Method for refining Fischer-Tropsch synthetic oil
A refining method and a Fischer-Tropsch synthesis technology, which are applied in the petroleum industry, hydrocarbon oil treatment, hydrotreating process, etc., can solve the problems of the unfavorable effects of fixed-bed hydrogenation catalysts and many oxygen-containing compounds, and achieve the reduction of unfavorable effects. The effect of reducing the amount of production
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Embodiment 1
[0020] Take 1 part of high temperature condensate and 2.5 parts of low temperature condensate as oil for experiment.
[0021] The low-temperature condensate was taken, mixed fully according to the oil-water ratio of 2:1, and the washing temperature was 20°C. After natural sedimentation, the water phase was separated to obtain the low-temperature condensate after washing. The properties of the low-temperature condensate after washing are shown in Table 2.
[0022] Mix 1 part of the high-temperature condensate and the low-temperature condensate after washing with water, and the obtained mixed oil B is used as the raw material for hydrorefining. The properties of the mixed oil B are shown in Table 2.
[0023] From the data in Table 1 and Table 2, it can be seen that the oxygen content of the low-temperature condensate after water washing is reduced from 4.28% by weight to 3.12% by weight, and the oxygen removal rate reaches 27%; the oxygen content of the mixed oil is reduced from ...
Embodiment 2
[0027] Take 1 part of high temperature condensate and 2.5 parts of low temperature condensate as oil for experiment.
[0028] Take the low-temperature condensate, fully mix it according to the oil-water ratio of 2:1, wash with water at 20°C, separate the water phase after natural sedimentation, and obtain the low-temperature condensate after the first water wash, and then add the low-temperature condensate after the first water wash with 2: The oil-water ratio of 1 was fully mixed, and the washing temperature was 20°C. After natural sedimentation, the water phase was separated. The properties of the low-temperature condensate after the second washing are shown in Table 4.
[0029] Mix 1 part of the high-temperature condensate with the low-temperature condensate after the second water washing, and the obtained mixed oil C is used as the raw material for hydrorefining. The properties of the mixed oil C are shown in Table 4.
[0030] From the data in Table 1 and Table 2, it can b...
Embodiment 3
[0045] The mixed oil C is used as the raw material for hydrofining. The catalyst is RTF-1 developed by the Petrochemical Science Research Institute. Speed 2.0h -1 . The refined oil was sampled at different operating times to analyze its oxygen content. The results are shown in Table 6.
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