US1627072A - Process of treating impure crude oil - Google Patents
Process of treating impure crude oil Download PDFInfo
- Publication number
- US1627072A US1627072A US688633A US68863324A US1627072A US 1627072 A US1627072 A US 1627072A US 688633 A US688633 A US 688633A US 68863324 A US68863324 A US 68863324A US 1627072 A US1627072 A US 1627072A
- Authority
- US
- United States
- Prior art keywords
- oil
- crude oil
- treating
- tank
- treating impure
- 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
- 238000000034 method Methods 0.000 title description 11
- 239000010779 crude oil Substances 0.000 title description 4
- 239000003921 oil Substances 0.000 description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- 239000012535 impurity Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 239000000839 emulsion Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- 238000013019 agitation Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 102000007469 Actins Human genes 0.000 description 1
- 108010085238 Actins Proteins 0.000 description 1
- 241000239290 Araneae Species 0.000 description 1
- 241000226211 Salminus brasiliensis Species 0.000 description 1
- 230000002844 continuous effect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 230000013707 sensory perception of sound Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Images
Classifications
-
- 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
Definitions
- My invention relates to a process of treating petrolcun'i oil to free it of impurities and break up emulsions of such oil with water, basic sediincn't and other objectionable matter.
- Another object is to clean the oil of its impurities largely through agitation and settling under heat without the loss of the ligl'itcr distillatcs through evaporation in a simple and economical manner.
- Fig. 1 is a central longitudinal section through an installation employing my invention
- Fig. 2 is a transverse section through-my propeller wheel.
- Like numerals of reference are employed to designate like parts in all the views.
- one side of the bottom is a chamber 3 boxed oil from the rest of the tank but having a perforated top 4. This forms a super-heater from which water is drawn to mix with the oil to be treated through an outlet pipe The steam pipes passing through this chamber maintain the water therein at high temperature.
- the oil to be treated I desire to thorough-v ly mix in atomized form with a spray of hot water. I do this .by spraying the oil with hot water drawn from the pipe 5 into closedchamber 6, mountedat 7 onthe arched upper end 8 of the tank.
- the two liquids are pumped in under pressure through two inclined nozzles 9 and 10, the nozzle 10 being connected with a sourcc of supply of oilunder pressure and the pipe 5 taking hot water from the coil 2 undccthe action of the pump shown in the drawing.
- a propeller wheel ll mounted on a vertical stub shaft 12 having hearings in the frame work of the housing.
- the blades or vanps 13 of the propeller are radial but have their outer ends curved rearwardly so as to better receive the impulse of the jets of liquid from the spray nozzles. thus causing the rotation of the propeller.
- crown gear wheel 14 On the shaft 12 below the pro eller is a. crown gear wheel 14:, positione with a smaller gear 15,-upon a shaft 16 em tending downwardly into the treating tank and baring a bearing at 17, in a spider 18 at the lower end of a cylindrical tube or agitating pipe 20.
- This tube is secured to the upper end 8 of the tank and extends to a point immediately above the steain'coils 2. The lower end is open and the fluid discharged downwardly will strike a horizontal ballle 21 below the outlet and secured to the tube by connecting strips 22.
- agitating members comprising longitudinal Paddles or blades 23 at the upper end. Below these blades are radial agitating vanes to mesh.
- a plurality of horizontal perforated battles 25 to assist in the separating of the water from the oil and actin to divide said tank into a plurality of vertically arranged settling chambers.
- oil and hot water are sprayed under pressure against the blades of the propeller 11.
- the nozzles are inclined so that the sprays will be intimately mixed and the oil acted upon by the hot water.
- The. mixture ofoil and water will be drawn down into the tube to where it will be further agitated and broken up by the blades and driven forcibly downward by the blades 24- and 19.
- the agitation of the liquids by the apparatus in the casing 6 and tube 20 assist in breaking up the particles of impurities in the oil whereby they are enabled to settle out; thereafter.
- the mixture issues from the tube 20 against the plate 21 and is deflected up away from the steam pipes and through the perforations in the baffles 25. This serves vto retard the flow and breaks up the bubbles which may form and allows the water and sediment to settle out.
- This oil which rises to the top will be free of emulsion and may be drawn off through an outlet pipe 26 to a storage tank 27. It will be noted that this process can be made continuous, it being only necessary to clear the treating tank of settlings at intervals through outlet 28. The employment of the suction automatically produced in the operation of the machines makes the process rapid and effective.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Mechanical Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Fats And Perfumes (AREA)
Description
W J. F. WRIGHT PROCESS OF TREATING IMPURE CRUDE OIL Filed Jan. 26. '1924 Wu F sm 0030+;
Patented May 3, 1927.
iii-airs JOHN F. WRIGHT, OF EL DORADO, ARKANSAS.
PROCESS OF TREATING IMPURE CRUDE OIL.
Application filed January 26, 1924. Serial No. 688,633.
My invention relates to a process of treating petrolcun'i oil to free it of impurities and break up emulsions of such oil with water, basic sediincn't and other objectionable matter.
