All Days 1998
DOI: 10.2118/49197-ms
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Scale Inhibitor Selection for Continuous and Downhole Squeeze Application in HP/HT Conditions

Abstract: With the development of a number of new HT/HP fields in the North Sea, for example the ETAP fields (Eastern Trough Area Project), a number of important "scale" control issues have arisen. In addition to harsh downhole conditions (T - 180 C; P - 13,000 psi), high salinity formation water chemistries indicate that the control of inorganic precipitates in these systems will be very important. The form of the inorganic precipitates are predicted to include the more Cornnjton oilfield scales (BaSO4 and CaCO3). In a… Show more

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Cited by 26 publications
(17 citation statements)
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“…Squeeze treatment of scale inhibitor is the most efficient and widely used method to prevent scale formation. Polymeric scale inhibitors typically have better thermal stability than phosphonates Fan, et al 2011;Wang, et al 2009;Graham, et al 1998). Many of these inhibitors are commonly applied by an inhibitor squeeze treatment (Rosenstein 1936;Kan, et al 2005).…”
Section: Introductionmentioning
confidence: 99%
“…Squeeze treatment of scale inhibitor is the most efficient and widely used method to prevent scale formation. Polymeric scale inhibitors typically have better thermal stability than phosphonates Fan, et al 2011;Wang, et al 2009;Graham, et al 1998). Many of these inhibitors are commonly applied by an inhibitor squeeze treatment (Rosenstein 1936;Kan, et al 2005).…”
Section: Introductionmentioning
confidence: 99%
“…That said, some general conclusions with respect to chemical retention in both carbonate and sandstone formations can be drawn from previous literature examples, which illustrate that some chemicals types, such as certain sulphonated polymers and modified "calcium tolerant" phosphonates, have relatively poor retention on the reservoir substrates leading to rapid release when compared with other chemicals. 1,3,8 Performance/Chemical Selection: The spent acid contains very high calcium (and magnesium) concentration typically > 50,000mg/l at mildly acidic pH's (~pH 4). While much of the spent acid in a field treatment is immediately produced back upon clean-up, a portion of it may remain in the reservoir matrix for extended time periods at full reservoir temperature (~210-225 o F).…”
Section: Introductionmentioning
confidence: 99%
“…Many scale inhibitor species, particularly conventional phosphonates and polyacrylate based polymers, suffer chemical incompatibility in high calcium formations. 9 Thermal Stability: The spent acid, although "neutralized", is expected to remain mildly acidic at a pH of ~4. The selected scale inhibitors must therefore remain thermally stable under extended periods of time at full reservoir temperature in the moderately acidic "spent acid" brine.…”
Section: Introductionmentioning
confidence: 99%
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“…But with increased concerns toward environment, phosphonates are prohibited in North Sea. Moreover, they are perceived to be unstable under high temperature condition compared to polymeric scale inhibitors, which typically have better thermal stability Fan, et al 2011;Wang, et al 2009;Graham, et al 1998). Sulphonated polymers such as sulphonated polycarboxylic acids have been developed to meet the increasingly strict bioaccumulation, biodegradation and ecotoxicity regulations (Dickinson, et al 2011).…”
Section: Introductionmentioning
confidence: 99%