SPE International Symposium on Oilfield Chemistry 1993
DOI: 10.2118/25211-ms
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Laboratory Acidization of an Eolian Sandstone at 380°F

Abstract: Formation damage was simulated by injecting completion fluid into cores and conditioning at 380°F (193°C) overnight. Low hydrofluoric (HF) acid concentrations from 0.05- to 0.1% blended with 10% acetic (HAc) effectively removed the damage. Some other acid systems we tested also worked well. Acidizing did not reduce the measured compressive strengths of the cores; however, microscopic analyses showed layers within the cores may have been seriously weakened.

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Cited by 25 publications
(4 citation statements)
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“…Calcium sulfate is a scale type that was found to have low solubility with high pH dissolvers . Also, dissolvers that have low pH will increase the tubular corrosion and therefore damage the facilities’ integrity. , Recent research studies are directed to provide chemical dissolvers with high pH to sustain the well downhole and surface equipment, processing units, and facilities; also, this will save the corrosion inhibitor and intensifier cost that is commonly added to the treatment operations for low pH dissolvers. , Ahmed et al added tetrakis hydroxymethyl phosphonium salts (THPS) to ethylenediaminetetraacetic acid (EDTA) to formulate a slightly alkaline chemical solution with about pH value of 8. Another recent research was executed and provided a chemical dissolver with a 12.5 pH value for composite sulfate/sulfide scale removal at low temperatures, and the results showed scale solubility efficiencies of 91.8% at 45 °C and 79% at 35 °C …”
Section: Scale Removalmentioning
confidence: 99%
See 1 more Smart Citation
“…Calcium sulfate is a scale type that was found to have low solubility with high pH dissolvers . Also, dissolvers that have low pH will increase the tubular corrosion and therefore damage the facilities’ integrity. , Recent research studies are directed to provide chemical dissolvers with high pH to sustain the well downhole and surface equipment, processing units, and facilities; also, this will save the corrosion inhibitor and intensifier cost that is commonly added to the treatment operations for low pH dissolvers. , Ahmed et al added tetrakis hydroxymethyl phosphonium salts (THPS) to ethylenediaminetetraacetic acid (EDTA) to formulate a slightly alkaline chemical solution with about pH value of 8. Another recent research was executed and provided a chemical dissolver with a 12.5 pH value for composite sulfate/sulfide scale removal at low temperatures, and the results showed scale solubility efficiencies of 91.8% at 45 °C and 79% at 35 °C …”
Section: Scale Removalmentioning
confidence: 99%
“…24 Also, dissolvers that have low pH will increase the tubular corrosion and therefore damage the facilities' integrity. 25,26 Recent research studies 27−30 are directed to provide chemical dissolvers with high pH to sustain the well downhole and surface equipment, processing units, and facilities; also, this will save the corrosion inhibitor and intensifier cost that is commonly added to the treatment operations for low pH dissolvers. 31,32 Ahmed et al 28 added tetrakis hydroxymethyl phosphonium salts (THPS) to ethylenediaminetetraacetic acid (EDTA) to formulate a slightly alkaline chemical solution with about pH value of 8.…”
Section: ■ Introductionmentioning
confidence: 99%
“…It is also common for investigators to use continuous interpretation and report their results as the ratio of current to initial permeability k/k o , for example as shown in Fig. 2 in Wehunt, et al (1993). When pseudo-continuous results are presented as k/k o , the usual assumption is that viscosity is constant and it can be neglected; however, this is not always-and perhaps not even usually-true.…”
Section: Pressure Data Interpretationmentioning
confidence: 99%
“…Organic acids have been extensively used in the acid stimulation of hydrocarbon reservoirs (Harris 1961;Scheuerman 1988;Wehunt et al 1993;Fredd and Fogler 1998;Shuchart and Gdanski 1996;Coulter and Jennings 1997;Nasr-El-Din et al 1997;da Motta et al 1998;Huang et al 2000a, 200b;Wang et al 2000;Nasr-El-Din et al 2001;Frenier 1989;Hashem et al 1999;van Domelen and Jennings 1995;Smith et al 1970;Chatelain et al 1976). The use of a combination of organic and inorganic acids dates back to 1978 (Dill and Keeney 1978).…”
Section: Introductionmentioning
confidence: 99%