The formation of mineral scale is one of the technical challenges that directly impacts well productivity and economic viability. Thermodynamically, scale forms due to a disruption in the equilibrium between formation water, injection water, and reservoir rock caused by extreme changes in physical conditions as the fluid moves from the reservoir to the surface (Kamal et al., 2018; Zakir-Hassan et al., 2022). 

A drop in pressure and changes in temperature cause formation water to lose its ability to dissolve minerals, making the water supersaturated, which triggers the deposition of mineral crystals on pipe walls and subsurface equipment. Calcium carbonate (CaCO₃) is the most common type of scale found in oil wells, including in the Pendopo Field. The formation of calcium carbonate scale is significantly influenced by the release of carbon dioxide (CO₂) and reservoir fluids. When CO₂ is present,the pH of the water increases, thereby accelerating the crystallization reaction and triggering CaCO₃ precipitation. In wells using Electric Submersible Pumps (ESPs), this condition is highly dangerous because scale not only blocks the flow path but also disrupts pump performance. The ESP motor's load changes dynamically due to the additional resistance caused by scale. Noul-Mehidi and Bukhamseen (2019) demonstrated that rapid scale buildup on the pump stages can be identified through fluctuations in the motor current signal. This symptom typically appears several weeks before total failure of the ESP system occurs. In other words, monitoring the motor current signal can serve as an early indicator to anticipate failures caused by scale.

Issues with the integrity of Electric Submersible Pumps (ESPs) in wells with high levels of mechanical impurities and a tendency for scale formation are the primary factors limiting the equipment's service life. In addition to mechanical damage caused by dynamic torsional stress during startup with a soft-starter system (Rabbi et al., 2020), the pump is also susceptible to hydro-abrasive wear on the impeller and diffuser due to solids, so that the ESP's service life can be drastically reduced sometimes lasting only a few days (Shishlyannikov et al., 2021). Well AWH-02 at the Pendopo Field has historically faced similar issues. Aggressive scale deposits have caused premature ESP failure. This condition requires well intervention (well service) at a very high cost

To date, scale removal has generally relied on hydrochloric acid (HCl). However, the use of HCl poses risks due to its highly corrosive nature toward the ESP's metal components and its adverse environmental impacts (Kamal et al., 2018; Ahmad et al., 2018). Research by Garcia-Olvera et al. (2018) indicates that the use of chelating agents as an alternative scale remover is safer. These agents can dissolve mineral deposits without damaging either the metallic or non-metallic materials of the ESP. Furthermore, this method can significantly increase production without damaging the equipment. As an innovative and sustainable solution, this study evaluates the use of an organic scale inhibitor based on areca nut (Areca catechu) extract. Areca nuts are rich in polyphenol and tannin compounds, which possess free hydroxyl groups and thus act as natural chelating agents (Vanimakhal & Balasubramanian, 2016). The primary mechanism involves binding to ions and disrupting crystal growth, thereby preventing the formation of mineral deposits (Wang et al., 2021). This paper aims to evaluate the effectiveness of this green technology at Well AWH-02, encompassing laboratory efficiency tests and economic simulations to establish new standards for effective, economical, and environmentally friendly scale management.

The AHW-02 well is a directional well with artificial lift issues using an Electric Submersible Pump (ESP). This well has a total depth of 2482 mMD. The well structure consists of 20” casing at a depth of 103 mMD, 13-3/8” casing at 405.6 mMD, 9-5/8” casing at 1800 mMD, 7” liner from 1516.12 to 2,306 mMD, and a 4-1/2” liner from 2,198.96 to 2,482 mMD. Well AWH-02 produces from the productive Batu Raja Formation (BRF) in the South Sumatra Basin, with an average oil production of approximately 30 BOPD and total (gross) fluid production of approximately 650 BFPD. However, this well has a high water cut of 95.3%.

Fig. 1: Production History of Well AWH-02.

The BRF layer in the AHW structure consists primarily of limestone rich in calcium carbonate (CaCO₃). This makes the layer highly susceptible to scale formation. During the production process, particularly with the aid of artificial lift, there are significant changes in pressure and temperature within the fluid, causing the calcium carbonate to become unstable and prone to precipitation, which then forms scale. 

