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Oilfield scale inhibition

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fluids are pumped from the ground, changes in temperature, pressure and chemical composition shift the equilibria and cause precipitation and deposition of sparingly soluble salts that build up over time with the potential of blocking vital assets in the oil production setups. Scaling can occur at all stages of oil/gas production systems (upstream, midstream and downstream) and causes blockages of well-bore perforations, casing, pipelines, pumps, valves etc. Severe scaling issues have been reported in Russia and certain North Sea production systems.
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these functional groups tend to prevent the crystal growth sites using dissociated or un-dissociated groups. The dissociation state is determined by the pH of the system, hence knowledge of the pKa values of the chemicals are important for different pH environments. Again, the inhibition efficiency of the SI depends on its compatibility with other production chemicals such as corrosion inhibitors.
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SIs have been made since the late 1990s and an increasing number of such SIs are becoming commercially available. Recent environmental awareness over the past 15 years has resulted in the production and application of more environmentally friendly SIs, otherwise called 'Green Scale Inhibitors' (GSI).
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have been used extensively for scale treatment in water systems due to their excellent solubility, thermal stability and dosage efficiency. In the water treatment industry, the major classes of SIs have inorganic phosphate, organophosphorous and organic polymer backbones and common examples are PBTC
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Sulfate scale usually forms when formation water and injected seawater mix together. The relationship between these and the degree of supersaturation is crucial in estimating the amount of sulfate salts that will precipitate in the system. Seawater has a high concentration of sulfate ions and mixing
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Two main classifications of scales are known; inorganic and organic scales and the two types are mutually inclusive, occurring simultaneously in the same system, referred to as mixed scale. Mixed scales may result in highly complex structured scales that are difficult to treat. Such scales require
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properties. The inhibitor molecules essentially bind ions in aqueous phase of production fluids that could potentially precipitate as scales. For instance, to bind positively charged ions in the water, anions must be present in the inhibitor molecular backbone structure and vice versa. Group (II)
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hazardous and harmful to human health, water supplies, marine and freshwater organisms. For instance trails of increased turbidity resulting from oil and gas exploratory activities on the eastern shelf of Sakhalin in Russia have been reported with consequential adverse effects on salmon, cod and
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A SI with a combination of two or more of these functional groups is more efficient in managing scale problems. Usually the sodium salts of the carboxylic derivatives are synthesized as the anionic derivatives and are known to be the most effective due to their high solubilities. Interactions of
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Due to its relatively high solubility in water, Calcium sulfate is the easiest sulfate scale to remove chemically as compared to strontium and barium sulfate. Scale crystals are initially dispersed in production systems until accumulation of stable crystals of insoluble sulfates and scale growth
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whose solubility decreases with temperature as is the case for most of the gases (exothermic dissolution reaction in water). In calcium sulfate, the reason is that the dissolution reaction of calcium sulfate itself is exothermic and therefore is favored when the temperature decreases (then, the
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The three prevailing water-related problems that upset oil companies today are corrosion, gas hydrates and scaling in production systems. The reservoir water has a high composition of dissolved minerals equilibrated over millions of years at constant physicochemical conditions. As the reservoir
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has been used in oil exploration and its very low toxicity and crystal growth inhibition power has been reported for treating calcite scales. Examples of poorly biodegradable SIs such as the amino-phosphonate and acrylate-based SIs are being phased-out by stringent environmental regulations as
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Generally, the environmental impacts of SIs are complicated further by combination of other chemicals applied through exploratory, drilling, well-completion and start-up operations. Produced fluids, and other wastes from oil and gas operations with high content of different toxic compounds are
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Another modern alternative to SI use for environmental protection is the development of materials or coatings that intrinsically resist formation of inorganic scale to begin with. A variety of strategies can be used to accomplish this aim, including engineering of wettability properties and
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Sulfates of Group (II) metal ions (M), generally decrease in solubility down the group. The most difficult scales to remove are those of Barium sulfate because of its high insolubility forming very hard scale deposits. A general representation of the reaction is summarized in reaction:
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SIs, commonly employed for treating calcium carbonate scales are known to be environmentally friendly but poor inhibition efficiency. Release of SIs containing Nitrogen and Phosphorus distorts the natural equilibrium of the immediate water body with adverse effects on aquatic life.
