Method for calculating methane-carbon dioxide-propane mixed gas diffusion coefficient by considering volume expansion of thickened oil
A technology of carbon dioxide and calculation methods, applied in the direction of climate sustainability, other gas emission reduction technologies, instruments, etc., can solve the problem of inapplicable, methane-carbon dioxide-propane mixed gas diffusion behavior research has not been involved, it is difficult to accurately describe the gas diffusion expansion effects, etc.
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Embodiment 1
[0113] A method for the diffusion coefficient of methane-carbon dioxide-propane mixture considering the volume expansion of heavy oil, the calculation model principle is as follows figure 1 As shown, the calculation flow chart is as figure 2 As shown, the calculation is performed as follows:
[0114] The calculation method of the diffusion coefficient of methane-carbon dioxide-propane mixture considering the volume expansion of heavy oil includes the following steps:
[0115] Step 1. Determine the reservoir temperature T and the initial injection pressure P(t 0 ), the initial gas phase height of the mixture h g (t 0 ), the height of the diffusion experiment vessel H, the oil-gas interface area S, and the mass of heavy oil m o ;
[0116] The relative molecular mass of each component: M 1 is the relative molecular mass of propane, M 2 is the relative molecular mass of carbon dioxide, M 3 is the relative molecular mass of methane, M 4 is the relative molecular mass of h...
Embodiment 2
[0208] A calculation method for the diffusion coefficient of methane-carbon dioxide-propane mixture considering the volume expansion of heavy oil.
[0209] A calculation method for the diffusion coefficient of methane-carbon dioxide-propane mixture considering the volume expansion of heavy oil as described in Example 1, the difference is that the initial injection of the heavy oil injection methane-carbon dioxide-propane mixture diffusion experiment is changed Pressure, the initial injection pressure is set as 8.65 and 10MPa to carry out the experiment respectively, calculate methane-carbon dioxide-propane mixed gas diffusion coefficient and average gas phase concentration according to the calculation steps of embodiment 1, the result is as follows Figure 18 and Figure 19 shown.
[0210] Effect example
[0211] In order to verify the accuracy of the calculation results obtained by the present invention, the average gas phase concentration in the heavy oil at each moment wa...
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