Search citation statements
Paper Sections
Citation Types
Year Published
Publication Types
Relationship
Authors
Journals
Scale dissolvers for CaSO4, are composed of chelants, including aminocarboxylates or phosphonates, and can contain lower concentrations of other chemical additives (enhancers) that improve dissolution. We investigate the effectiveness of enhancers, whose function is to increase the dissolution rate, by examining the effect of substituted acetates. The objective is to elicit the chemical properties that make an enhancer effective, identify costs, safety considerations, and validate their application and limitations for field use. Two types of mineral anhydrite and nine enhancer agents were used in static dissolution tests. Thin slabs were soaked in dissolver fluids, including a converter agent, at a pH between eight and ten. The enhancer concentration spanned 0.5, 5, and 10% w/v and probed both the catalytic and inhibitory effects. The dissolver was selected and optimized based on a customized screening methodology. Tests with mass/volume ratios of 0.1 and 0.02 were employed to fit mass-loss data to a kinetic model and rank the general rates of dissolution, which indicate there is a favorable chemical enhancer type of additive. Mass-loss rates using two types of anhydrite, obtained at 200°F from one to six hours, indicate strong enhancer activity. Distinctive effects are found depending on the chemical substituent on the enhancer agent. Dissolution of anhydrite shows significantly different rates at 1 hour and mass-limiting effects with no differentiation for m/v = 0.02 at four hours and nearly a similar initial rate at one hour for m/v = 0.1. A significant differentiation is observable after one hour. Inhibitory effects are discernable at high concentrations (10% enhancer). The type of substrate also shows differences in dissolution activity among blue and grey anhydrite. We found a strong correlation with the dissolver enhancer chemical type, indicating a chemical class of agents that could have applicability in descaling operations. The enhancers have been ranked by health and safety characteristics and cost to assess the feasibility of use in oilfield environments. The use of enhancer agents in scale dissolver fluids can provide dissolution within one to four hours, helping shorten the shut-in period for this treatment. Tests show that including highly polarizable agents can lead to faster dissolution of anhydrite.
Scale dissolvers for CaSO4, are composed of chelants, including aminocarboxylates or phosphonates, and can contain lower concentrations of other chemical additives (enhancers) that improve dissolution. We investigate the effectiveness of enhancers, whose function is to increase the dissolution rate, by examining the effect of substituted acetates. The objective is to elicit the chemical properties that make an enhancer effective, identify costs, safety considerations, and validate their application and limitations for field use. Two types of mineral anhydrite and nine enhancer agents were used in static dissolution tests. Thin slabs were soaked in dissolver fluids, including a converter agent, at a pH between eight and ten. The enhancer concentration spanned 0.5, 5, and 10% w/v and probed both the catalytic and inhibitory effects. The dissolver was selected and optimized based on a customized screening methodology. Tests with mass/volume ratios of 0.1 and 0.02 were employed to fit mass-loss data to a kinetic model and rank the general rates of dissolution, which indicate there is a favorable chemical enhancer type of additive. Mass-loss rates using two types of anhydrite, obtained at 200°F from one to six hours, indicate strong enhancer activity. Distinctive effects are found depending on the chemical substituent on the enhancer agent. Dissolution of anhydrite shows significantly different rates at 1 hour and mass-limiting effects with no differentiation for m/v = 0.02 at four hours and nearly a similar initial rate at one hour for m/v = 0.1. A significant differentiation is observable after one hour. Inhibitory effects are discernable at high concentrations (10% enhancer). The type of substrate also shows differences in dissolution activity among blue and grey anhydrite. We found a strong correlation with the dissolver enhancer chemical type, indicating a chemical class of agents that could have applicability in descaling operations. The enhancers have been ranked by health and safety characteristics and cost to assess the feasibility of use in oilfield environments. The use of enhancer agents in scale dissolver fluids can provide dissolution within one to four hours, helping shorten the shut-in period for this treatment. Tests show that including highly polarizable agents can lead to faster dissolution of anhydrite.
Removal of wellbore scale from downhole equipment continues to impact well economics due to productivity losses and asset maintenance. The use of first-of-its-class calcium sulfate (CaSO4) scale dissolver in high producing offshore wells equipped with electric submersible pumps (ESP) is presented. The efficiency of the new fluid surpasses the performance of established dissolvers since it does not require long shut-in periods. Anhydrite (CaSO4) scale dissolution and removal can be accomplished with a simple treatment fluid employing a formulation that has been field-proven to restore production and protect downhole equipment in a time-efficient manner. Mineral anhydrite and wellbore scale samples were tested with the dissolver formulation at 200°F (93.3°C), under static conditions for one hour. Dissolution efficiencies greater than 94% were a requirement. Fluid compatibility with metallic and non-metallic components in the wellbore were assessed at bottom hole static temperature (BHST) conditions for a period of 24 hours. The fluid was deployed from a stimulation vessel at a pumping rate from 1 to 5 bpm. A small volume pill of 5 m3 on average was pumped in at least 20 wells, through the production tubing to the ESP and was allowed to soak for 1 hour. Wells were immediately opened to production after a 1-h soak period. Minimizing the non-productive time incurred when long soak periods are required has been attained with the use of the new dissolver fluid, leading to greater efficiencies associated with CaSO4-type scale removal. ESP temperature was monitored and reduced by 13°F (7.2°C) after treatment, similar to temperatures before scale build up. After the treatment, the results show a 1.125-fold increase in oil production. The fast-acting formulation exceeds 90% dissolution efficiency within one hour and improves operations by using a fluid that is non-corrosive to downhole materials in a one-stage removal package. The dissolver formulation provides dissolution of anhydrite at 200°F in ESPs. The fast acting dissolver is delivered as a single fluid package and eliminates the need for separate fluid stages as well as the use of incompatible fluids. Anhydrite scale dissolution and removal can be accomplished with a simple treatment fluid and extend the life of the ESP.