Fig. 1 shows the production history of Well AWH-02 with a Qmax of 811 BFPD. The production target for Well AWH-02 utilizes a Premiere brand ESP pump, type TD 750, operating at a frequency of 56 Hz; with 334 stages; at a pump set depth of 1,777 m, achieving an efficiency of 83%. During well servicing, scale formation was observed on the gas separator and inside the wellhead due to the accumulation of mineral scale deposits.

Production of Scale Inhibitor from Areca Nut Extract

The areca nut seed extract used as a scale inhibitor is produced by drying small pieces of areca nut seeds in the sun for approximately 2 weeks. Afterward, the seeds, which still contain moisture, are dried further in an oven until their weight remains constant, then ground into a fine powder using a blender. One gram of the powder is dissolved in distilled water to a total volume of 1 liter to produce a solution with an initial concentration of 1000 ppm. 

Fig. 2: Production Issues at Well AWH-02.

This solution is stirred using a magnetic stirrer for 2–3 hours at 90 °C, then filtered through filter paper to obtain a pure extract. From this initial solution, dilutions are prepared at 100 ppm, 200 ppm, and 300 ppm, which are then used as standards in laboratory testing of the inhibitor's effectiveness. Calculation of the Effectiveness of Areca Nut Scale Inhibitors in the Laboratory Laboratory test data were obtained using the bottle test (static test) titration method to determine the growth rate of CaCO₃in accordance with NACE TM0374-2001, with observations taken over a 30-minute period in a water bath at 90 °C. Once the results of the laboratory test were obtained, the percentage effectiveness of the areca nut scale inhibitor could be calculated using the following formula: Where: Ca = weight of the precipitate after the inhibitor was added at the equilibrium point (g/L) Cb = weight of the precipitate without the inhibitor at equilibrium (g/L) Cc = initial precipitate weight (g/L) From the test data of formation water from well AWH-02 without the addition of a scale inhibitor, the weight of CaCO3precipitate was found to be 2.842 grams/liter. Subsequently, testing of formation water from well AWH-02 using areca nut scale inhibitor at various concentrations (ppm) yielded CaCO₃ sediment weights of 2.275 grams/liter at a 100 ppm inhibitor dose, 2.192 grams/liter at a 200 ppm dose, and 2.078 grams/liter at a 300 ppm dose. The following table shows the results of the scale inhibitor tests in the laboratory. From this data, the percentage effectiveness of the areca nut scale inhibitor can be calculated. Scale inhibitor solution at a concentration of 100 ppm % Inhibitor Effectiveness =(100 × (2.275-2.842))/((0-2.482)) = 19.95% Scale inhibitor solution at a concentration of 200 ppm % Inhibitor Effectiveness =(100 × (2.192-2.842))/((0-2.482)) = 22.87% Scale inhibitor solution at a concentration of 300 ppm % Inhibitor Effectiveness =(100 × (2.078-2.842))/((0-2.482)) = 26.88% Planning and Implementation of Organic Scale Inhibitor Injection Scale inhibitor injection is planned for well AWH-02 to prevent mineral scale deposition, thereby extending the pump's service life. Based on laboratory test results, the effectiveness of the areca nut scale inhibitor was calculated to determine the optimal dosage. Based on the laboratory tests conducted, it was found that a dosage of 300 ppm is the optimal dosage for the initial reference of the organic scale inhibitor pilot project. A dosage of 300 ppm was selected because it demonstrated the highest scale inhibitor effectiveness value of 26.88%. The required injection volume can be calculated based on the optimal dose determined by comparing it with the estimated daily formation water production at a target flow rate of 80% of 811 BFPD, or 650 BWPD. With a scale inhibitor concentration of 300 ppm, the daily volume requirement for the chemical scale inhibitor is 31 liters per day. Dimana: LPD = Liters per day Ppm = Parts per million BFPD = Barrels of fluid per day LPD =((300×650×159))/1.000.000 LPD = 31 liters / day Economic Evaluation An economic evaluation was conducted to determine the economic viability of the production target for well AWH-02 in relation to the additional operating costs from the injection of organic scale inhibitor derived from areca nut extract, the investment cost of capillary tubes for injection into the well, and the reduction in well maintenance frequency resulting from the increased lifespan of the ESP pump in well AWH-02. Tabel 1 shows the costs required for the implementation of organic scale inhibitor injection using areca nut seed extract into the downhole of well AWH-02, assuming there are no costs for the chemical injection pump since it is company-owned equipment.

Table 1: Costs of Implementing Organic Areca Nut Scale Inhibitor Injection.