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Another alternative, polysaccharide SIs meet the requirements for environmentally friendly materials; they contain no Phosphorus or Nitrogen and are noted for their non-toxic, renewable, and biodegradable properties. Carboxymethyl inulin (CMI), which is isolated from the roots of
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The first two methods may be used for short-term treatment and effective for mild-scaling conditions, however, continuous injection or chemical scale squeeze treatment with SIs have been proven over the years to be the most efficient and cost-effective preventative technique.
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engineering of epitaxial properties to prevent mineral growth or to make minerals easier to remove following growth. Recent work has demonstrated that some classes of hydrophobic and superhydrophobic surfaces can cause self-ejection of scale grown during evaporation
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used to describe solid deposits that grow over time, blocking and hindering fluid flow through pipelines, valves, pumps etc. with significant reduction in production rates and equipment damages. Scaling represents a major challenge for
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Shi, Wen-Yan; Ding, Cheng; Yan, Jin-Long; Han, Xiang-Yun; Lv, Zhi-Min; Lei, Wu; Xia, Ming-Zhu; Wang, Feng-Yun (2012-04-02). "Molecular dynamics simulation for interaction of PESA and acrylic copolymers with calcite crystal surfaces".
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copolymers, such as SPOCA (sulfonated phosphonocarboxylic acid), polyvinyl sulfonates. Two common oilfield mineral SIs are Poly-Phosphono Carboxylic acid (PPCA) and Diethylenetriamine- penta (methylene phosphonic acid)
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is the scale saturation ratio, defined as the ratio of the activity product to the solubility product of the salt. Activity is defined as the product of the activity coefficients and the concentrations of Ca and
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Laing, N.; Graham, G.M.; Dyer, S.J. (2003-01-01). "Barium Sulphate Inhibition in Subsea Systems – the Impact of Cold Seabed Temperatures on the Performance of Generically Different Scale Inhibitor Species".
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While the solubility of most inorganic salts (NaCl, KCl, ...) increases with temperature (endothermic dissolution reaction), some inorganic salts such as calcium carbonate and calcium sulfate have also a
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with formation water with many Ca and other M ions in the formation water. Severe problems with sulfate scale are common in reservoirs where seawater has been injected to enhance oil recovery.
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Pro, Danièle; Huguet, Samuel; Arkoun, Mustapha; Nugier-Chauvin, Caroline; Garcia-Mina, José Maria; Ourry, Alain; Wolbert, Dominique; Yvin, Jean-Claude; Ferrières, Vincent (2014-11-04).
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Jordan, Myles M.; Sorhaug, Eyvind; Marlow, David (2012-11-01). "Red vs. Green Scale Inhibitors for Extending Squeeze life--A Case Study From the North Sea, Norwegian Sector--Part II".
685:, drilling operations and extraction of the oil from the well bore decreases the pressure of the formation and the equilibrium shifts to the right (3) to increase the production of CO 1565:
Lawless, T.A.; Bourne, H.M.; Bolton, J.R. (1993-01-01). "Examining the Potential for Corrosion Inhibitor and Scale Inhibitor Compatibility in a Multifunctional Squeeze Strategy".
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Graham, GM Boak, LS Sorbie, KS (2003). "The influence of formation calcium and magnesium on the effectiveness of generically different barium sulphate oilfield scale inhibitors".
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Shakkthivel, P.; Vasudevan, T. (2006-10-02). "Acrylic acid-diphenylamine sulphonic acid copolymer threshold inhibitor for sulphate and carbonate scales in cooling water systems".