Summary Issues such as high corrosion rate, hydrogen sulfide (or H2S) generation, and scale reprecipitation have required the use of alternative dissolvers such as tetrakis(hydroxymethyl)phosphonium sulfate (THPS)–ammonium chloride (or NH4Cl) blend and chelating agents to dissolve iron sulfide (or FeS) scales. However, there are many aspects of these dissolvers that need investigation. This paper provides a guideline to select the best dissolver under various oilfield conditions by an extensive laboratory study. Furthermore, the iron sulfide scale removal is enhanced by the use of new synergists to the chelating agents. The application of THPS and diethylenetriaminepentaacetic acid (DTPA) in well tubulars or pipelines requires laboratory testing to determine the optimal conditions such as dissolver concentration, treatment time, and dissolver/scale (D/S) ratio (cm3/g) at 150°F. This evaluation considers oil-wet scales, mixed scales, presence of additives, and presence of salts during the treatment. Synergists such as potassium chloride (or KCl), potassium iodide (or KI), potassium formate (or HCOOK), sodium fluoride (or NaF), and potassium citrate (or K-Citrate) were added to ethylenediaminetetraacetic acid (EDTA), DTPA, and hydroxyethylethylenediaminetriacetic acid (HEDTA), and the scale solubility was evaluated at 150 and 300°F. Inductively coupled plasma–optical emission spectrometer analysis of the supernatant solution at various intervals of time up to 48 hours revealed the kinetics of the dissolution process. H2S generated from the scale dissolution process was measured using Draeger tubes. Corrosion tests helped in measuring the damage to the tubulars as a result of the dissolver’s contact with N-80coupons. Solubility tests indicated the dissolver’s scale removal capacity at different concentrations. The work also accounted for the consumption of the dissolver for the scale removal. The optimal blend was chosen considering both the dissolution capacity and the dissolver consumption. For THPS–ammonium chloride blend, 0.75 mol/L THPS (30 wt%) and 2 mol/L NH4Cl (10 wt%) proved to be the optimum dissolver concentration at 150°F. Similarly, for DTPA, 0.4 mol/L K2-DTPA was evaluated to be the most effective dissolver concentration. The THPS–ammonium chloride blend was found to dissolve the iron sulfide slowly compared with K2-DTPA and 15% hydrochloric acid (HCl). The presence of crude oil on the scale hindered its solubility with K2-DTPA by 8%. The presence of calcium carbonate influenced higher selectivity of chelating the calcium ions by K2-DTPA. However, the overall fraction of scale removal was not affected. Adding corrosion inhibitors (CIs) did not affect the scale solubility significantly and also helped in maintaining an acceptable corrosion rate of N-80 coupons below 0.05 lb/ft2 at 150°F. The reaction of HCl and the iron sulfide scale generated 1,800 ppm of H2S in comparison with 0- and 10-ppm by THPS–ammonium chloride blend and K2-DTPA, respectively. Adding potassium iodide and potassium citrate to EDTA helped in improving the scale solubility at 150°F. Sodium fluoride improved the scale dissolution by EDTA and DTPA at 300°F. This paper addresses oilfield-like conditions on scale solubility by evaluating the role of mixed scale, scale mass, presence of hydrocarbons on the scale, and presence of monovalent/divalent ions in dissolver solution. A detailed and direct comparison of HCl, THPS–ammonium chloride blend, and DTPA in dissolving iron sulfide at various conditions enables easier selection of the dissolver for a field treatment. New synergists for iron sulfide scale dissolution are introduced in this paper. This work can help oilfield companies understand the nuances of applying different alternative iron sulfide dissolvers.
scite is a Brooklyn-based organization that helps researchers better discover and understand research articles through Smart Citations–citations that display the context of the citation and describe whether the article provides supporting or contrasting evidence. scite is used by students and researchers from around the world and is funded in part by the National Science Foundation and the National Institute on Drug Abuse of the National Institutes of Health.
customersupport@researchsolutions.com
10624 S. Eastern Ave., Ste. A-614
Henderson, NV 89052, USA
This site is protected by reCAPTCHA and the Google Privacy Policy and Terms of Service apply.
Copyright © 2024 scite LLC. All rights reserved.
Made with 💙 for researchers
Part of the Research Solutions Family.