US2004209781A1PendingUtilityA1
Method to recover brine from drilling fluids
Priority: Apr 15, 2003Filed: Apr 14, 2004Published: Oct 21, 2004
Est. expiryApr 15, 2023(expired)· nominal 20-yr term from priority
Inventors:Michael Harris
B01D 21/0012E21B 21/065
42
PatentIndex Score
0
Cited by
0
References
0
Claims
Abstract
Processes to recover brine from drilling fluids and other fluids is described. One process involves filtering drilling fluids or other well servicing fluids using a rotary vacuum filter to recover at least a portion of the brine in the drilling fluid. Well servicing fluids, including drilling fluids, containing recycled brine are further described.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . A method to recover brine from a drilling fluid or other well servicing fluid comprising filtering said fluid with a rotary vacuum filter to recover at least a portion of said brine in said fluid, wherein said fluid is treated with a filtering aid.
2 . The method of claim 1 , wherein said rotary vacuum filter is a drum filter.
3 . The method of claim 1 , wherein said rotary vacuum filter is a disc filter.
4 . The method of claim 1 , wherein said rotary vacuum filter is a horizontal belt filter.
5 . The method of claim 1 , wherein said rotary vacuum filter is a horizontal scroll discharge.
6 . The method of claim 1 , wherein said rotary vacuum filter is a horizontal tipping pan.
7 . The method of claim 1 , wherein a filter cloth is present on said filter.
8 . The method of claim 2 , wherein a filter cloth is present on said drum filter.
9 . The method of claim 8 , wherein said filter cloth is polypropylene.
10 . The method of claim 8 , wherein said filter cloth has a pore size of from about 75 microns to about 90 microns.
11 . The method of claim 7 , wherein a precoat filter media layer is present on said filter cloth.
12 . The method of claim 8 , wherein a precoat filter media layer is present on said filter cloth.
13 . The method of claim 12 , wherein said precoat filter media layer is from about 1 cm thick to about 15 cm thick.
14 . The method of claim 2 , wherein a precoat filter media layer is present on said drum filter.
15 . The method of claim 12 , wherein said precoat filter media layer comprises diatomaceous earth, perlite, cellulose, or combinations thereof.
16 . The method of claim 2 , wherein said drum filter is rotated during said process such that said drum filter is partially submerged in said drilling fluid.
17 . The method of claim 12 , wherein during filtering, solids present in said drilling fluid become present on the surface of the precoat filter media layer, and said solids are removed to expose a fresh surface of the filter media layer.
18 . The method of claim 17 , wherein said solids are removed with a knife blade.
19 . The method of claim 18 , wherein said knife blade continuously removes said solids.
20 . The method of claim 18 , wherein said knife blades continuously removes said solids, and said knife blade moves at a rate of from about 0.005 mm to about 100 mm per hour.
21 . The method of claim 1 , wherein said drilling fluid is heated above ambient temperature prior to and/or during said filtering.
22 . The method of claim 2 , wherein said drilling fluid is heated above ambient temperature prior to and/or during said filtering.
23 . The method of claim 2 , wherein said drilling fluid is heated to a temperature of at least about 50° C.
24 . The method of claim 2 , wherein said drilling fluid is heated to a temperature of from about 20° C. to about 180° C.
25 . A method to purify brine in a brine containing solution comprising filtering said brine containing solution with a rotary vacuum filter to recover at least a portion of said brine having a higher purity than the brine present in the starting brine containing solution, wherein said brine containing solution is treated with a filtering aid.
26 . The method of claim 25 , wherein said rotary vacuum filter is a drum filter.
27 . The method of claim 1 , wherein said filtering aid comprises at least one alkali metal hydroxide or polyelectrolyte or both.
28 . The method of claim 2 , wherein said filtering aid comprises at least one alkali metal hydroxide or polyelectrolyte or both.
29 . The method of claim 1 , wherein said filtering aid comprises sodium hydroxide or potassium hydroxide or both.
30 . The method of claim 2 , wherein said filtering aid comprises sodium hydroxide or potassium hydroxide or both.
31 . The method of claim 2 , wherein said polyelectrolyte comprises iron salt, aluminum salt, cationic polymer flocculant, anonic polymer flocculant, or combinations thereof.
32 . The method of claim 2 , wherein said filtering aid is present in an amount of from about 0.1 kiloliter to about 35 kiloliters per m 3 of drilling fluid.
33 . The method of claim 16 , wherein said drum filter is rotated at a speed of from about 0.05 to about 5 rpm.
34 . The method of claim 14 , wherein a vacuum is applied to the inside of the drum filter to draw said drilling fluid through said precoat filter media, wherein said brine is separated from said drilling fluid.
35 . The method of claim 14 , wherein a vacuum is applied to the inside of a drum filter to draw said drilling fluid through said precoat filter media layer, wherein solids and polymers present in said drilling fluid are substantially removed and remain as a coating on the surface of the precoat filter media layer, and wherein said brine passes through the precoat filter media layer for recovery.
36 . The method of claim 35 , wherein said brine is collected into a tank.
37 . The method of claim 35 , further comprising spraying the outside surface of said drum filter with water.
38 . The method of claim 1 , further comprising treating the brine separated from the fluid with a pH agent to lower the pH.
