Production method for extra high voltage transformer oil
A technology for transformer oil and production method, applied in the petroleum industry, hydrocarbon oil treatment, hydrotreating process and other directions, can solve the problems of reducing the yield of the target product, environmental problems, etc., and achieve the effect of improving the product yield
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Embodiment 1
[0025] This example illustrates the effect of the method provided by the present invention.
[0026] The feed oil is naphthenic distillate at atmospheric pressure, and its properties are shown in Table 1. 300 ml of hydrotreating catalyst A and 150 ml of hydrotreating catalyst B were loaded into two fixed-bed hydrogenation reactors I and II respectively. Catalysts A and B are presulfurized before the raw material oil is passed through. The vulcanized oil is kerosene containing 2.0% by weight of carbon disulfide. The vulcanization conditions are: hydrogen partial pressure 12 MPa, temperature 370°C, total space velocity 1.0h 400, curing time 15 hours.
[0027] After presulfurization, the feed oil is switched through reactors I and II in sequence. The reaction conditions in the controlled hydrotreating reaction zone are: hydrogen partial pressure 12 MPa, temperature 340°C, space velocity 0.6h -1 , the ratio of hydrogen to oil is 800:1; the reaction conditions in the controlled ...
Embodiment 2
[0034] The feed oil is naphthenic distillate at atmospheric pressure, and its properties are shown in Table 3. 375 g of hydrotreating catalyst A and 110 g of hydrofinishing catalyst B were respectively loaded into two series-connected fixed-bed hydrogenation reactors I (300 ml) and II (150 ml). Catalysts A and B were presulfurized according to the method in Example 1 before the raw material oil was passed through.
[0035] After presulfurization, the feed oil is switched through reactors I and II in sequence. The reaction conditions in the controlled hydrotreating reaction zone are: hydrogen partial pressure 12 MPa, temperature 355°C, space velocity 0.4h -1 , the ratio of hydrogen to oil is 800:1; the reaction conditions in the controlled hydrofining reaction zone are: hydrogen partial pressure 12 MPa, reaction temperature 240°C, space velocity 0.8h -1 , the ratio of hydrogen to oil is 800:1, and the total space velocity is 0.27h -1 . The resulting oil is distilled to obta...
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