Electrostatic separation device, process and slurry purification device for removing solid particles in catalytic cracking oil slurry
A technology of catalytic cracking oil slurry and electrostatic separation, which is applied in the petroleum industry, processing hydrocarbon oil, and through electric/magnetic refining, etc. It can solve the problems of increased operational difficulty, large property differences, and increased medium conductivity, and achieves improved The effect of removing rate and electrostatic separation efficiency, increasing electrostatic adsorption capacity, and enhancing polarization
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Embodiment 1
[0061] refer to figure 1 and figure 2 As shown, the present embodiment provides a catalytic cracking oil slurry electrostatic separation device, which includes an electrostatic separator 3, the electrostatic separator 3 is composed of a casing 13, a high voltage power supply 4, a raw material distributor 2, an electrostatic field area, and a left head 16 And right head 17 forms. The heated catalytic cracking oil slurry is evenly distributed in the electrostatic field area through the raw material distributor 2 to polarize the oil slurry, so that the solid particles gather and grow on the electrode plate, and are adsorbed on the electrode surface, and gravity sedimentation occurs, and then from the catalytic cracking Separation and removal from cracked oil slurry.
[0062] Specifically, refer to figure 1 and figure 2 As shown, the raw material enters the raw material distributor 2 through the raw material inlet 1 provided at the bottom of the shell 13, and the raw materia...
Embodiment 2
[0079] This embodiment provides an example of purifying heavy oil catalytic cracking oil slurry using the purification device shown in Embodiment 1.
[0080] The density of heavy oil catalytic cracking oil slurry in Refinery 1# is 1.0256g / cm 3 , the solid particle content is 2550μg / g, the oil slurry is heated to 160°C, and then enters the electrostatic separator for purification treatment. The electrostatic separation time is 60min, and the voltage is AC DC12000V. Sampling and analysis are carried out every 60min. The test results are shown in the table 1.
[0081] From the test results, after the catalytic oil slurry is purified, micron and submicron particles are removed, the solid particle removal rate exceeds 98%, and the solid particle content is ≤50μg / g, which meets the requirements of deep purification, and the oil The pulp recovery rate can reach 95%. In addition, the device can realize continuous and stable operation.
[0082] Table 1 The effect of electrostatic sep...
Embodiment 3
[0085] This embodiment provides an example of purifying heavy oil catalytic cracking oil slurry using the purification device shown in Embodiment 1.
[0086] The density of heavy oil catalytic cracking slurry in refinery 2# is 1.1359g / cm 3 , the solid particle content is 4230μg / g, the oil slurry is heated to 170°C, and then enters the electrostatic separator for purification treatment. The electrostatic separation time is 90min, and the voltage is DC13000V. Sampling and analysis are carried out every 90min. The test results are shown in Table 2 .
[0087] According to the test results, after the catalytic oil slurry is purified, the solid particle removal rate exceeds 99%, and the solid particle content is ≤20μg / g, which meets the requirements of deep purification, and the recovery rate of the oil slurry can reach 95%. In addition, the The device can realize continuous and stable operation.
[0088] Table 2 The effect of electrostatic separation and purification of 2# oil sl...
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