A method of delayed coking
A technology of delayed coking and coking raw materials, applied in the field of delayed coking, which can solve the problems affecting the operation cycle and operation stability and safety of coking equipment and downstream processes, affecting the separation effect of vacuum fractionation tower, and the liquid fraction is easy to contain coke powder, etc. Achieve the effects of improving the quality of coking products, increasing the yield of liquid products, and extending the operating cycle
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Embodiment 1
[0078] This embodiment adopts figure 1 The process flow, this embodiment illustrates the situation of using a higher circulation ratio of 0.4 and a higher furnace outlet temperature of 503°C.
[0079] Fresh coking raw material (vacuum residue) from pipeline 1 is mixed with part of fractionation tower bottom oil from pipeline 23, and then enters the convection section 2 and radiation section 4 of the heating furnace in sequence, and enters the top of the tower as a spherical head after heating up to 503°C coke tower 5 and carry out the coking reaction at 0.15MPa, and the circulation ratio is 0.4:1 (that is, the feed mass ratio of the fractionation tower bottom oil to the fresh coking raw material); 24h), the generated coked oil gas enters the cyclone separator 7 in a tangential manner, and the residence time of the coked oil gas in the cyclone separator is 1 minute. The mixture is injected into the top of the cyclone separator as washing oil (the mass ratio of the upper layer ...
Embodiment 2
[0081] This embodiment adopts figure 1 The flow process is carried out according to the method of Example 1, the difference is that after the fresh coking raw material (vacuum residue) from the pipeline 1 is mixed with the part fractionation bottom oil from the pipeline 23, it enters the heating furnace convection section 2, radiation Section 4, after heating up to 504°C, it enters the coke tower 5 with a spherical head at the top of the tower, and the circulation ratio is 0.1:1, the length of the coke tower feed position from the lower end of the cylinder accounts for 6 / 10 of the entire cylinder length; sedimentation The mass ratio of the lower layer oil in the tank to the feed of fresh coking raw materials is 0.02:1; the mass ratio of the washing oil injection to the feed of fresh coking raw materials is 0.04:1. The mass ratio of the bottom oil of the 22 partial fractionation tower is 1:1; the weight ratio of cooling oil and desalted water is 0.2:1, and the weight ratio of t...
Embodiment 3
[0083] In this embodiment, the attached figure 1 The flow process of the method is carried out according to the method of embodiment 1, and the difference is that after the fresh coking raw material (vacuum residue) from pipeline 1 is mixed with the part fractionation tower bottom oil from pipeline 23, it enters the heating furnace convection section 2 and radiation section successively 4. After heating up to 505°C, it enters the coke tower 5 with a spherical head at the top of the tower, and the circulation ratio is 0.1:1; the length of the coke tower feed position from the lower end of the cylinder accounts for 7 / 10 of the entire cylinder length; the washing oil The mass ratio of injection amount to fresh coking raw material feed is 0.05:1, and the mass ratio of the upper layer oil of the settling tank from pipeline 20 in the washing oil to the partial fractionation tower bottom oil from pipeline 22 is 4:1; the cooling oil and demineralized water The weight ratio is 0.3:1, a...
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