Direct Emulsions and Methods of Use
US-2018298706-A1 · Oct 18, 2018 · US
US2020181471A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2020181471-A1 |
| Application number | US-202016789749-A |
| Country | US |
| Kind code | A1 |
| Filing date | Feb 13, 2020 |
| Priority date | Aug 13, 2014 |
| Publication date | Jun 11, 2020 |
| Grant date | — |
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This invention provides zinc-free aqueous brine compositions. These zinc-free aqueous brine compositions have a density of about 14.3 pounds per gallon or more, and a true crystallization temperature of about 20° F. or less, and comprise water and one or more inorganic bromide salts, with the provisos that when calcium bromide is present, one or more other water-soluble inorganic salts are also present, when lithium bromide is present, calcium bromide is absent, when bismuth(III) bromide is present, one or more other water-soluble inorganic salts are also present, and for a true crystallization temperature of about 10° F. or less, when manganese(II) bromide is present, one or more other water-soluble inorganic salts are also present. Processes for forming these zinc-free aqueous brine compositions are also provided.
Opening claim text (preview).
That which is claimed is: 1 . A wellbore fluid comprising a zinc-free aqueous brine having a density of 1.71 kg/L (14.3 pounds per gallon) or more, and a true crystallization temperature of −6.7° C. (20° F.) or less, which aqueous brine comprises calcium bromide and a manganese salt selected from manganese(II) bromide, manganese(II) nitrate, and manganese polytungstate. 2 . A wellbore fluid of claim 1 wherein the manganese salt is manganese(II) bromide. 3 . A wellbore fluid of claim 1 in which the aqueous brine has a density of 1.75 kg/L (14.6 pounds per gallon) or more. 4 . A wellbore fluid of claim 2 in which the aqueous brine has a density of 1.75 kg/L (14.6 pounds per gallon) or more and a pH value in the range of 2.5 to 5. 5 . A wellbore fluid of claim 2 also comprising tin(IV) bromide, wherein the aqueous brine has a density of 1.80 kg/L (15.0 pounds per gallon) or more. 6 . A wellbore fluid of claim 2 also comprising bismuth(III) bromide, and wherein the aqueous brine has a density of 1.92 kg/L (16.0 pounds per gallon) or more. 7 . A wellbore fluid of claim 2 also comprising tin(II) bromide or indium(III) bromide. 8 . A wellbore fluid of claim 2 which also comprises tin(II) bromide, wherein the aqueous brine has a density of 1.80 kg/L (15.0 pounds per gallon) or more; or indium(III) bromide, wherein the aqueous brine has a density of 1.92 kg/L (16.0 pounds per gallon) or more. 9 . A process for forming a wellbore fluid comprising a zinc-free aqueous brine having a density of 1.71 kg/L (14.3 pounds per gallon) or more, and a true crystallization temperature of −6.7° C. (20° F.) or less, which process comprises mixing, in any order, components comprising water, calcium bromide and a manganese salt selected from manganese(II) bromide, manganese(II) nitrate, and manganese polytungstate. 10 . A process of claim 9 wherein the manganese salt is manganese(II) bromide. 11 . A process of claim 9 in which the aqueous brine has a density of 1.75 kg/L (14.6 pounds per gallon) or more. 12 . A process of claim 10 in which the aqueous brine has a density of 1.75 kg/L (14.6 pounds per gallon) or more and a pH value in the range of 2.5 to 5. 13 . A process of claim 10 wherein the aqueous brine also comprises tin(IV) bromide, wherein the aqueous brine has a density of 1.80 kg/L (15.0 pounds per gallon) or more. 14 . A process of claim 10 wherein the aqueous brine also comprises bismuth(III) bromide, and wherein the aqueous brine has a density of 1.92 kg/L (16.0 pounds per gallon) or more. 15 . A process of claim 10 wherein the aqueous brine also comprises tin(II) bromide or indium(III) bromide. 16 . A process of claim 10 wherein the aqueous brine also comprises tin(II) bromide, wherein the aqueous brine has a density of 1.80 kg/L (15.0 pounds per gallon) or more; or indium(III) bromide, wherein the aqueous brine has a density of 1.92 kg/L (16.0 pounds per gallon) or more. 17 . A method of treating a wellbore, said method comprising: introducing into the wellbore a wellbore fluid comprising a zinc-free aqueous brine having a density of 1.71 kg/L (14.3 pounds per gallon) or more, and a true crystallization temperature of −6.7° C. (20° F.) or less, which fluid comprises calcium bromide and a manganese salt selected from manganese(II) bromide, manganese(II) nitrate, and manganese polytungstate. 18 . A method of claim 17 wherein the manganese salt is manganese(II) bromide. 19 . A method of claim 17 in which the aqueous brine has a density of 1.75 kg/L (14.6 pounds per gallon) or more. 20 . A method of claim 18 in which the aqueous brine has a density of 1.75 kg/L (14.6 pounds per gallon) or more and a pH value in the range of 2.5 to 5. 21 . A method of claim 18 wherein the aqueous brine also comprises tin(IV) bromide, and wherein the aqueous brine has a density of 1.80 kg/L (15.0 pounds per gallon) or more. 22 . A method of claim 18 wherein the aqueous brine also comprises bismuth(III) bromide, and wherein the aqueous brine has a density of 1.92 kg/L (16.0 pounds per gallon) or more. 23 . A method of claim 18 wherein the aqueous brine also comprises tin(II) bromide or indium(III) bromide. 24 . A method of claim 18 wherein the aqueous brine also comprises tin(II) bromide, wherein the aqueous brine has a density of 1.80 kg/L (15.0 pounds per gallon) or more; or indium(III) bromide, wherein the aqueous brine has a density of 1.92 kg/L (16.0 pounds per gallon) or more.
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