US5246592A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method and apparatus for recovering oil from the surface of a body of water
Assignee: Amistco Separation Products Inc
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Filing: 1992-05-14
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Granted: 1993-09-21
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Expires: 2012-05-14
Abstract
Abstract An apparatus for recovering oil from an oil spill on the surface of a body of water includes a skimmer unit for recovering an oil-water mixture from the surface of the body of water, a three stage coalescer unit for separating the oil in the oil-water mixture from the water therein and a solvent injection assembly for injecting solvent into the coalescer unit after the first and second stages in order to reduce the viscosity of the oil entering the second and third stages. The first, second, and third stages of the coalescer unit comprise interceptors having a surface area ratios between 27 and 65 ft 2 /ft 3 ; 65 ft 2 /ft 3 and 2500 ft 2 /ft 3 ; and 500 ft 2 /ft 3 and 4200 ft 2 /ft 3 , respectively.
Inventors
- 👤 Richard W. Schweizer
- 👤 Kantilal P. Patel
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 19:37
CPC Classifications
E; E02; E02B; E02B15/00; E02B15/04; E02B15/045; B; B01; B01D; B01D17/00; B01D17/02; B01D17/0208; B01D17/0211; B01D17/04; B01D17/045; B01D17/047; Y; Y02; Y02A; Y02A20/00; Y02A20/20; Y02A20/204; Y10; Y10S; Y10S210/00; Y10S210/05; Y10S210/918; Y10S210/922; Y10S210/923
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
228 words
A method of recovering a hydrophobic hydrocarbon oil from the surface of a body of water, said body of water having a water temperature, said oil having a specific gravity which is less than the specific gravity of the water in said body of water and a viscosity which is greater than approximately 80 centipoise at said water temperature, said method comprising the steps of: a. continuously withdrawing a feed oil-water mixture from the surface of said body of water; b. continuously passing said feed oil-water mixture through a first stage oil-water coalescer to separate said feed oil-water mixture into a first oil outlet stream and a first reduced oil-water mixture stream, said first stage oil-water coalescer comprising an interceptor having a surface area ratio between approximately 27 ft 2 /ft 3 and 65 ft 2 /ft 3 ; c. continuously adjusting the viscosity of the oil in said first reduced oil-water mixture stream to a level below approximately 80 centipoise to form an adjusted first reduced oil-water mixture stream; and d. continuously passing said adjusted first reduced oil-water mixture stream through a second stage oil-water coalescer to separate said adjusted first reduced oil-water mixture stream into a second oil outlet stream and a second reduced oil-water mixture stream said second stage coalescer having a surface area ratio of at least approximately 65 ft 2 /ft 3 .
Claim 2
Independent Claim
228 words
A method of recovering a hydrophobic hydrocarbon oil from the surface of a body of water, said body of water having a water temperature, said oil having a specific gravity which is less than the specific gravity of the water in said body of water and a viscosity which is greater than approximately 80 centipoise at said water temperature, said method comprising the steps of: a. continuously withdrawing a feed oil-water mixture from the surface of said body of water; b. continuously passing said feed oil-water mixture through a first stage oil-water coalescer to separate said feed oil-water mixture into a first oil outlet stream and a first reduced oil-water mixture stream, said first stage oil-water coalescer comprising an interceptor having a surface area ratio between approximately 27 ft 2 /ft 3 and 65 ft 2 /ft 3 ; c. continuously adjusting the viscosity of the oil in said first reduced oil-water mixture stream to a level below approximately 80 centipoise to form an adjusted first reduced oil-water mixture stream; and d. continuously passing said adjusted first reduced oil-water mixture stream through a second stage oil-water coalescer to separate said adjusted first reduced oil-water mixture stream into a second oil outlet stream and a second reduced oil-water mixture stream said second stage coalescer having a surface area ratio of at least approximately 65 ft 2 /ft 3 .
Claim 3
Dependent Claim
76 words
The method of claim 1, further comprising the steps of continuously maintaining the viscosity of the oil in said second reduced oil-water mixture stream at a level below approximately 80 centipoise to form an adjusted second reduced oil-water mixture stream and continuously passing said adjusted second reduced oil-water mixture stream through a third stage oil-water coalescer to separate said adjusted second reduced oil-water mixture stream into a third oil outlet stream and a water outlet stream.
Claim 4
Dependent Claim
133 words
In the method of claim 1, said adjusting step comprising continuously adding a hydrophobic hydrocarbon solvent to at least a portion of said first reduced oil-water mixture stream to form said adjusted first reduced oil-water mixture stream, said solvent having a viscosity of less than approximately 80 centipoise at said water temperature and a specific gravity which is less than the specific gravity of the water in said first reduced oil-water mixture stream, said solvent being added at a rate sufficient to reduce the viscosity of the oil in said portion of said first reduced oil-water mixture stream to below approximately 80 centipoise, said continuously passing step further comprising separating the oil and solvent in said adjusted first reduced oil-water mixture stream from the water in said adjusted first reduced oil-water mixture stream.