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Knudsen, B.L.; Hjelsvold, M.; Frost, T.K.; Svarstad, M.B.E.; Grini, P.G.; Willumsen, C.F.; Torvik, H. (2004-01-01). "Meeting the Zero Discharge Challenge for Produced Water".
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Shi, Wenyan; Xia, Mingzhu; Lei, Wu; Wang, Fengyun (2013-08-01). "Molecular dynamics study of polyether polyamino methylene phosphonates as an inhibitor of anhydrite crystal".
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Liu, Jun; Willför, Stefan; Xu, Chunlin (2015-01-01). "A review of bioactive plant polysaccharides: Biological activities, functionalization, and biomedical applications".
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Inhibition of calcium carbonate scale deposition and crystal studies of its polymorphs have been conducted. Different SIs are designed for specific scaling conditions and
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Liang, Bin; Pan, Kai; Li, Li; Giannelis, Emmanuel P.; Cao, Bing (2014-08-15). "High performance hydrophilic pervaporation composite membranes for water desalination".
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The scaling-tendency of an oil-well can be predicted based on the prevailing conditions such as pH, temperature, pressure, ionic strength and the mole fraction of CO
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occur at nucleation centers. Uneven pipeline surfaces and production equipment such as pumps and valves cause rapid scale growth to levels that can block pipelines.
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Amjad, Zahid; Koutsoukos, Petros G. (2014-02-17). "Evaluation of maleic acid based polymers as scale inhibitors and dispersants for industrial water applications".
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such as injection water. The mixing changes causes reaction between incompatible ions and changes the thermodynamic and equilibrium state of the reservoir fluids.
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are the most often encountered organic scales in the oil industry. This article focuses on the simplest and common form of scales encountered; inorganic scales.
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Alzahrani, Salem; Mohammad, Abdul Wahab (2014-12-01). "Challenges and trends in membrane technology implementation for produced water treatment: A review".
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ions. The ionic strength is a measure of the concentration of the dissociated ions dissolved in water also called as “total dissolved solids” (TDS).
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to offset the change in pressure. After years of oil production, wells may experience significant pressure drops resulting in large CaCO
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Kırboga, Semra; Öner, Mualla (2012-03-01). "The inhibitory effects of carboxymethyl inulin on the seeded growth of calcium carbonate".
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Kirboga, Semra; Ă–ner, Mualla (2013-04-16). "Investigation of calcium carbonate precipitation in the presence of carboxymethyl inulin".
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Fried, Ruth; Mastai, Yitzhak (2012-01-01). "The effect of sulfated polysaccharides on the crystallization of calcite superstructures".
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Crabtree, M., Eslinger, D., Fletcher, P., Miller, M., Johnson, A., & King, G. (1999). "Fighting Scale- prevention and removal".
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Scale inhibitors are specialty chemicals that are added to oil production systems to delay, reduce and/or prevent scale deposition.
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and subsequent deposition of the inorganic salts occur. The most common types of inorganic scales known to the oil/gas industry are
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from blocking or hindering fluid flow through pipelines, valves, and pumps used in oil production and processing.
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Mitchell, R.W; Grist, D.M.; Boyle, M.J. (May 1980). "Chemical Treatments Associated with North Sea Projects".
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Different oilfield scale remediation techniques are known but majority are based on three basic themes:
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Boak, Lorraine S.; Sorbie, Ken (2010-11-01). "New Developments in the Analysis of Scale Inhibitors".
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Oddo, J.E.; Tomson, M.B. (1994-02-01). "Why Scale Forms in the Oil Field and Methods To Predict It".
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Water, noted for its high solvation power can dissolve certain gases such as carbon dioxide (CO
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properties and therefore reduce pollution of the waters around oil production systems.
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The two reactions (2) and (4) describe the equilibrium between bicarbonate ions (HCO
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Wayne W Frenier, Murtaza Ziauddin, N. Wolf (Editor), Ryan Hartman (Editor) (2008).
