Heavy oil product treatment processing method
A technology for processing technology and oil products, which is applied in the field of combined process for processing heavy oil, and can solve problems such as the inability to fundamentally change the pressure drop growth trend of the pre-reactor and the unfavorable stable operation of the device.
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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 solvent deasphalting unit to obtain deasphalted oil and deoiled asphalt. The obtained deasphalted oil and light fraction, 50% of the catalytic cracking diesel and all the catalytic cracking heavy cycle oil of the catalytic cracking unit are sent 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 reactor C are exactly the same, and the hydrogenation pretreatment ...
Embodiment 2
[0079] 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 obtained heavy fraction is processed through a solvent deasphalting unit to obtain deasphalted oil and deoiled asphalt. The deasphalted oil and light fraction, 30% of the catalytic cracking diesel and all the catalytic cracking heavy cycle oil of the catalytic cracking unit are sent to the hydropretreatment reaction zone. The total catalyst loading and feed properties of the hydrogenation pretreatment reactor A, hydrogenation pretreatment reactor B, and hydrogenation pretreatment reactor C are exactly the same, and the feed space velocity is differe...
Embodiment 3
[0081] 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 600°C. Then, the obtained heavy fraction is processed through a solvent deasphalting device to obtain deasphalted oil and deoiled asphalt. The hydrogenation pretreatment reactor A adopts the deasphalted oil of raw material A, the hydrogenation pretreatment reactor B adopts the deasphalted oil of raw material B, and the hydrogenation pretreatment reactor C adopts the deasphalted oil of raw material C. The feed amount of described hydrogenation pretreatment reactor A, hydrogenation pretreatment reactor B, hydrogenation pretreatment reactor C is the same, and described hydrogenation pretreatm...
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