A method for integrating production and transportation of heavy oil with hydrothermal catalytic upgrading and viscosity reduction
A technology of modification and viscosity reduction and thermal catalysis, which is applied in the direction of mining fluid, earthwork drilling, wellbore/well parts, etc., which can solve the problems of complex process and high catalytic modification temperature, and achieve simple process and good viscosity reduction effect , to reduce the effect of gravity resistance
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Embodiment 1
[0033] Using the method of the preferred embodiment of the present invention, a certain oilfield heavy oil (with a viscosity of 8800 mPa.s at 50°C and a water content of 9.36%) is exploited and hydrothermally catalytically upgraded to reduce viscosity. The test conditions and test results are as follows.
[0034] Blending thinner and reducing viscosity: The mass ratio of the viscosity-reducing oil to the thick oil used for mixing is 1:5, and the viscosity of the produced thinner and thick oil is 765mPa.s.
[0035] Hydrothermal catalytic upgrading: the catalyst is nickel sulfate, the dosage is 0.05wt% of the weight of the thin heavy oil; the hydrogen donor is tetralin, the dosage is 0.5wt% of the weight of the thin heavy oil; the reaction temperature is 160℃, the reaction The time is 6h; after the reaction, a part of the viscosity-reducing oil is returned to the wellbore of the oil well according to the above-mentioned mixing ratio for mixing and viscosity-reducing, and the remainin...
Embodiment 2
[0037] The method of the preferred embodiment provided by the present invention is used to exploit and reduce the viscosity of a certain oil field heavy oil (with a viscosity of 12780 mPa.s at 50°C and a water content of 15.78%). The test conditions and test results are as follows.
[0038] Blending thinner and reducing viscosity: The mass ratio of the viscosity-reducing oil to the thick oil used for mixing is 1:3, and the viscosity of the produced thinner and thick oil is 2645mPa.s.
[0039] Hydrothermal catalytic upgrading: the catalyst is ferrous acetylacetonate, the dosage is 0.05wt% of the weight of thin heavy oil; the hydrogen donor is formic acid, the dosage is 1.0wt% of the weight of thin heavy oil; the reaction temperature is 200℃, The time is 12h; after the reaction, part of the viscosity-reducing oil is returned to the wellbore of the oil well according to the above-mentioned mixing ratio for mixing and viscosity-reducing, and the remaining part is exported. The viscosi...
Embodiment 3
[0041] The method of the preferred embodiment provided by the present invention is used to exploit and reduce the viscosity of a certain oil field heavy oil (50°C viscosity of 30780 mPa.s, water content of 5.13%). The test conditions and test results are as follows.
[0042] Blending thinner and reducing viscosity: The mass ratio of the viscosity-reducing oil to the heavy oil used for mixing is 1:2, and the viscosity of the produced thinning and thick oil is 4459mPa.s.
[0043] Hydrothermal catalytic upgrading: the catalyst is vanadyl sulfate, the dosage is 0.2wt% of the weight of thin heavy oil; the auxiliary is cyclohexanone, the dosage is 1.0wt% of the weight of thin heavy oil; the reaction temperature is 240℃, and the reaction The time is 24h; after the reaction, a part of the viscosity-reducing oil is returned to the wellbore of the oil well according to the above-mentioned mixing ratio for mixing and viscosity-reducing, and the rest is transported. The viscosity of the reduc...
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