Delayed coking system and delayed coking process
A delayed coking and process technology, applied in non-catalytic thermal cracking, cracking, petroleum industry and other directions, can solve the problems of complex improvement, easy coking in the wax oil section, and insufficient liquid recovery effect, and achieve the effect of improving product quality.
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Embodiment 1
[0032] figure 1 The delayed coking system 100 provided by Embodiment 1 of the present invention is shown, including a coke tower 101, an oil and gas flash tank 102, a fractionation tower 103, a first oil and gas pipeline 104 and a second oil and gas pipeline 105, and the coke tower 101 passes through the first oil and gas pipeline 104 communicates with the oil-gas flash tank 102, and the oil-gas flash tank 102 communicates with the fractionation tower 103 through the second oil-gas pipeline 105. The oil-gas flash tank 102 is provided with a quenching system 106, and the quenching system 106 is used to provide Quenching oil, the quenching oil is used to cool and wash the oil and gas generated by the coke tower 101 and enters the oil-gas flash tank 102 .
[0033] In the present embodiment, one end of the first oil and gas pipeline 104 communicates with the top of the coke tower 101, and the other end communicates with the bottom of the oil and gas flash tank 102 (limited by 1 / 2 ...
Embodiment 2
[0042] figure 2 Shown is the delayed coking system 200 provided by Embodiment 2 of the present invention. The setting of the second oil-gas pipeline 201 of this embodiment is different from that of Embodiment 1, and the spraying amount of the quenching oil in the oil-gas flash tank 102 is related to the delayed Except that the mass ratio of the feed amount of the coking system 200 is 0.3:1.0, other settings are the same as in the first embodiment.
[0043] In this embodiment, the second oil and gas pipeline 201 includes a tank top pipeline 202 and a tank bottom pipeline 203. The top of the oil and gas flash tank 102 communicates with the upper part of the fractionation tower 103 through the tank top pipeline 202, and the bottom of the oil and gas flash tank 102 passes through the tank. The bottom line 203 communicates with the lower part of the fractionation column 103 . The "upper part" and "lower part" mentioned here are bounded by 1 / 2 of the vertical height of the oil and...
Embodiment 3
[0047] Embodiment 3 of the present invention provides a delayed coking system, wherein the mass ratio of the spraying amount of the quenching oil in the oil-gas flash tank 102 to the feed amount of the delayed coking system 200 is 0.1:1, except that other settings and implementation Example 2 is the same. In addition, the gauge pressure of the oil-gas flash tank 102 is preferably 10-170 kPa, and in this embodiment, the gauge pressure is 130 kPa.
[0048] The temperature of the oil that enters the oil-gas flash tank 102 from the coke tower 101 is higher, and the pressure is also larger, and in the present embodiment, the pressure inside the oil-gas flash tank 102 is controlled within a small range, so that the oil-gas flash tank 102 The total pressure is small, so the partial pressure of the oil and gas is also small. Under the condition of constant reaction temperature and circulation ratio, this setting can reduce the residual amount of heavy hydrocarbons, reduce the coke yie...
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