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Formation, removal, and inhibition of inorganic scale in the oilfield environment
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Formation, removal, and inhibition of inorganic scale in the oilfield environment
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in the oil and gas industry. Examples of oilfield scales are calcium carbonate (
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Johannsen, F. R (2003-01-01). "Toxicological profile of carboxymethyl inulin".
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metal ions are commonly sequestered by SIs with the following functionalities;
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and accumulation of insoluble crystals (salts) from a mixture of incompatible
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Scale build-up effectively decreases pipeline diameter and reduces flow rate
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in the vapor and aqueous phases. For instance the saturation index for CaCO
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in water according to equation (3) to form hydronium and bicarbonate (HCO
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Chemical Structure of Diethylenetriaminepenta(methylene-phosphonic acid)
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Collins, I.R. (2002-01-01). "A New Model for Mineral Scale Adhesion".
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deposits as the equilibrium shifts to offset the pressure changes.
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These GSIs are designed to have reduced bio-accumulating and high
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aggressive, severe and sometimes costly remediation techniques.
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demonstrated in the North sea by Norway zero discharge policy.
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McBride, Samantha; Lake, John; Varanasi, Kripa (2023-04-07).
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Application of Scale Inhibitors (SIs) for scale prevention
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that occur when the formation water mixes with different
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NACE International. pp. 523–32. 934: 738:scale is calculated using the formula; 1956:Colloids and Surfaces B: Biointerfaces 1719: 1709: 1659: 1600: 1590: 1543: 1326: 1316: 1230: 1201: 1191: 1114: 1104: 1775: 1773: 1771: 1735: 1733: 1437: 1435: 7: 1250: 1248: 1082: 1080: 1054: 1052: 1050: 1048: 1046: 1044: 1042: 1040: 1038: 1036: 981: 979: 977: 975: 973: 971: 969: 967: 965: 944:Journal of Water Process Engineering 1688:. Society of Petroleum Engineers. 1569:. Society of Petroleum Engineers. 1295:. Society of Petroleum Engineers. 1170:. Society of Petroleum Engineers. 1091:. Society of Petroleum Engineers. 992:. Society of Petroleum Engineers. 35:phases in oil processing systems. 14: 493:, Ni and Fe mixed oxide: NiO + Fe 1995:The Journal of Chemical Physics 1782:SPE Production & Operations 1742:SPE Production & Operations 1404:Journal of Petroleum Technology 1257:SPE Production & Facilities 463:Fe and Fe mixed oxide: FeO + Fe 1968:10.1016/j.colsurfb.2011.10.031 1491:10.1016/j.jcrysgro.2011.09.044 1141:Society of Petroleum Engineers 1: 1898:10.1016/S0278-6915(02)00213-2 1836:10.1016/j.carbpol.2014.05.075 1059:Kelland, M. A. (6 Feb 2014). 