Process method for treating residual oil
A process method and residual oil technology, which can be used in hydrotreating process, hydrocarbon oil treatment, petroleum industry, etc., can solve problems such as unfavorable stable operation of devices and inability to fundamentally change the growth trend of pressure drop in pre-reactors.
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Embodiment 1
[0077] The properties of the raw material A used in Example 1 are shown in Table 1. After mixing with hydrogen, it enters the hydrogenation pretreatment device for hydrogenation pretreatment. The reaction temperature is 377 °C and the volume space velocity is 0.4h. -1 , the reaction pressure is 16MPa, the oil produced by the reaction is separated to obtain light fraction and heavy fraction, and the cut point is 620°C. The heavy fraction is processed through a coking unit, and then separated to obtain coked gasoline, coked diesel oil, coked wax oil and coke. The operating conditions of coking are: reaction temperature 505°C, pressure 170000Pa.
[0078] Send coker wax oil and light fraction, 30% catalytic cracked diesel and all catalytic cracked heavy cycle oil to the hydrogenation pretreatment reaction zone. The total catalyst loading, feed properties and feed amount of the hydropretreatment reactor A, hydrogenation pretreatment reactor B, and hydrogenation pretreatment reacto...
Embodiment 2
[0080] In Example 2, the properties of the raw material B used are shown in Table 1. After mixing with hydrogen, it enters the hydrogenation pretreatment device for hydrogenation pretreatment reaction. The reaction temperature is 375°C and the volume space velocity is 0.40h. -1 , the reaction pressure is 16MPa, the oil produced by the reaction is separated to obtain light fraction and heavy fraction, and the cut point is 610°C. The heavy fraction is processed through a coking unit, and then separated to obtain coked gasoline, coked diesel oil, coked wax oil and coke. The operating conditions of coking are: reaction temperature 505°C, pressure 170000Pa.
[0081] Send coker wax oil, light distillate oil and light distillate, as well as 20% catalytic cracked diesel oil and all catalytic cracked heavy cycle oil from the catalytic cracking unit to the hydrotreating reaction zone. The total catalyst loading and feed properties of the hydrogenation pretreatment reactor A, hydrogenat...
Embodiment 3
[0083] In Example 3, raw materials A, B, and C were mixed with hydrogen and then entered into respective hydrogenation pretreatment devices for hydrogenation pretreatment. The reaction temperature was 380°C and the volume space velocity was 0.4h -1 , the reaction pressure is 16MPa, the oil produced by the reaction is separated to obtain light fraction and heavy fraction, and the cut point is 608°C. The heavy fraction is processed through a coking unit, and then separated to obtain coked gasoline, coked diesel oil, coked wax oil and coke. The operating conditions of coking are: reaction temperature 505°C, pressure 170000Pa.
[0084] The hydropretreatment reactor A adopts the coker gas oil of raw material A and the light fraction of A, the hydropretreatment reactor B adopts the coker gas oil of raw material B and the light fraction of B, and the hydropretreatment reactor C adopts Feedstock C coker gas oil and C light fractions. The feed amount of described hydrogenation pretre...
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