1990
DOI: 10.2118/15457-pa
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Use of Inhibitors for Scale Control in Brine-Producing Gas and Oil Wells

Abstract: Field and laboratory work sponsored by t h e Cas Research Xnstituto (Cat) 8nd the Department of Energy (WE) have shown t h a t calcium-carbonate scale formation in waters produced with natural gas and o i l can be preventod by injection of phosphonate inhibitor i n t o t h e tomation, even i t h e fornration is sandstone without calcite binding material. c a r r i e d out on DOE'S geopressured-geothermal Gladys Hccall brine-gas well and CRI's to-production wells in the Hitchcock f i o l d .

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Cited by 23 publications
(6 citation statements)
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“…Phase I phosphonate return corresponds to the residual phosphonate that does not attached to the solid phase and returns in 3 pore volumes; phase II return corresponds to the dissolution from a high solubility solid phase and phase III return corresponds to the dissolution from a crystalline solubility phase (2) For DTPMP, phase II return can be characterized with a solubility product, pK sp = 52.4 -52.6 by assuming a stoichiometry of Ca 3 H 4 DTPMP; and phase III return corresponds to the dissolution from a crystalline solubility solid phase (pK sp = 53.3 -…”
Section: Discussionmentioning
confidence: 99%
See 1 more Smart Citation
“…Phase I phosphonate return corresponds to the residual phosphonate that does not attached to the solid phase and returns in 3 pore volumes; phase II return corresponds to the dissolution from a high solubility solid phase and phase III return corresponds to the dissolution from a crystalline solubility phase (2) For DTPMP, phase II return can be characterized with a solubility product, pK sp = 52.4 -52.6 by assuming a stoichiometry of Ca 3 H 4 DTPMP; and phase III return corresponds to the dissolution from a crystalline solubility solid phase (pK sp = 53.3 -…”
Section: Discussionmentioning
confidence: 99%
“…1,2 More recent papers have advanced the knowledge of inhibitor reactions under various production conditions. [3][4][5][6][7][8][9][10][11][12] The primary conclusions from several previous studies of NTMP(aminotri(methylene phosphonic acid))calcite reaction are [13][14][15][16] : (1) The extent of NTMP retention by carbonate-rich formation rock is limited by the amount of calcite that can dissolve prior to inhibitor-induced surface poisoning; (2) Calcite-surface poisoning effect is observed after approximately 20 molecular layers of phosphonate surface coverage that retards further calcite dissolution; (3) The consequence of retarded calcite dissolution is that less basic ion, − 2 3 CO , is released into solution, leaving the solution more acidic; therefore, more soluble calcium phosphonate solid phases form.…”
Section: Introductionmentioning
confidence: 99%
“…With this method, the scale-control options include the following: limiting production so that the drop in pressure is not sufficient to induce precipitation; injecting trace concentration of inhibitors in the surface equipment; injecting trace concentrations of inhibitors downwell to pressurize the fluid above the flash point; and squeezing inhibitor into the formation so that the inhibitor will be released slowly when production begins [2,12,43]. In addition, the use of downhole pumps can prevent scaling within the wellbore.…”
Section: Calcium Carbonatementioning
confidence: 99%
“…High concentrations of iron have in the past been tied to problems with scale inhibitor treatments. 5 It has been cited by a number of authors as a potential source of damage in many chemical treatments. 6,7 In addition to the residual concentration of iron after the acid treatment, core flood studies by Company A had shown iron values of > 900 mg/L would be generated through the dissolution of the normal iron minerals as a result of the treatment chemical.…”
Section: Postmortemmentioning
confidence: 99%