Controlling sulfide scavenger content of oil-based drilling fluid

Claim 2

A process for determining the amount of unspent zinc-based sulfide scavenger in an oil-based drilling fluid, performed at a field location comprising: mixing one part by volume of circulating oil-based drilling fluid from a well site with at least about 4 parts by volume of a selective solvent for zinc ions, which solvent establishes a mixture with a pH of no less than about 6 and is capable of dissolving substantially all of the zinc present in the drilling mud except for zinc ions that have been combined into molecules of zinc sulfides; separating the resulting aqueous solution from any oil phase and undissolved solids; and measuring the amount of zinc in the aqueous solids-free solution in order to determine the amount of unspent zinc-based sulfide scavenger in the circulating oil-based drilling fluid.

Claim 3

The process of claim 1 in which the selective solvent for zinc is glacial acetic acid.

Claim 4

The process for claim 1 in which the amount of zinc in the aqueous solution is determined by measuring the amount of X-ray fluorescence exhibited by the solution.

Claim 5

The process of claim 1 in which the selective solvent for zinc is glacial acetic acid, the mixture of drilling fluid and selective solvent contains about 1 part by volume of the drilling fluid per 4 to 10 parts by volume of glacial acetic acid, and the amount of zinc dissolved in the aqueous solution is determined by a measurement of X-ray fluorescence.

Claim 6

The process of claim 4 in which the amount of zinc dissolved in the aqueous solution is determined by a portable X-ray fluorescence spectrographic unit.

Claim 7

The process of claim 1 in which an additional portion of the same drilling fluid is similarly mixed with a solvent consisting essentially of an aqueous strong acid solution capable of dissolving substantially all combined and non-combined zinc in the drilling fluid, with the amount of zinc in the aqueous solution being similarly measured to determine the decrease in scavenger due to drilling fluid dilution and reaction of scavenger with sulfides.

Claim 8

The process of claim 6 in which the strong acid is hydrochloric acid having a normality of about 1 to 3.

Claim 9

The process of claim 1 in which the amount of zinc dissolved in the selective solvent for zinc ions is determined by colorimetric analysis.

Claim 10

A process for drilling a well with an oil-based drilling fluid comprising: (1) adding zinc-based scavengers to the oil-based drilling fluid for controlling encountered sulfide ions, (2) monitoring the drilling fluid to determine the amount of unspent zinc-based sulfide scavenger by: (a) mixing one part by volume of a sample of circulating drilling fluid with at least 4 or more parts by volume of a selective solvent for zinc ions, with said solvent establishing a pH of less than about 6 and being capable of dissolving substantially all of the zinc present in the drilling fluid except for zinc ions combined into molecules of zinc sulfides; (b) separating the resulting aqueous solution from any oil phase and undissolved solids; and (c) measuring the amount of zinc in the aqueous solution in order to determine the proportion of the unspent zinc-based sulfide scavenger in the circulating drilling fluids; and (3) adjusting the amount of scavenger in the circulating drilling fluid to the extent required to maintain an amount of scavenger in the drilling fluid sufficient to scavenge encountered sulfide ions.

Claim 11

A process for drilling a well with an oil-based drilling fluid comprising: (1) adding zinc-based scavengers to the oil-based drilling fluid for controlling encountered sulfide ions, (2) monitoring the drilling fluid to determine the amount of unspent zinc-based sulfide scavenger by: (a) mixing one part by volume of a sample of circulating drilling fluid with at least 4 or more parts by volume of a selective solvent for zinc ions, with said solvent establishing a pH of less than about 6 and being capable of dissolving substantially all of the zinc present in the drilling fluid except for zinc ions combined into molecules of zinc sulfides; (b) separating the resulting aqueous solution from any oil phase and undissolved solids; and (c) measuring the amount of zinc in the aqueous solution in order to determine the proportion of the unspent zinc-based sulfide scavenger in the circulating drilling fluids; and (3) adjusting the amount of scavenger in the circulating drilling fluid to the extent required to maintain an amount of scavenger in the drilling fluid sufficient to scavenge encountered sulfide ions.

