Patent US3723845A successfully refreshed from Google Patents.
Patent US4482459A successfully refreshed from Google Patents.
US4482459A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Continuous process for the reclamation of waste drilling fluids
Assignee: Newpark Waste Treatment Systems Inc
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Filing: 1983-04-27
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Granted: 1984-11-13
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Expires: 2003-04-27
Abstract
Abstract A continuous process for the reclamation of a slurry of waste drilling mud fluids and water normally resulting from drilling operations. The process comprises the steps of conducting the drilling mud slurry to a slurry surge tank for liquid solid separation by chemical and physical methods. The mud slurry is subjected to a primary solids separation unit after pH adjustment is used to initiate coagulation and an organic flocculant is added to aid flocculation of the solids. The water is then subjected to a secondary solids removal, and the solids recovered are reintroduced in the primary solids separation unit. Thereafter the water obtained from the secondary solids removal is then subjected to a chemical oxygen demand reduction unit having a carbon adsorption unit or reverse osmosis membrane units therein to remove organic matter or dissolved solids to produce water meeting environmental discharge requirements. The solids removed from the primary solids separation unit are converted to a cake meeting leachate requirements for other beneficial use.
Inventors
- 👤 Carolyn Shiver
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 15:48
CPC Classifications
E; E21; E21B; E21B41/00; E21B41/005; B; B01; B01D; B01D36/00; B01D61/00; B01D61/02; B01D61/025; C; C02; C02F; C02F9/00; E21B21/00; E21B21/06; B01D21/00; B01D21/02; B01D21/26; B01D21/262; B01D2311/00; B01D2311/02; C02F1/00; C02F1/001; C02F1/004; C02F1/24; C02F1/28; C02F1/283; C02F1/38; C02F1/385; C02F1/40; C02F1/44; C02F1/441; C02F1/52; C02F1/5236; C02F1/54; C02F1/56; C02F1/66; C02F1/72; C02F1/74; C02F11/00; C02F11/12; C02F11/121; C02F11/127; C02F11/14; C02F11/143; C02F11/147; C02F2001/007; C02F2103/00; C02F2103/10; C02F5/00
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
222 words
The method of rendering a waste drilling fluid slurry from oil wells containing cuttings, formation fluid solids and liquids and the like, safe for environmental discharge both in a liquid and solid cake state comprising the steps of (a) conducting the uphole drilling fluids to a continuous flow process having a slurry surge tank for chemical conditioning by addition of an inorganic acidic coagulant permitting settling and thickening, (b) subjecting the thickened mud slurry under flow from step (a) thereafter to a primary solids separation unit where an organic flocculant of the group of polyacrylamides is added to aid flocculation of the solids and from which solids of less than 50% moisture content and water are produced, (c) subjecting the water from (b) to a secondary solids removal unit, chemically conditioning and reintroducing the solids recovered back to the primary solids separation unit, (d) subjecting the water obtained from the secondary solids removal step (a) to a chemical oxygen demand reduction unit having a carbon adsorption unit for removal of organic substances or a reverse osmosis unit for removal of organic substances and dissolved solids including chlorine compounds to meet environmental discharge requirements, (e) removing the treated primary solids from step (b) consisting of an environmentally compatible cake meeting environmental leachate requirements for disposal as landfill on or off the drill site.
Claim 2
Independent Claim
222 words
The method of rendering a waste drilling fluid slurry from oil wells containing cuttings, formation fluid solids and liquids and the like, safe for environmental discharge both in a liquid and solid cake state comprising the steps of (a) conducting the uphole drilling fluids to a continuous flow process having a slurry surge tank for chemical conditioning by addition of an inorganic acidic coagulant permitting settling and thickening, (b) subjecting the thickened mud slurry under flow from step (a) thereafter to a primary solids separation unit where an organic flocculant of the group of polyacrylamides is added to aid flocculation of the solids and from which solids of less than 50% moisture content and water are produced, (c) subjecting the water from (b) to a secondary solids removal unit, chemically conditioning and reintroducing the solids recovered back to the primary solids separation unit, (d) subjecting the water obtained from the secondary solids removal step (a) to a chemical oxygen demand reduction unit having a carbon adsorption unit for removal of organic substances or a reverse osmosis unit for removal of organic substances and dissolved solids including chlorine compounds to meet environmental discharge requirements, (e) removing the treated primary solids from step (b) consisting of an environmentally compatible cake meeting environmental leachate requirements for disposal as landfill on or off the drill site.
Claim 3
Dependent Claim
18 words
The process of claim 1, wherein the primary solids separation unit of step (c) is a decanting centrifuge.
Claim 4
Dependent Claim
21 words
The process of claim 1, wherein the primary solids separation unit of step (c) is a positive vacuum filtration thickener unit.
Claim 5
Dependent Claim
44 words
The process of claim 1, wherein the secondary solids separation unit of step (d) conducts a liquid suspension through separate parallel settling spaces defined by inclined surfaces wherein the clarified liquid flows upward of the surfaces, and the solids sink down the inclined surfaces.
Claim 6
Dependent Claim
35 words
The process of claim 1, wherein the secondary solids separation unit of step (d) is a flotation unit wherein the solids are floated to the surface on extremely small bubbles and skimmed from the surface.
Claim 7
Dependent Claim
49 words
The process of claim 1 wherein the pH of the normally alkaline drilling fluids is reduced to less than 4.5 by the addition of an inorganic acidic coagulant of the group of aluminum sulfate, phosphoric acid or nitric acid, the quantity of coagulant being dependant upon monitoring the pH.
Claim 8
Dependent Claim
45 words
The process of claim 1 wherein the chemical conditioning consists of reducing pH of fluids to 4.5 with use of an inorganic acid coagulant and raising the pH to 6.5 with use of an inorganic basic coagulant of aluminum sulfate and an organic polyacrylamide flocculant.
Claim 9
Dependent Claim
77 words
The process of claim 1, wherein the organic flocculant is a polyacrylamide introduced after the chemical conditioning by addition of an acidic inorganic coagulant of aluminum sulfate in steps 1(a) and 1(d) and a basic inorganic coagulant of sodium aluminate in step 1(d) to the drilling fluids the proportions of each coagulant being that amount necessary to reduce the fluids to a pH of 4.5 and then to raise the pH to 6.5 respectively for environmental discharge.
Claim 10
Dependent Claim
30 words
The process of claim 9 wherein an acidic inorganic coagulant aluminum sulfate is added in an amount necessary to reduce the water with solids content to a pH of 4.5.
Claim 11
Dependent Claim
25 words
The process of claim 8 wherein the pH is raised to a range of 6.0 to 9.0 by addition of a quantity of sodium aluminate.
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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) | 1987-11-13 | 1988-05-14 | 1988-11-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-11-13 | 1992-05-14 | 1992-11-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-11-13 | 1996-05-14 | 1996-11-13 | $7700.00 | Window Closed / Lapsed |