Work starting method for coal tar hydrotreatment technique
A technology for hydrotreating and coal tar, which is applied in tar processing, petroleum industry, refining hydrocarbon oil, etc., and can solve problems not involved in the start-up of devices
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Embodiment 1
[0016] This example is a method for starting the plant after hydrotreating the heavy fraction of coal tar at -1 , then the reaction temperature was raised to 230°C at 10°C / h, constant temperature vulcanization for 8h, and then the reaction temperature was raised to 360°C at 10°C / h, constant temperature vulcanization for 8 hours, and then the 300 Coked diesel oil at -350°C is pumped into the reactor with a space velocity of 1.2h -1 , the volume ratio of hydrogen to oil is 1000, run at a constant temperature for 200 hours, and finally adjust the temperature to the reaction temperature to feed coal tar raw materials. The device starts normally and runs smoothly.
Embodiment 2
[0018] This example is a method for starting up the device after hydrotreating the whole fraction of coal tar by using a fixed bed. The specific operation process is: after the reactor bed of the device is heated to 150°C, the aviation kerosene containing 1.5v% carbon disulfide is pumped to the reactor with a space velocity of 1.0h -1 , then raise the reaction temperature to 230°C at 10°C / h, vulcanize at constant temperature for 8 hours, then raise the reaction temperature to 360°C at 10°C / h, vulcanize at constant temperature for 8 hours, and then directly add polyoxyethylene ether containing 3wt% fatty alcohol The 350-500 ℃ catalytic back refining pump is sent into the reactor with a space velocity of 1.0h -1 , the volume ratio of hydrogen to oil is 1500, run at a constant temperature for 300 hours, and finally adjust the temperature to the reaction temperature to feed coal tar raw materials. The device starts normally and runs smoothly.
Embodiment 3
[0020] This example is a method for starting up the device after hydrotreating coal tar distillate oil at -1 , then raise the reaction temperature to 230°C at 10°C / h, vulcanize at constant temperature for 8 hours, then raise the reaction temperature to 360°C at 10°C / h, vulcanize at constant temperature for 8 hours, then adjust the temperature to the reaction temperature, and then The 350-400 ℃ coking wax oil pump of 4wt% alkylphenol polyoxyethylene ether is sent into the reactor, and the space velocity is 1.0h -1 , the volume ratio of hydrogen to oil is 1000, run at a constant temperature for 100 hours, and finally pump the coal tar raw material into the reactor device. The device starts normally and runs smoothly.
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