1886:Food and Chemical Toxicology 1623:www.offshore-environment.com 887:Environmental considerations 1519:10.1016/j.desal.2012.01.019 1456:10.1016/j.desal.2013.05.013 1385:10.1016/j.desal.2005.12.023 1358:10.1016/j.desal.2013.12.012 1027:10.1016/j.desal.2014.05.021 2062: 1871:10.1016/j.bcdf.2014.12.001 986:W. Frenier, Wayne (2008). 956:10.1016/j.jwpe.2014.09.007 98:Inorganic scales refer to 1644:Oilfield water technology 1471:Journal of Crystal Growth 17:Oilfield scale inhibition 901:environmentally friendly 899:Efforts to develop more 683:Le Chatelier's principle 363:Aluminium oxy-hydroxides 141:Le Chatelier's principle 39:is a common term in the 875:- Carboxylate ions (-CO 861:- Phosphonate ions (-PO 844:- Phosphonate ions (-PO 537:Calcium carbonate scale 126:are often encountered. 868:- Sulphonate ions (-SO 796: 65: 1824:Carbohydrate Polymers 794: 681:) salt. According to 132:retrograde solubility 63: 854:Phosphate ions (-OPO 545:) to form aqueous CO 1483:2012JCrGr.338..147F 824:terpolymers (MAT), 278:Magnesium hydroxide 2036:Petroleum industry 1933:10.1039/c3ce27022j 1117:has generic name ( 894:littoral amphipods 797: 66: 2008:10.1063/5.0142428 1794:10.2118/140752-pa 1754:10.2118/130401-pa 1653:978-1-57590-204-3 1534:Soc Petroleum Eng 764:Scale remediation 534: 533: 431:Metallic copper, 169:Calcium carbonate 160:Chemical Formula 145:calcium hydroxide 2053: 2021: 2020: 2010: 1986: 1980: 1979: 1951: 1945: 1944: 1916: 1910: 1909: 1881: 1875: 1874: 1854: 1848: 1847: 1821: 1812: 1806: 1805: 1777: 1766: 1765: 1737: 1728: 1727: 1721: 1717: 1715: 1707: 1694:10.2118/86671-ms 1681: 1672: 1671: 1665: 1657: 1639: 1633: 1632: 1630: 1629: 1615: 1609: 1608: 1602: 1598: 1596: 1588: 1575:10.2118/25167-ms 1562: 1556: 1555: 1549: 1541: 1529: 1523: 1522: 1501: 1495: 1494: 1466: 1460: 1459: 1439: 1430: 1429: 1419: 1395: 1389: 1388: 1368: 1362: 1361: 1341: 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CRC press. 1062: 1055: 1053: 1051: 1049: 1047: 1045: 1043: 1041: 1039: 1037: 1033: 1028: 1024: 1020: 1016: 1009: 1006: 1001: 995: 991: 990: 982: 980: 978: 976: 974: 972: 970: 968: 966: 962: 957: 953: 949: 945: 938: 935: 929: 927: 923: 920: 914: 911: 907: 902: 897: 895: 886: 884: 880: 873: 866: 859: 853: 849: 842: 839: 834: 832: 827: 826:sulfonic acid 823: 819: 815: 810: 807:polymers and 806: 802: 793: 786: 784: 777: 774: 771: 770: 769: 763: 761: 749: 739: 728: 724: 720: 703: 696: 694: 684: 654: 626: 605: 583: 582: 581: 536: 530: 527: 509: 507: 504: 503: 492: 489: 479: 477: 474: 473: 462: 452: 450: 447: 446: 442: 434: 430: 427: 425: 422: 421: 418: 414: 410: 407: 393: 391: 388: 387: 384: 380: 376: 372: 369: 366: 364: 361: 360: 357: 353: 349: 345: 341: 337: 333: 329: 314: 312: 309: 308: 305: 302: 299: 297: 294: 293: 290: 287: 281: 279: 276: 275: 272: 269: 263: 261: 258: 257: 254: 251: 241: 239: 236: 235: 223: 219: 207: 203: 200: 194: 192: 189: 188: 185: 181: 178: 172: 170: 167: 166: 162: 159: 156: 155: 152: 150: 146: 142: 133: 127: 125: 121: 117: 113: 109: 105: 101: 93: 91: 89: 85: 81: 72: 70: 62: 55: 53: 51: 47: 42: 36: 34: 30: 29:precipitation 26: 22: 18: 1998: 1994: 1984: 1959: 1955: 1949: 1927:(18): 3678. 