
-
1926
- 1926-01-04 US US79095A patent/US1602190A/en not_active Expired - Lifetime
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2678305A (en) * | 1952-01-07 | 1954-05-11 | Juan F Villarreal | Method for breaking water and oil emulsions |
| US2793193A (en) * | 1955-11-25 | 1957-05-21 | Union Oil Co | Sludge treatment |
| US3096819A (en) * | 1959-05-22 | 1963-07-09 | Champion Chemicals Inc | Method and composition for preventing corrosion |
| US3566970A (en) * | 1969-02-13 | 1971-03-02 | Dresser Ind | Method of injecting treating liquids into well tubing |
| US3759324A (en) * | 1972-05-25 | 1973-09-18 | Kobe Inc | Cleaning apparatus for oil well production |
| US3802501A (en) * | 1972-05-25 | 1974-04-09 | Kobe Inc | Cleaning apparatus for oil well production |
| US4323122A (en) * | 1980-06-02 | 1982-04-06 | Knopik Dwayne L | Process for recovering organic liquids from underground areas |
| US4347899A (en) * | 1980-12-19 | 1982-09-07 | Mobil Oil Corporation | Downhold injection of well-treating chemical during production by gas lift |
| US4376676A (en) * | 1981-10-19 | 1983-03-15 | Gill Carl L | In-line separator for crude oil |
| US4423779A (en) | 1981-11-04 | 1984-01-03 | Livingston Arnold M | Oil recovery system and process |
| US4892477A (en) * | 1987-09-30 | 1990-01-09 | Larry Zimmiond | Apparatus for flaring gas |
| US5664911A (en) * | 1991-05-03 | 1997-09-09 | Iit Research Institute | Method and apparatus for in situ decontamination of a site contaminated with a volatile material |
| US5343941A (en) * | 1992-12-03 | 1994-09-06 | Raybon Michael L | Apparatus for treating oil and gas wells |
| US5707214A (en) * | 1994-07-01 | 1998-01-13 | Fluid Flow Engineering Company | Nozzle-venturi gas lift flow control device and method for improving production rate, lift efficiency, and stability of gas lift wells |
| US5743717A (en) * | 1994-07-01 | 1998-04-28 | Fluid Flow Engineering Company | Nozzle-venturi gas lift flow control device |
| US5547021A (en) * | 1995-05-02 | 1996-08-20 | Raden; Dennis P. | Method and apparatus for fluid production from a wellbore |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US1602190A (en) | Method of dehydrating petroleum emulsions | |
| US2214064A (en) | Oil production | |
| US5547021A (en) | Method and apparatus for fluid production from a wellbore | |
| Chilingarian et al. | Surface operations in petroleum production, I | |
| US2652130A (en) | Gas-oil separator | |
| US2706531A (en) | Gas and multiple liquid separator apparatus | |
| US1674815A (en) | Art of removing oil from oil wells | |
| US3333638A (en) | Liquid disposal | |
| US1496090A (en) | Trapped outlet separator | |
| US2624410A (en) | Apparatus for secondary recovery in oil wells | |
| US2341359A (en) | Apparatus for producing oil wells which make water | |
| US3516490A (en) | Method and apparatus for producing an off-shore well | |
| US1499589A (en) | Method and apparatus for extracting oil from wells | |
| US1886886A (en) | Method of and apparatus for the recovery of matter from wells | |
| US3548939A (en) | Oil well production system | |
| US2713908A (en) | Apparatus for coating the interior of well pipes | |
| USRE21239E (en) | Method of recovering well fluids | |
| US2292796A (en) | Pumping system | |
| US2777399A (en) | Pneumatic pumping system | |
| US2238701A (en) | Method of recovering oil from oil and gas bearing sands | |
| US1437721A (en) | Automatic gas separator for oil wells | |
| US2764102A (en) | Constriction gas anchor | |
| US1554444A (en) | System for the recovery of mineral oils | |
| US1760420A (en) | Oil recovery method and apparatus | |
| US1310615A (en) | Method of and system for pumping |