Method and device for controlling the quality of coking mixed oil
A technology for mixed oil and coking heavy oil, which is applied in tar processing, coking carbonaceous materials, and chemical processing of tar asphalt/petroleum asphalt/natural asphalt, etc. It can solve the problems of impurities and affecting the quality of coking mixed oil, and achieve The effect of using less
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Embodiment 1
[0028] The control device for the quality of coking mixed oil in the production of coal series needle coke, such as figure 1 As shown, it consists of a coking tower 1, a swirl-type two-phase flow separation tower 2, a fractionation tower 3 and a heating furnace 4, and the gas outlet of the coking tower 1 is connected to the swirl-flow two-phase flow separation tower 2 through a pipeline , the gas outlet of the swirling two-phase flow separation tower 2 is connected with the fractionation tower 3 through a pipeline, and the bottom of the fractionation tower 3 is connected with the heating furnace 4 through a pipeline, and the heating furnace 4 is connected with the heating furnace 4 through a pipeline. The feed ports of the coking tower 1 are connected by pipelines.
Embodiment 2
[0030] The method for controlling the quality of coking mixed oil in the production of coal-based needle coke described in this example is as follows: figure 2 shown, including the following steps:
[0031] (1) When the production feed of the coking tower is delayed for 6 hours, the high-temperature coking oil gas at 435°C from the top of the coking tower enters the high-temperature swirling two-phase flow separation tower in a tangential direction, and the tangential introduction of the airflow causes rotational movement.
[0032] (2) Spray 223kg / h of coking heavy oil on the upper part of the high-temperature swirl-type two-phase flow separation tower to control the gas outlet temperature at the top of the swirl-type two-phase flow separation tower, and separate high polymers and micron-sized solid particles from oil and gas, The purified high-temperature coking oil gas is discharged from the top of the high-temperature swirling two-phase flow separation tower, and the heavy...
Embodiment 3
[0040] The method for controlling the quality of coking mixed oil in the production of coal-based needle coke described in this embodiment includes:
[0041] (1) When the production feed of the coking tower is delayed for 10 hours, the high-temperature coking oil gas at 439 °C from the top of the coking tower enters the high-temperature swirling two-phase flow separation tower along the tangential direction.
[0042](2) Spray 236kg / h of coking heavy oil on the upper part of the high-temperature swirl-type two-phase flow separation tower to control the gas outlet temperature at the top of the swirl-type two-phase flow separation tower, and to separate high polymers and micron-sized solid particles from oil and gas, The purified high-temperature coking oil gas is discharged from the top of the high-temperature swirling two-phase flow separation tower, and the heavy oil containing polymers and micron-sized solid particles is discharged from the tower and used as fuel oil. The puri...
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