1924: 1921:CrystEngComm 1920: 1914: 1892:(1): 49–59. 1889: 1885: 1879: 1865:(1): 31–61. 1862: 1858: 1852: 1827: 1823: 1810: 1785: 1781: 1745: 1741: 1685: 1643: 1637: 1626:. Retrieved 1622: 1613: 1566: 1560: 1546:cite journal 1537: 1533: 1527: 1510: 1507:Desalination 1506: 1499: 1474: 1470: 1464: 1447: 1444:Desalination 1443: 1407: 1403: 1393: 1376: 1373:Desalination 1372: 1366: 1352:(1): 55–63. 1349: 1346:Desalination 1345: 1339: 1292: 1285: 1263:(1): 47–54. 1260: 1256: 1233:cite journal 1224: 1220: 1214: 1167: 1161: 1144: 1140: 1134: 1088: 1060: 1018: 1015:Desalination 1014: 1008: 988: 947: 943: 937: 924: 915: 898: 890: 881: 874: 867: 860: 851: 850: 843: 835: 809:phosphonates 801:acrylic acid 798: 781: 767: 750: 740: 729: 725: 721: 704: 700: 672: 540: 352:cristobalite 330:Serpentine, 128: 97: 88:gas hydrates 80:Paraffin wax 76: 67: 41:oil industry 16: 15: 2046:Engineering 1830:: 145–151. 1450:: 137–143. 1227:(3): 30–45. 1115:|last= 1021:: 199–206. 950:: 107–133. 822:maleic acid 805:maleic acid 224:form) (CaSO 222:hemihydrate 149:portlandite 84:asphaltenes 2030:Categories 1628:2016-11-22 930:References 803:polymers, 506:Phosphates 413:cancrinite 112:carbonates 56:Background 2041:Chemistry 1962:: 18–25. 1941:1466-8033 1802:1930-1855 1762:1930-1855 1722:ignored ( 1712:cite book 1662:cite book 1603:ignored ( 1593:cite book 1426:0149-2136 1329:ignored ( 1319:cite book 1277:1064-668X 1204:ignored ( 1194:cite book 1107:cite book 491:Trevorite 449:Magnetite 356:pectolite 340:gehlenite 311:Silicates 304:Periclase 253:Beerstone 218:bassanite 202:Anhydrite 184:aragonite 124:chlorites 50:limescale 2017:37031132 1976:22079106 1906:12453728 1844:25129728 1686:All Days 1567:All Days 1513:: 8–14. 1293:All Days 1168:All Days 580:) ions. 553:O and CO 441:tenorite 417:noselite 409:Analcite 383:corundum 379:diaspore 375:gibbsite 371:Boehmite 367:AlO(OH) 336:gyrolite 163:Mineral 120:sulfides 116:sulfates 1479:Bibcode 751:Where F 433:cuprite 323:) · y H 289:Brucite 228:· 0.5 H 180:Calcite 33:aqueous 2015:  1974:  1939:  1904:  1842:  1800:  1760:  1700:  1650:  1581:  1424:  1307:  1275:  1182:  1095:  1067:  996:  745:= {}/K 666:↔ CaCO 443:(Cu ) 424:Copper 348:quartz 332:acmite 282:Mg(OH) 271:Barite 206:gypsum 104:brines 1820:(PDF) 831:DTPMP 716:→ MSO 627:2 HCO 618:+ HCO 612:3(aq) 602:3(aq) 586:2(aq) 571:3(aq) 555:2(aq) 547:2(aq) 315:Me(Si 212:· 2 H 208:(CaSO 157:Name 37:Scale 21:scale 2013:PMID 1972:PMID 1937:ISSN 1902:PMID 1840:PMID 1798:ISSN 1758:ISSN 1724:help 1698:ISBN 1668:link 1648:ISBN 1605:help 1579:ISBN 1552:link 1422:ISSN 1331:help 1305:ISBN 1273:ISSN 1239:link 1206:help 1180:ISBN 1126:link 1119:help 1093:ISBN 1065:ISBN 994:ISBN 814:ATMP 718:4(s) 714:(aq) 709:+ SO 707:(aq) 705:5. 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Index

scale
Scale inhibitors
precipitation
aqueous
oil industry
flow assurance
limescale

Paraffin wax
asphaltenes
gas hydrates
mineral deposits
brines
Supersaturation
carbonates
sulfates
sulfides
chlorites
retrograde solubility
Le Chatelier's principle
calcium hydroxide
portlandite
Calcium carbonate
Calcite
aragonite
Calcium sulfate
Anhydrite
gypsum
bassanite
hemihydrate

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