US4725362A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Treatment techniques for drill fluids, cuttings and other oil field wastes
Assignee: Individual
•
Filing: 1985-11-18
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Granted: 1988-02-16
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Expires: 2005-11-18
Abstract
Abstract Method and apparatus for treatment of oilfield wastes, so that the wastes may be disposed of without harm to the environment or may be recovered as valuable products, wherein the wastes are pretreated to enhance separation of solid materials, the solid materials being dried and incinerated to a char solids condition, the char solids and the heating gases being cooled by heat exchange to provide hot air for combustion in the dryer-incinerator, thereby saving heating fuel cost, the gases being scrubbed to remove contaminants, and the condensed water-hydrocarbon phases being separated for reuse or for further treatment for recovery.
Inventors
- 👤 John W. Dugat
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 14:44
CPC Classifications
F; F23; F23G; F23G7/00; F23G7/05; B; B01; B01D; B01D37/00; B01D37/03; E; E21; E21B; E21B21/00; E21B21/06; E21B21/063; E21B21/065; E21B21/066; E21B41/00; E21B41/005
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
221 words
Process for treatment of oilfield wastes for disposal or recovery, the oilfield wastes including one or more types of drilling mud, drill cuttings and soil solids, petroleum, diesel and other oils, salts, and water, comprising separating the liquid components of said oilfield wastes from the solid components thereof by filtration to produce a filtrate, treating said filtrate with acid to reduce its pH and with a flocculating agent to flocculate solids therefrom and filtering said flocculated solids from the remaining liquid and combining same with said solid components, heating and incinerating said solid components at a temperature between about 200° F. (93° K.) and about 1500° F. (816° K.) with hot gases to produce char solids and flue gas containing materials vaporized from said solid components, cooling said char solids to a temperature between about 190° F. (88° K.) and about 350° F. (177° K.) by heat exchange with air to produce heated combustion air, cooling said flue gas to a temperature between about 200° F. (93° K.) and about 700° F. (371° K.) by heat exchange with air to produce condensed materials and additional heated combustion air, burning a fuel with said heated combustion air and said additional heated combustion air to produce said hot gases, and recovering said cooled char solids and said condensed materials for disposal or use.
Claim 2
Dependent Claim
221 words
Process for treatment of oilfield wastes for disposal or recovery, the oilfield wastes including one or more types of drilling mud, drill cuttings and soil solids, petroleum, diesel and other oils, salts, and water, comprising separating the liquid components of said oilfield wastes from the solid components thereof by filtration to produce a filtrate, treating said filtrate with acid to reduce its pH and with a flocculating agent to flocculate solids therefrom and filtering said flocculated solids from the remaining liquid and combining same with said solid components, heating and incinerating said solid components at a temperature between about 200° F. (93° K.) and about 1500° F. (816° K.) with hot gases to produce char solids and flue gas containing materials vaporized from said solid components, cooling said char solids to a temperature between about 190° F. (88° K.) and about 350° F. (177° K.) by heat exchange with air to produce heated combustion air, cooling said flue gas to a temperature between about 200° F. (93° K.) and about 700° F. (371° K.) by heat exchange with air to produce condensed materials and additional heated combustion air, burning a fuel with said heated combustion air and said additional heated combustion air to produce said hot gases, and recovering said cooled char solids and said condensed materials for disposal or use.
Claim 3
Dependent Claim
33 words
Process according to claim 1, including centrifuging said remaining liquid to remove additional solids therefrom, and combining said additional solids with said solid components and said flocculated solids for said heating and incineration.
Claim 4
Dependent Claim
26 words
Process according to claim 1, including scrubbing said cooled flue gas with an alkaline solution and burning the scrubbed gas to remove any remaining hydrocarbons therefrom.
Claim 5
Dependent Claim
32 words
Process according to claim 1, said flue gases being further cooled by additional heat exchage with air to a temperature between about 95° F. (35° K.) and about 200° F. (93° K.).
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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) | 1991-02-15 | 1991-08-17 | 1992-02-16 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-02-15 | 1995-08-17 | 1996-02-16 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-02-15 | 1999-08-17 | 2000-02-16 | $7700.00 | Window Closed / Lapsed |