It is an object of my invention to pro vide a method of treating impure crude oil whereby it may be cleaned of impurities without. the use of chemicals.
Another object is to clean the oil of its impurities largely through agitation and settling under heat without the loss of the ligl'itcr distillatcs through evaporation in a simple and economical manner.
It is now common to cause the separation of oil and its emulsions of oil and basic sediment by methods including the use of heat and chemicals through the use of costly apparatus or by electrical dehydration, centrifugal machines and similar processes involving a costly installation and expensive upkeep. The process devised by me is intended to be simple economical and con tinuous.
Referring to the drawing herewith wherein a preferrtwl embodiment of my invention is disclosed, Fig. 1 is a central longitudinal section through an installation employing my invention; Fig. 2 is a transverse section through-my propeller wheel. Like numerals of reference are employed to designate like parts in all the views.
In carrying out my invention I employ a large treating tank 1 having in the bottom of the same a. series of steam coils 2 tending to heat the contents of the tank. At
one side of the bottom is a chamber 3 boxed oil from the rest of the tank but having a perforated top 4. This forms a super-heater from which water is drawn to mix with the oil to be treated through an outlet pipe The steam pipes passing through this chamber maintain the water therein at high temperature.
The oil to be treated, I desire to thorough-v ly mix in atomized form with a spray of hot water. I do this .by spraying the oil with hot water drawn from the pipe 5 into closedchamber 6, mountedat 7 onthe arched upper end 8 of the tank. The two liquids are pumped in under pressure through two inclined nozzles 9 and 10, the nozzle 10 being connected with a sourcc of supply of oilunder pressure and the pipe 5 taking hot water from the coil 2 undccthe action of the pump shown in the drawing.
Within the chamber is a propeller wheel ll mounted on a vertical stub shaft 12 having hearings in the frame work of the housing. The blades or vanps 13 of the propeller are radial but have their outer ends curved rearwardly so as to better receive the impulse of the jets of liquid from the spray nozzles. thus causing the rotation of the propeller.
On the shaft 12 below the pro eller is a. crown gear wheel 14:, positione with a smaller gear 15,-upon a shaft 16 em tending downwardly into the treating tank and baring a bearing at 17, in a spider 18 at the lower end of a cylindrical tube or agitating pipe 20. This tube is secured to the upper end 8 of the tank and extends to a point immediately above the steain'coils 2. The lower end is open and the fluid discharged downwardly will strike a horizontal ballle 21 below the outlet and secured to the tube by connecting strips 22.
Mounted upon the shaft 16 are a series of agitating members comprising longitudinal Paddles or blades 23 at the upper end. Below these blades are radial agitating vanes to mesh.
2-4; curved to imparta downward drive upon the liquid. Below these blades is a spiral or screw blade 19, also adapted to impart a downward motion to the liquid during rotation of the shaft.
Within the tank and fitting about the tube 20 are a plurality of horizontal perforated battles 25 to assist in the separating of the water from the oil and actin to divide said tank into a plurality of vertically arranged settling chambers.
In the operation of the device, oil and hot water are sprayed under pressure against the blades of the propeller 11. The nozzles are inclined so that the sprays will be intimately mixed and the oil acted upon by the hot water. The. mixture ofoil and water will be drawn down into the tube to where it will be further agitated and broken up by the blades and driven forcibly downward by the blades 24- and 19. The agitation of the liquids by the apparatus in the casing 6 and tube 20 assist in breaking up the particles of impurities in the oil whereby they are enabled to settle out; thereafter.
The mixture issues from the tube 20 against the plate 21 and is deflected up away from the steam pipes and through the perforations in the baffles 25. This serves vto retard the flow and breaks up the bubbles which may form and allows the water and sediment to settle out.
This oil which rises to the top will be free of emulsion and may be drawn off through an outlet pipe 26 to a storage tank 27. It will be noted that this process can be made continuous, it being only necessary to clear the treating tank of settlings at intervals through outlet 28. The employment of the suction automatically produced in the operation of the machines makes the process rapid and effective.
Having thus described myinvention, what I claim as new; and desire to protect by Letters'Patent is:
1. The process of treating impure petroleum to relieve it of its impurities comprising spraying and atomizing the impure oil against a rotatable member, spraying hot water into contact with said atomized oil, 20
JOHN .F. WRIGHT.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US688633A US1627072A (en) | 1924-01-26 | 1924-01-26 | Process of treating impure crude oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US688633A US1627072A (en) | 1924-01-26 | 1924-01-26 | Process of treating impure crude oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1627072A true US1627072A (en) | 1927-05-03 |
Family
ID=24765147
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US688633A Expired - Lifetime US1627072A (en) | 1924-01-26 | 1924-01-26 | Process of treating impure crude oil |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1627072A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2521859A (en) * | 1945-01-11 | 1950-09-12 | Parkersburg Rig & Reel Co | Oil emulsion treater |
-
1924
- 1924-01-26 US US688633A patent/US1627072A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2521859A (en) * | 1945-01-11 | 1950-09-12 | Parkersburg Rig & Reel Co | Oil emulsion treater |
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