Hydrophobic Paramagnetic Nanoparticles as Intelligent Crude Oil Tracers
US-2015376493-A1 · Dec 31, 2015 · US
US9785802B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9785802-B2 |
| Application number | US-201113994157-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 7, 2011 |
| Priority date | Dec 17, 2010 |
| Publication date | Oct 10, 2017 |
| Grant date | Oct 10, 2017 |
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Method of modelling the evolution of the pH value of a porous medium after injection of an alkaline agent solution into this medium. The alkaline agent is considered as a soda pseudo-constituent of concentration equal to an OH— concentration corresponding to the pH value of the alkaline agent solution injected. An adsorption equation calibrated to experimental data is then used to determine an amount of soda pseudo-constituent adsorbed, from the concentration of the soda pseudo-constituent. Finally, the evolution of the pH value is modelled by modelling the transport of the alkaline agent solution by means of a soda transport simulator, by replacing the soda by the soda pseudo-constituent.
Opening claim text (preview).
The invention claimed is: 1. A method for enhanced recovery of hydrocarbons contained in a porous medium provided underground, comprising a technique of sweeping the porous medium by an aqueous solution comprising at least one chemical product intended to improve sweeping of the porous medium, wherein an amount of a buffer alkaline agent solution comprising a buffer alkaline agent is additionally introduced so as to limit the adsorption of the at least one chemical product, characterized in that the amount of the buffer alkaline agent to be injected is determined by carrying out the following stages: modelling an evolution of a pH value in the porous medium after injection of an amount of the buffer alkaline agent solution into the porous medium, by using a flow simulator modelling a transport of the buffer alkaline agent solution through the porous medium, characterized in that: during the modelling, the buffer alkaline agent is considered as a soda pseudo-constituent of concentration equal to an OH— concentration corresponding to the pH value of the buffer alkaline agent solution injected, an OH— ions adsorption equation depending on parameters to be calibrated is used, this equation being calibrated to experimental data for determining an amount of soda pseudo-constituent adsorbed from the concentration of the soda pseudo-constituent, wherein the adsorption equation has the form of a Langmuir isotherm relative to an OH— concentration, the adsorption equation is written as follows: C r OH - = q ma x k e · C w OH - 1 + k e · C w OH - with: C w OH— : amount, concentration, of the soda pseudo-constituent in the buffer alkaline agent solution C r OH— : amount, mass fraction, of the soda pseudo-constituent adsorbed q max , K e : parameters of the adsorption equation to be calibrated, and calibration of the adsorption equation is performed by applying the following stages: determining an experimental pH profile describing a pH evolution as a function of a volume of solution injected, by injecting the buffer alkaline agent solution into a sample of the porous medium, and by measuring the pH value of effluents leaving the sample, determining a simulated pH profile by modelling the injection of the buffer alkaline agent solution into the sample with the flow simulator and the adsorption equation, modifying parameters of the adsorption equation until differences between the simulated profile and the experimental profile are minimized, the evolution of the pH value is modelled by modelling the transport of the buffer alkaline agent solution using the determined amount of soda pseudo-constituent adsorbed and the flow simulator, by considering the buffer alkaline agent to be the soda pseudo-constituent, repeating the modelling of an evolution of the pH value for various amounts of the buffer alkaline agent solution injected, selecting the amount of the buffer alkaline agent solution to be added so as to optimize the enhanced recovery of hydrocarbons. 2. The method according to claim 1 , the simulated pH profile being further determined using the following formula (4): pH= pKw =log( C w OH− ) (4).
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