Oily material suitable for producing needle coke as well as preparation method and system thereof
A technology of needle coke and oil quality, which is applied in the petroleum industry and the treatment of hydrocarbon oil, etc. It can solve the problems of short residence time, application limitations, difficulty in meeting the requirements of sulfur content in coking wax oil, etc., and achieve the effect of retaining content and reducing concentration
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[0023] The first aspect of the present invention provides a method for preparing an oily material suitable for producing needle coke, the method comprising:
[0024] 1) Send the raw oil 1 to the fractionation tower 2 for fractionation treatment to obtain the crude wax oil component 5 and the fractionation tower bottom heavy oil component 6;
[0025] 2) The crude wax oil component 5 and the first steam 7 are sent to the first stripper 8 for the first stripping treatment to obtain the first stripped light components 9 and the first stripper bottom oil 10;
[0026] 3) The fractionation tower bottoms heavy oil component 6, the first stripper bottom oil 10 and the second steam 13 are sent to the second stripper 12 for the second stripping treatment to obtain the second stripped light group Point 15 and the second stripper bottom oil 14;
[0027] 4) The first stripping light component 9 and the second stripping light component 15 are separated into wax oil light component 19 rich ...
Embodiment 1
[0078] This example is used to illustrate the preparation method of the oily material suitable for producing needle coke according to the present invention.
[0079] use figure 1 The system shown performs the manufacturing process described below.
[0080] (1) Feedstock oil 1 is sent in fractionating tower 2, and fractionating condition is: fractionating tower top temperature is 126 ℃, and fractionating tower top pressure is 0.15MPa, and fractionating tower bottom temperature is 332 ℃ to carry out fractionation treatment, and Separate and obtain gasoline 3, diesel oil 4, crude wax oil component 5 (that is, distillate oil with a distillation range of 350-450° C.) and fractionation tower bottom heavy oil component 6;
[0081] (2) The fourth stripper bottom oil 27 that the crude wax oil component 5 and the tower bottom of the fourth stripper 24 is discharged merges to obtain mixed oil 28 and is sent to the first stripper 8 and enters the first The steam 7 is subjected to the fi...
Embodiment 2
[0088] This example is used to illustrate the preparation method of the oily material suitable for producing needle coke according to the present invention.
[0089] According to the method described in embodiment 1, the difference is:
[0090] In step (2), the conditions for the first stripping treatment include: the temperature is 330°C, the gauge pressure is 0.15MPa, and the residence time is 1.5h; the crude wax oil component 5, the fourth stripper bottom oil 27 and The weight ratio of the amount of the first steam 7 is 100:10:5;
[0091] In step (3), the conditions of the second stripping treatment include: the temperature is 350°C, the gauge pressure is 0.15MPa, and the residence time is 1h; The weight ratio is 100:5;
[0092] In step (4), the conditions for the third stripping treatment include: the temperature is 300°C, the gauge pressure is 0.12MPa, and the residence time is 1h; the weight ratio of the mixed oil 16 and the third steam 17 is 100:10;
[0093] In step ...
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