Claim 12

The process of claim 9 in which the amount of zinc in the aqueous solution is determined by measuring the amount of X-ray fluorescence exhibited by the solution.

Claim 13

The process of claim 9 in which the selective solvent for zinc is glacial acetic acid.

Claim 14

The process of claim 9 in which the selective solvent for zinc is glacial acetic acid, the mixture of drilling fluid and selective solvent contains about 1 part by volume of the drilling fluid per 4 to 10 parts by volume of glacial acetic acid, and the amount of zinc dissolved in the aqueous solution is determined by a measurement of X-ray fluorescence.

Claim 15

The process of claim 9 in which an additional portion of the same drilling fluid is similarly mixed with solvent consisting essentially of an aqueous strong acid solution capable of dissolving substantially all combined and non-combined zinc in the drilling fluid, with the amount of zinc in the aqueous solution being similarly measured to determine the decrease in scavenger due to drilling fluid dilution and reaction of scavenger with sulfides.

Claim 16

The process of claim 13 in which the strong acid is hydrochloric acid having a normality of about 1 to 3.

Claim 17

The process of claim 9 in which the amount of zinc dissolved in the selective solvent for zinc ions is determined by colorimetric analysis.

Claim 18

The process of claim 9 in which the zinc-based sulfide scavenger is a zinc carbonate.

Claim 19

The process of claim 9 in which the zinc-based sulfide scavenger is basic zinc carbonate.

Claim 20

The process of claim 9 in which the zinc-based sulfide scavenger is an organic zinc chelate.

Claim 21

The process of claim 9 in which determinations of the proportion of unspent zinc-based scavenger in an oil-based drilling fluid are (a) initiated at a frequency which provides a rate of testing that varies with variations in the likelihood of the borehole encountering changed sulfide ion concentrations which change the extent to which the amount of unspent scavenger is different between the tests, (b) are conducted at the drill site and, (c) to the extent required, are utilized to proportion changes in the concentration of scavenger in the drilling fluid for keeping that concentration high enough to scavenge the sulfide being encountered.

Claim 22

A process for drilling a well with an oil-based drilling fluid comprising: (1) adding zinc-based scavengers to the drilling fluid for controlling encountered sulfide ions, (2) monitoring the drilling fluid to determine the amount of unspent zinc-based sulfide scavenger by: (a) mixing one part by volume of a sample of circulating drilling fluid with about 4 to 10 parts by volume of glacial acetic acid; (b) separating the resulting aqueous solution from any oil phase and undissolved solids; and (c) determining the amount of zinc in the aqueous solution, by measuring the amount of X-ray fluorescence exhibited by the solution with a portable X-ray fluorescence spectographic unit, in order to determine the proportion of the unspent zinc-based sulfide scavenger in the circulating drilling fluid; and (3) adjusting the amount of scavenger in the circulating drilling fluid to the extent required to maintain an amount of scavenger in the drilling fluid sufficient to scavenge encountered sulfide ions.

Claim 23

A process for drilling a well with an oil-based drilling fluid comprising: (1) adding zinc-based scavengers to the drilling fluid for controlling encountered sulfide ions, (2) monitoring the drilling fluid to determine the amount of unspent zinc-based sulfide scavenger by: (a) mixing one part by volume of a sample of circulating drilling fluid with about 4 to 10 parts by volume of glacial acetic acid; (b) separating the resulting aqueous solution from any oil phase and undissolved solids; and (c) determining the amount of zinc in the aqueous solution, by measuring the amount of X-ray fluorescence exhibited by the solution with a portable X-ray fluorescence spectographic unit, in order to determine the proportion of the unspent zinc-based sulfide scavenger in the circulating drilling fluid; and (3) adjusting the amount of scavenger in the circulating drilling fluid to the extent required to maintain an amount of scavenger in the drilling fluid sufficient to scavenge encountered sulfide ions.