Claim 5
Dependent Claim
33 words
In the method of claim 1, said second stage oil-water coalescer comprising an interceptor having a surface area ratio between approximately 65 ft 2 /ft 3 and 2500 ft 2 /ft 3 .
Claim 6
Dependent Claim
60 words
In the method of claim 2, said second stage oil-water coalescer comprising an interceptor having a surface area ratio between approximately 65 ft 2 /ft 3 and 2500 ft 2 /ft 3 , said third stage oil-water coalescer comprising an interceptor having a surface area ratio between approximately 500 ft 2 /ft 3 and 4200 ft 2 /ft 3 .
Claim 7
Dependent Claim
17 words
In the method of claim 1, said first stage oil-water coalescer comprising a corrugated plate vane-type coalescer.
Claim 8
Independent Claim
228 words
An apparatus for recovering a hydrophobic hydrocarbon oil from a source of oil on the surface of a body of water, said body of water having a water temperature, said oil having a specific gravity which is less than the specific gravity of the water in said body of water and a viscosity which is greater than approximately 80 centipoise at said water temperature, said apparatus comprising: a. means for continuously withdrawing a feed oil-water mixture from the surface of said body of water; b. first stage coalescer means for receiving said feed oil-water mixture and separating said feed oil-water mixture into a first oil outlet stream and a first reduced oil-water mixture stream, said first stage coalescer means comprising an interceptor having a surface area ratio between approximately 27 ft 2 /ft 3 and 65 ft 2 /ft 3 ; c. means for adjusting the viscosity of the oil in said first reduced oil-water mixture stream to a level below approximately 80 centipoise to form an adjusted first reduced oil-water mixture; d. second stage coalescer means for receiving said adjusted first reduced oil-water mixture stream and for separating said adjusted first reduced oil-water mixture stream into a second oil outlet stream and a second reduced oil-water mixture stream said second stage coalescer having a surface area ratio of at least approximately 65 ft 2 /ft 3 .
Claim 9
Independent Claim
228 words
An apparatus for recovering a hydrophobic hydrocarbon oil from a source of oil on the surface of a body of water, said body of water having a water temperature, said oil having a specific gravity which is less than the specific gravity of the water in said body of water and a viscosity which is greater than approximately 80 centipoise at said water temperature, said apparatus comprising: a. means for continuously withdrawing a feed oil-water mixture from the surface of said body of water; b. first stage coalescer means for receiving said feed oil-water mixture and separating said feed oil-water mixture into a first oil outlet stream and a first reduced oil-water mixture stream, said first stage coalescer means comprising an interceptor having a surface area ratio between approximately 27 ft 2 /ft 3 and 65 ft 2 /ft 3 ; c. means for adjusting the viscosity of the oil in said first reduced oil-water mixture stream to a level below approximately 80 centipoise to form an adjusted first reduced oil-water mixture; d. second stage coalescer means for receiving said adjusted first reduced oil-water mixture stream and for separating said adjusted first reduced oil-water mixture stream into a second oil outlet stream and a second reduced oil-water mixture stream said second stage coalescer having a surface area ratio of at least approximately 65 ft 2 /ft 3 .
Claim 10
Dependent Claim
99 words
In the apparatus of claim 7, said means for adjusting comprising means for adding hydrophobic hydrocarbon solvent from a source of said solvent to said first reduced oil-water mixture stream, said solvent having a viscosity of less than approximately 80 centipoise at said water temperature and a specific gravity which is less than the specific gravity of the water in said feed oil-water mixture, said means for adding said solvent being operative for adding said solvent at a rate sufficient to reduce the viscosity of the oil in said first reduced oil-water mixture stream to below approximately 80 centipoise.
Claim 11
Dependent Claim
45 words
The apparatus of claim 7, further comprising third stage coalescer means for receiving said second reduced oil-water mixture stream from said second stage coalescer means and for separating said second reduced oil-water mixture stream into a third oil outlet stream and a water outlet stream.
Claim 12
Dependent Claim
29 words
The apparatus of claim 9, further comprising means for adjusting the viscosity of the oil in said second reduced oil-water mixture stream to a level below approximately 80 centipoise.
Claim 13
Dependent Claim
29 words
In the apparatus of claim 7, said second stage coalescer having a surface area ratio between approximately 65 ft 2 /ft 3 and 2500 ft 2 /ft 3 .
Claim 14
Dependent Claim
29 words
In the apparatus of claim 9, said third stage coalescer having a surface area ratio between approximately 500 ft 2 /ft 3 and 4200 ft 2 /ft 3 .
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1996-09-20 | 1997-03-22 | 1997-09-21 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2000-09-20 | 2001-03-22 | 2001-09-21 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2004-09-20 | 2005-03-22 | 2005-09-21 | $7700.00 | Window Closed / Lapsed |