Author:
Murtaza Mobeen,Alarifi Sulaiman A.,Rasm Mohammed Yousef,Kamal Muhammad Shahzad,Mahmoud Mohamed,Al-Ajmi Mohammed
Abstract
AbstractCalcium sulfate (CaSO4) scale has been identified as one of the most common scales contributing to several serious operating problems in oil and gas wells and water injectors. Removing this scale is considered an economically feasible process in most cases as it enhances the productivity of wells and prevents potential severe equipment damage. In this study, a single-step method utilizing potassium carbonate and tetrapotassium ethylenediaminetetraacetate (K4-EDTA) at high temperature (200 °F) has been used to remove CaSO4 scale. The CaSO4 scale was converted to calcium carbonate (CaCO3) and potassium sulfate (K2SO4) using a conversion agent, potassium carbonate (K2CO3), at a high temperature (200 °F) and under various pH conditions. Various parameters were investigated to obtain a dissolver composition at which the optimum dissolution efficiency is achieved including the effect of dissolver pH, soaking time, the concentration of K4-EDTA, the concentration of potassium carbonate (K2CO3), temperature impact and agitation effect. Fourier transform infrared, X-ray crystallography, ion chromatography, stability tests and corrosion tests were carried out to test the end product of the process and showcase the stability of the dissolver at high temperature conditions. A reaction product (K2SO4) was obtained in most of the tests with different quantities and was soluble in both water and HCl. It was observed that the dissolver solution was effective at low pH (7) and resulted in a negligible amount of reaction product with 3 wt% CaSO4 dissolution. The 10.5-pH dissolver was effective in most of the cases and provided highest dissolution efficiency. The reaction product has been characterized and showed it is not corrosive. Both 7-pH and 10.5-pH dissolvers showed high stability at high temperature and minimum corrosion rates. The single step dissolution process showed its effectiveness and could potentially save significant pumping time if implemented in operation.
Publisher
Springer Science and Business Media LLC
Reference28 articles.
1. Frenier, W. Formation, removal, and inhibition of inorganic scale in the oilfield environment. Society of Petroleum Engineers. ISBN 978-1555631406 (2008).
2. Mitchell, R. W., Grist, D. M. & Boyle, M. J. Chemical treatments associated with north sea projects. Soc. Pet. Eng. 32(5), 904–912 (1980).
3. Smit, L. Removal and inhibition of calcium sulfate scale in waterflood projects. In SPE Paper Presented at the SPE 42nd Annual Fall Meeting held in Houston, USA, October 1–4 (1967).
4. Al-Khaldi, M. H., Al-Juhani, A. M., Al-Mutairi, S. H., M. N. Gurmen. New insights into the removal of calcium sulfate scale. In Paper presented at the SPE European Formation Damage Conference, Noordwijk, The Netherlands. https://doi.org/10.2118/144158-MS (2011).
5. Binmerdhah, A. & Yassin, A. Laboratory study and prediction of calcium sulphate at high-salinity formation water. Open Pet. Eng. J. 1, 62–73. https://doi.org/10.2174/1874834100801010062 (2008).
Cited by
11 articles.
订阅此论文施引文献
订阅此论文施引文献,注册后可以免费订阅5篇论文的施引文献,订阅后可以查看论文全部施引文献