2018 Spring Meeting and 14th Global Congress on Process Safety
(90d) Effect of Crude Oil on the Reaction Kinetics of Diesel Emulsified Acid with Calcite at High-Pressure and High-Temperature HPHT
In this work, two sets of reaction kinetic experiment were conducted using rotating disk apparatus RDA. The first set of oil-saturated disks, and the second for dry calcite ones. Emulsified acid was prepared using acid to diesel ratio of 70:30, emulsifier concentration and corrosion inhibitor were used in 1 vol.% and 0.3 vol. % respectively. Compositional analysis for diesel was done. Limestone core samples from local outcrop were used after checking its purity using XRD and XRF analysis. A small disk of 1.5 in. the diameter and 0.75 in. the length was prepared. The saturation by crude oil was made by soaking the disks in crude oil for 48 hours at 65âC. All the rotating desk experiments were conducted at 3000psi and 135âC. The disk rotational speed varied between (200-1500 rpm). Effluent samples of 5 ml were taken every two minutes and then analyzed through Inductively coupled plasma mass spectrometry (ICP-MS). The dissolution rate was measured at each RPM an
From the lab results a couple of two conclusions were drawn, firstly the Diffusion coefficient of H+(De) value at HPHT is much lower than those obtained at low-pressure low- temperature LPLT and the extrapolation of these De values at lower downhole conditions for deep reservoirs could lead to severe acidizing and hydraulic fracturing design inaccuracy. Secondly, two De values were observed for oil saturated limestone reaction kinetics, one for lower RPM where crude oil saturation effect is highly impacting the diffusion and leading to lower reaction, whereas at higher ones the (De) value is almost close to the (De) value for dry calcite rock.
To sum up, from lab results and for better acidizing modeling Itâs recommended to use diffusion coefficient (De) calculated using disks saturated with reservoir fluids at downhole conditions.