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
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Cited by
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References
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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-modified
What 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.

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