Low temperature switch oil and preparation method thereof
A switching oil, low temperature technology, used in the petroleum industry, base materials, lubricating compositions, etc., can solve the problems of less electrical switching oil, poor arc extinguishing effect, carbonization of oil products, etc., to achieve fast flow speed, reduce burning loss, Low pour point effect
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[0027] The following example is the preparation method of the low-temperature switch oil of the present invention, wherein the raw material is naphthenic crude oil and / or paraffin-based crude oil, and the relevant parameters of naphthenic crude oil and paraffin-based crude oil are shown in Table 1 below.
[0028] Table 1 Relevant parameters of naphthenic crude oil and paraffinic base crude oil
[0029] project naphthenic oil paraffinic base oil experiment method Kinematic viscosity at 40℃, mm 2 / s
Embodiment 1
[0031] 1. Catalyst presulfidation
[0032] The catalyst in this embodiment includes 4% of nickel oxide, 5% of molybdenum oxide, 3% of cobalt oxide, 3% of tungsten oxide and 85% of silicon oxide carrier according to weight percentage. Among them, the average pore diameter of the catalyst is The average pore volume is 0.2cm 3 / g, the average specific surface area is 190m 3 / g, the average strength is 100N / mm.
[0033] The above-mentioned catalyst is loaded into the hydrogenation reaction fixed-bed reactor and utilizes sulfurized oil to contain carbon disulfide CS 2 The kerosene is vulcanized, and the vulcanization process conditions are: hydrogen sulfide partial pressure 4MPa, vulcanization temperature 380°C, total space velocity 0.2h -1 , the volume ratio of hydrogen to oil is 800:1, and the vulcanization time is 15 hours. The presulfided catalyst is ready for use.
[0034] 2. Catalytic hydrogenation
[0035] This embodiment selects naphthenic crude oil as raw material, a...
Embodiment 2
[0043] 1. Catalyst presulfidation
[0044] The catalyst in this embodiment includes 10% of nickel oxide, 4% of molybdenum oxide, 2% of cobalt oxide, 7% of tungsten oxide and 77% of silicon oxide carrier according to weight percentage. Among them, the average pore diameter of the catalyst is The average pore volume is 1.5cm 3 / g, the average specific surface area is 250m 3 / g, the average strength is 60N / mm.
[0045] The above-mentioned catalyst is loaded into the hydrogenation reaction fixed-bed reactor and utilizes sulfurized oil to contain carbon disulfide CS 2 The kerosene is vulcanized, and the vulcanization process conditions are: hydrogen sulfide partial pressure 10MPa, vulcanization temperature 300°C, and total space velocity 1.5h -1 , the volume ratio of hydrogen to oil is 700:1, and the vulcanization time is 20 hours. The presulfided catalyst is ready for use.
[0046] 2. Catalytic hydrogenation
[0047] This embodiment selects naphthenic crude oil as raw mate...
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