39 . The method of claim 2 , further comprising treating the brine separated from the fluid with a pH agent to lower the pH.
40 . The method of claim 39 , wherein said pH is lowered to a pH of about 7 to about 12.
41 . The method of claim 1 , wherein said brine comprises formate, acetate, chloride, bromide, iodide, tungstate, carbonate, bicarbonate, or nitrate salts of ammonium, sodium, potassium, cesium, rubidium, lithium, calcium, magnesium, zinc, or barium, or a blend of two or more of these salts.
42 . The method of claim 2 , wherein said brine comprises formate, acetate, chloride, bromide, iodide, tungstate, carbonate, bicarbonate, or nitrate salts of ammonium, sodium, potassium, cesium, rubidium, lithium, calcium, magnesium, zinc, or barium, or a blend of two or more of these salts.
43 . The method of claim 1 , wherein said brine comprises at least one formate salt and/or tungstate salt.
44 . The method of claim 2 , wherein said brine comprises at least one formate salt and/or tungstate salt.
45 . The method of claim 1 , wherein said brine comprises cesium formate, potassium formate, cesium tungstate, potassium tungstate, or combinations thereof.
46 . The method of claim 2 , wherein said brine comprises cesium formate, potassium formate, cesium tungstate, potassium tungstate, or combinations thereof.
47 . The method of claim 1 , wherein said brine comprises cesium formate or cesium acetate or both.
48 . The method of claim 2 , wherein said brine comprises cesium formate or cesium acetate or both.
49 . The method of claim 1 , wherein said rotary vacuum filter is a continuous rotary vacuum filter.
50 . The method of claim 2 , wherein said rotary vacuum filter is a continuous rotary vacuum filter.
51 . A well servicing fluid or drilling fluid comprising recycled brine.
52 . The fluid of claim 51 , wherein said recycled brine has a purity of at least about 95%.
53 . The fluid of claim 51 , wherein said recycled brine comprises cesium formate or cesium acetate or both.
54 . The fluid of claim 5 1 , wherein said brine comprises a formate, acetate, chloride, bromide, iodide, tungstate, carbonate, bicarbonate, or nitrate salt of ammonium, sodium, potassium, cesium, rubidium, lithium, calcium, magnesium, zinc, or barium, or blends of two or more of these salts.
55 . The method of claim 1 , wherein said method is mobile.
56 . The method of claim 1 , wherein said method occurs on a drilling rig.
57 . The method of claim 1 , wherein said method occurs on a floating drilling rig.
58 . The method of claim 1 , wherein said method occurs on a ship or other floating vessel.
59 . A method to recover brine from a drilling fluid or other well servicing fluid comprising treating said drilling fluid with a filtering aid and filtering said fluid to recover at least a portion of said brine in said fluid.
60 . The method of claim 59 , wherein said filtering is with a centrifuge, membrane, filter paper, or combinations thereof.
61 . The method of claim 59 , wherein said filtering aid comprises at least one alkali metal hydroxide or polyelectrolyte or both.
62 . The method of claim 59 , wherein said filtering aid comprises at least one alkali metal hydroxide or polyelectrolyte or both.
63 . The method of claim 59 , wherein said filtering aid comprises sodium hydroxide or potassium hydroxide or both.
64 . The method of claim 61 , wherein said polyelectrolyte comprises iron salt, aluminum salt, cationic polymer flocculant, anionic polymer flocculant, or combinations thereof.
65 . The method of claim 59 , wherein said filtering aid is present in an amount of from about 0.1 kiloliter to about 35 kiloliters per m 3 of drilling fluid.
66 . The method of claim 59 , further comprising treating the brine separated from the fluid with a pH agent to lower the pH.
67 . The method of claim 66 , wherein said pH is lowered to a pH of about 7 to about 12.
68 . The method of claim 59 , wherein said brine comprises formate, acetate, chloride, bromide, iodide, tungstate, carbonate, bicarbonate, or nitrate salts of ammonium, sodium, potassium, cesium, rubidium, lithium, calcium, magnesium, zinc, or barium, or a blend of two or more of these salts.
69 . The method of claim 59 , wherein said brine comprises at least one formate salt or tungstate salt.
70 . The method of claim 59 , wherein said brine comprises cesium formate, potassium formate, cesium tungstate, potassium tungstate, or combinations thereof.
71 . The method of claim 59 , wherein said brine comprises cesium formate or cesium acetate or both.
72 . The method of claim 59 , wherein said drilling fluid is heated above ambient temperature prior to and/or during said filtering.
73 . The method of claim 59 , wherein said drilling fluid is heated to a temperature of at least about 50° C.
74 . The method of claim 59 , wherein said drilling fluid is heated to a temperature of from about 20° C. to about 180° C.
75 . The method of claim 1 , wherein said filtering of the drilling fluid or other well servicing fluid produces waste material which then is washed to remove any additional brine present on the waste material.
76 . The method of claim 75 , wherein said additional brine is filtered in order to obtain a more purified version of said brine.
77 . The method of claim 76 , wherein said filtering of said additional brine is achieved with a rotary vacuum filter.
78 . The method of claim 75 , wherein said waste material comprises drill cuttings.Join the waitlist — get patent alerts
Track US2004209781A1 — get alerts on status changes and closely related new filings.
We store only your email — no account needed. See our privacy policy.